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Небесная энциклопедия

Космические корабли и станции, автоматические КА и методы их проектирования, бортовые комплексы управления, системы и средства жизнеобеспечения, особенности технологии производства ракетно-космических систем

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Мониторинг СМИ

Мониторинг СМИ и социальных сетей. Сканирование интернета, новостных сайтов, специализированных контентных площадок на базе мессенджеров. Гибкие настройки фильтров и первоначальных источников.

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Применить Всего найдено 1286. Отображено 195.
19-12-2019 дата публикации

СПОСОБЫ И СИСТЕМЫ ДЛЯ УЛУЧШЕНИЯ ЭКСПЛУАТАЦИОННЫХ ХАРАКТЕРИСТИК ОХЛАЖДАЮЩЕГО БАССЕЙНА И ПРОИЗВОДСТВА СОЛИ В ОПЕРАЦИИ ДОБЫЧИ РАСТВОРЕНИЕМ

Номер: RU2709686C2
Принадлежит: ДЗЕ МОЗАИК КОМПАНИ (US)

Изобретение относится к системам охлаждения бассейнов для извлечения соли из раствора соли, более конкретно к регулированию глубины охлаждающего бассейна и помещению одного или нескольких затопленных водосливов. Включение одного или нескольких затопленных водосливов в существующую систему охлаждающих бассейнов может уменьшать температуру выходящего потока на 1-5°F по сравнению с такой же системой охлаждающих бассейнов без каких-либо затопленных водосливов. В качестве дополнения или в качестве альтернативы глубина бассейна может регулироваться для улучшения перемешивания потока и конвекционного охлаждения. Когда температура уменьшается во всей системе охлаждающих бассейнов, содержащие калий соли в большем количестве осаждаются из концентрированного соляного раствора, приводя к увеличению производства или извлечения в пределах той же области охлаждения. Изобретение обеспечивает улучшение охлаждающей способности в системе охлаждающих бассейнов с использованием одного или нескольких затопленных ...

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29-05-2020 дата публикации

РЕЛЬСОВОЕ ТРАНСПОРТНОЕ СРЕДСТВО С УСТРОЙСТВОМ ОЧИСТКИ СТОЧНЫХ ВОД

Номер: RU197807U1

Полезная модель относится к рельсовому транспортному средству с устройством (1) для очистки сточных вод, содержащему, по меньшей мере, один испаритель (2) для испарения сточной воды посредством подвода тепловой энергии и перетекающего воздуха, при этом воздух отбирается из рельсового транспортного средства. РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 197 807 U1 (51) МПК B61D 35/00 (2006.01) C02F 1/04 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ПОЛЕЗНОЙ МОДЕЛИ К ПАТЕНТУ (52) СПК B61D 35/00 (2020.02); C02F 1/04 (2020.02) (21)(22) Заявка: 2019136879, 27.04.2018 (24) Дата начала отсчета срока действия патента: Дата регистрации: (73) Патентообладатель(и): СИМЕНС МОБИЛИТИ ГМБХ (DE) 29.05.2020 (56) Список документов, цитированных в отчете о поиске: DE 4200296 A1, 15.07.1993. DE 102004028036 A1, 05.01.2006. EP 1401548 B1, 13.10.2004. SU 1654151 A1, 07.06.1991. DE 102013205084 B3, 28.05.2014. DE 102014220666 A1, 14.04.2016. 24.05.2017 DE 10 2017 208 852.4 (45) Опубликовано: 29.05.2020 Бюл. № 16 (85) Дата начала рассмотрения заявки PCT на национальной фазе: 18.11.2019 1 9 7 8 0 7 Приоритет(ы): (30) Конвенционный приоритет: R U 27.04.2018 (72) Автор(ы): КЕЛЕМЕН, Маттиас (DE), ШНАЙДЕР, Кристиан (DE), УНГЕРЕР, Маркус (DE) (86) Заявка PCT: EP 2018/060851 (27.04.2018) U 1 (87) Публикация заявки PCT: Адрес для переписки: 101000, Москва, ул. Мясницкая, д. 13, стр. 5, ООО "Союзпатент" (54) РЕЛЬСОВОЕ ТРАНСПОРТНОЕ СРЕДСТВО С УСТРОЙСТВОМ ОЧИСТКИ СТОЧНЫХ ВОД (57) Реферат: Полезная модель относится к рельсовому воды посредством подвода тепловой энергии и транспортному средству с устройством (1) для перетекающего воздуха, при этом воздух очистки сточных вод, содержащему, по меньшей отбирается из рельсового транспортного мере, один испаритель (2) для испарения сточной средства. R U 1 9 7 8 0 7 U 1 WO 2018/215165 (29.11.2018) Стр.: 1 U 1 U 1 1 9 7 8 0 7 1 9 7 8 0 7 R U R U Стр.: 2 RU 5 10 15 20 25 30 35 40 45 197 807 U1 Полезная модель относится к рельсовому ...

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10-04-2008 дата публикации

УСТРОЙСТВО ДЛЯ РАЗБРЫЗГИВАНИЯ ЖИДКОСТИ И СПОСОБ И СИСТЕМА ДЛЯ ОПРЕСНЕНИЯ СОЛЕНОЙ ВОДЫ, ИСПОЛЬЗУЮЩИЕ УКАЗАННОЕ УСТРОЙСТВО ДЛЯ РАЗБРЫЗГИВАНИЯ ЖИДКОСТИ

Номер: RU2006135152A
Принадлежит:

... 1. Устройство для разбрызгивания жидкости, содержащее форсунку с рабочей камерой, канал для подвода жидкости в указанную рабочую камеру форсунки, на выходе которой имеется сопло, и генератор давления, отличающееся тем, что генератор давления представляет собой импульсный генератор давления, причем указанный генератор давления установлен внутри рабочей камеры форсунки и соединен с генератором электрических или электромагнитных импульсов.2. Устройство по п.1, отличающееся тем, что между рабочей камерой форсунки и ее соплом имеется кольцевая камера, сообщающаяся по меньшей мере с двумя акустическими резонаторами, представляющими собой полости.3. Устройство по п.2, отличающееся тем, что указанные акустические резонаторы равномерно разнесены по окружности.4. Устройство по п.2, отличающееся тем, что каждый резонатор включает в себя группу полостей, каждая из которых рассчитана на собственную частоту колебаний.5. Устройство по п.2, отличающееся тем, что указанные полости выполнены с возможностью ...

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30-06-2011 дата публикации

Sprinkler irrigation stripping module for removing volatile solute substance from groundwater stream, comprises two vacuum-pressure-resistant sprinkler irrigation columns in water through flow direction connected in series

Номер: DE102009055182A1
Принадлежит:

The sprinkler irrigation stripping module for removing volatile solute substance from groundwater stream, comprises two vacuum-pressure-resistant sprinkler irrigation columns in water flow direction connected in series, where each sprinkler irrigation column comprises a water distributor- and gas collection unit in a head part and a gas distributor and water collection unit in the bottom part. Packing body (2) is arranged between the head part and the bottom part into the sprinkler irrigation column. A carrier gas system is provided with a vacuum pump system. The sprinkler irrigation stripping module for removing volatile solute substance from groundwater stream, comprises two vacuum-pressure-resistant sprinkler irrigation columns in water flow direction connected in series, where each sprinkler irrigation column comprises a water distributor- and gas collection unit in a head part and a gas distributor and water collection unit in the bottom part. Packing body (2) is arranged between the ...

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30-05-2012 дата публикации

Systems and methods for concentrating waste water fluids

Номер: GB0002485961A
Принадлежит:

The invention relates to a method and apparatus for processing waste water generated during oilfield drilling operations with a mobile processing unit utilizing heat energy sourced from burning hydrocarbon fuel directly and/or capturing and using the exhaust heat energy generated by burning hydrocarbons in engines such as diesel engines in order to vaporize a dominant mass of the aqueous phase of the waste water while clarifying the heat source combustion gasses. The water vapor generated by the vaporization process may be discharged directly to the atmosphere or alternately condensed and captured for use as potable water. The residual waste water is thereby concentrated and the cost to dispose of the waste water is greatly reduced.

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19-01-2022 дата публикации

Compact containerized system and method for spray evaporation of water

Номер: GB0002597168A
Принадлежит:

A wastewater evaporation system for spray evaporating water comprising: a wastewater feed inlet; a pump, wherein an outlet of the wastewater inlet is fluidly connected to the pump and wherein the pump is fluidly connected a manifold; a drip orifice, wherein the manifold is fluidly connected to the drip orifice; a container, wherein an upper portion of the container is enclosed with a demister element; a packing and/or tray system disposed within the container, wherein the drip orifice discharges water droplets onto the packing and/or tray system; a discharge outlet, wherein a bottom of the container is fluidly connected to the discharge outlet; and an air system wherein the air system discharges air flow counter to the water droplets from the drip orifice. A method of spray evaporating water while limiting emission of particles regulated as pollutants is also disclosed.

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28-02-2011 дата публикации

Water purification device and method.

Номер: AP2011005558A0
Принадлежит:

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31-12-2012 дата публикации

A desalination unit for the production of potable water from sub-soil brine

Номер: AP2012006553A0
Принадлежит:

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31-01-2014 дата публикации

Method ans system for removal of dissolved organiccompounds in process water

Номер: AP2014007380A0
Автор: SOGAARD DENNIS
Принадлежит:

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31-12-2012 дата публикации

A desalination unit for the production of potable water from sub-soil brine

Номер: AP0201206553D0
Принадлежит:

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31-01-2014 дата публикации

Method ans system for removal of dissolved organiccompounds in process water

Номер: AP0201407380A0
Автор: SOGAARD DENNIS
Принадлежит:

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31-12-2012 дата публикации

A desalination unit for the production of potable water from sub-soil brine

Номер: AP0201206553A0
Принадлежит:

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28-02-2011 дата публикации

Water purification device and method.

Номер: AP0201105558A0
Принадлежит:

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15-05-2011 дата публикации

SEAWATER DESALINATION PROCEDURE AND - DEVICE

Номер: AT0000506326T
Принадлежит:

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23-10-2008 дата публикации

Apparatus for purifying contaminated liquid

Номер: AU2008238608A1
Принадлежит:

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18-06-2009 дата публикации

Multipurpose adiabatic potable water production apparatus and method

Номер: AU2005250900B2
Принадлежит:

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25-11-2010 дата публикации

Method and apparatus for separating caustic soda and fresh water from seawater by using green energy

Номер: AU2010200189B1
Принадлежит:

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09-10-2014 дата публикации

Device for generating drinking water by condensing water vapour generated in an evaporation device

Номер: AU2011252335B2
Принадлежит:

The invention relates to a device for generating drinking water by condensing water vapour, comprising an acceleration pressure pipe (19) that can be arranged vertically and a suction chamber (64) adjoining the upper end of the acceleration pressure pipe (19). The water vapour introduced into the acceleration pressure pipe (19) is driven, similarly to a thundercloud, upwards inside the acceleration pressure pipe, wherein in addition steam is injected via lateral steam nozzles (29) and water is injected via lateral water injection nozzles (28). The injected water is withdrawn from the water that is generated in the suction chamber (64) from the condensed water vapour.

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18-05-2017 дата публикации

Compact waste water concentrator and contaminant scrubber

Номер: AU2017202735A1
Принадлежит: Shelston IP Pty Ltd.

The invention provides a wastewater concentrating and contaminant removal system comprising: a gas inlet; a gas outlet; a concentrating section disposed between the gas inlet and the gas outlet, the concentrating section having a narrowed portion in which gas flow within the concentrating section accelerates; a liquid inlet through which wastewater is injected into the concentrating section, the liquid inlet being disposed in the concentrating section upstream of the narrowed portion; a demister disposed downstream of the narrowed portion, the demister removing entrained liquid droplets from the gas flow; and wherein the concentrating section is adapted to be connected to a sequential mixing and settling tank, a reagent tank that holds a supply of reagent being connected to the sequential mixing and settling tank. Fig. 3 134 CONTROLLER 308- 1313 3V12 315 19 196 14193 177 175 172 317 122 ...

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28-03-2019 дата публикации

FLUID TREATMENT SYSTEMS AND METHODS

Номер: CA0003075259A1
Принадлежит: MILTONS IP/P.I.

A system for concentrating wastewater with a heated gas is disclosed wherein a heated gas directed into a first wastewater heating chamber at a first velocity and a first wastewater stream is directed into the first wastewater heating chamber. A second wastewater heating chamber coupled to the first wastewater heating chamber and in fluid communication with the first wastewater heating chamber. A second wastewater stream is directed into the second wastewater heating chamber at a velocity that greater than the velocity of the heated gas directed into the first wastewater heating chamber.

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24-03-2011 дата публикации

SYSTEMS AND METHODS FOR CONCENTRATING WASTE WATER FLUIDS

Номер: CA0002751895A1
Принадлежит:

The invention relates to a method and apparatus for processing waste water generated during oilfield drilling operations with a mobile processing unit utilizing heat energy sourced from burning hydrocarbon fuel directly and/or capturing and using the exhaust heat energy generated by burning hydrocarbons in engines such as diesel engines in order to vaporize a dominant mass of the aqueous phase of the waste water while clarifying the heat source combustion gasses. The water vapor generated by the vaporization process may be discharged directly to the atmosphere or alternately condensed and captured for use as potable water. The residual waste water is thereby concentrated and the cost to dispose of the waste water is greatly reduced.

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23-01-2014 дата публикации

THERMODYNAMIC BALANCING OF COMBINED HEAT AND MASS EXCHANGE DEVICES

Номер: CA0002875826A1
Принадлежит: BORDEN LADNER GERVAIS LLP

A carrier-gas mixture is directed through a fluid flow path (16, 18) in a combined heat and mass transfer device (12, 14), which can be operated at sub-atmospheric pressure. Heat and mass are transferred from/ to the carrier-gas mixture via interaction with a liquid composition including a vaporizable component in a liquid state to substantially change the content of the vaporizable component in the carrier-gas mixture via evaporation or condensation. The mass flow rate of the carrier-gas mixture is varied by extracting/injecting (60, 62, 64) the carrier-gas mixture from at least one intermediate location in the fluid flow path, and/or the mass flow rate of the liquid composition is varied by extracting/injecting the liquid composition from at least one intermediate location in the fluid flow path. The flow of the carrier-gas mixture or the liquid composition is regulated to reduce the average local enthalpy pinch.

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14-07-2017 дата публикации

Low-temperature distillation plant.

Номер: CH0000712029A1
Автор: MARKUS LEHMANN
Принадлежит:

Die Erfindung betrifft eine Nieder-Temperatur-Destillationsanlage (LTD-Anlage) (1) zur Destillierung einer Mischflüssigkeit (5) zu einer reinen Flüssigkeit (6). Die LTD-Anlage weist einen Verdampfer (2) mit einem Dampfraum (4) und mit einer wärmeren einbringbaren Mischflüssigkeit (5) sowie einen Kondensor (3) mit einem Dampfraum (4) und mit einer kühleren einsprühbaren reinen Flüssigkeit (6) auf, wobei die Dampfräume (4) des Verdampfers (2) und des Kondensors (3) durch Dampfverbindungen (10) miteinander zu einem gemeinsamen Dampfraum (4) verbunden sind. Erfindungsgemäss umfasst die LTD-Anlage mindestens eine Aggregatseinrichtung (14), welche eingangsseitig mit dem Dampfraum einer Unterkühlkammer (15) verbunden ist, wobei in die Unterkühlkammer (15) aufgefangene Mischflüssigkeit (5) aus einem Verdampfer (2) einbringbar ist. Ausgangsseitig ist die Aggregatseinrichtung (14) mit dem Dampfraum einer Überhitzekammer (16) verbunden, wobei in die Überhitzekammer (16) aufgefangene reine Flüssigkeit ...

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29-04-2011 дата публикации

УСТАНОВКА ДЛЯ ОЧИСТКИ ВОДЫ

Номер: EA0201000640A1
Принадлежит:

Задача изобретения заключается в обеспечении очистки воды, в частности получения дистиллированной воды, в промышленном объеме на технологичном оборудовании, которое может быть использовано в составе газоперекачивающего агрегата для транспортировки природного газа, использующего газотурбинную установку с отводом выхлопных газов через шахту выхлопа, которые как правило, оборудованы утилизаторами тепла для разогрева воды. Либо в составе иных систем, предусматривающих эксплуатацию стационарных газовых турбин с организацией отвода выхлопных газов через шахты выхлопа. Технология очистки воды, в том числе решение задачи только обессоливания, не предусматривает использование каких-либо дополнительных химических компонентов, отходы удаляются без каких-либо особых трудозатрат и на оборудование не распространяются требования, предъявляемые к безопасности эксплуатации сосудов высокого давления. Установка содержит герметичный полый парообразователь 1, выполненный для подачи в верхнюю часть пара с возможностью ...

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29-04-2011 дата публикации

УСТАНОВКА ДЛЯ ОЧИСТКИ ВОДЫ

Номер: EA0000015066B1

Задача изобретения заключается в обеспечении очистки воды, в частности получения дистиллированной воды, в промышленном объеме на технологичном оборудовании, которое может быть использовано в составе газоперекачивающего агрегата для транспортировки природного газа, использующего газотурбинную установку с отводом выхлопных газов через шахту выхлопа, которые, как правило, оборудованы утилизаторами тепла для разогрева воды, либо в составе иных систем, предусматривающих эксплуатацию стационарных газовых турбин с организацией отвода выхлопных газов через шахты выхлопа. Технология очистки воды, в том числе решение задачи только обессоливания, не предусматривает использование каких-либо дополнительных химических компонентов, отходы удаляются без каких-либо особых трудозатрат и на оборудование не распространяются требования, предъявляемые к безопасности эксплуатации сосудов высокого давления. Установка содержит герметичный полый парообразователь 1, выполненный для подачи в верхнюю часть пара с возможностью ...

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10-03-2015 дата публикации

COMPACT CONCENTRATOR WASTEWATER AND SCRUBBER

Номер: UA0000107956C2
Принадлежит:

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21-12-2018 дата публикации

Towerless deaerator

Номер: CN0109052535A
Автор: XIAO PENGYUAN
Принадлежит:

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12-07-2019 дата публикации

DEVICE FOR EVAPORATING/CONDENSING

Номер: FR0002975479B1
Принадлежит:

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23-11-2012 дата публикации

DEVICE Of EVAPORATION/CONDENSATION

Номер: FR0002975479A1
Автор: TREMEL LAURENT
Принадлежит: MONTPELLIER ENGINEERING

Dispositif (10) d'évaporation/condensation comprenant : un condenseur (12) ; des moyens d'alimentation (14) en gaz du condenseur (12) adaptés pour alimenter le condenseur (12) avec un gaz (G1) à une première température (T1) ; et des moyens d'alimentation (16) en liquide du condenseur (12) adaptés pour alimenter le condenseur (12) avec un liquide (L1) à une deuxième température (T2) inférieure à la première température (T1), le condenseur (12) étant adapté pour mettre en contact direct le gaz (G1) et le liquide (L1) de manière à condenser le gaz (G1), caractérisé en ce qu'il comprend : un évaporateur (42) ; des moyens d'alimentation (44) en gaz de l'évaporateur (42) adaptés pour alimenter l'évaporateur (42) avec un gaz (G2) à une troisième température (T3) ; et des moyens d'alimentation (46) en liquide de l'évaporateur (42) adaptés pour alimenter l'évaporateur (42) avec un liquide (L2) à une quatrième température (T4) supérieure à la troisième température (T3), l'évaporateur (42) étant ...

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10-10-2013 дата публикации

SPRAY-DRYING DEVICE FOR DEHYDRATED FILTRATE FROM DESULFURIZATION WASTEWATER, EXHAUST GAS TREATMENT SYSTEM AND METHOD

Номер: KR1020130111572A
Автор:
Принадлежит:

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09-03-2006 дата публикации

EVAPORATION CHAMBER USED FOR SINGLE STAGE FLUSH EVAPORATION METHOD SEAWATER DESALINATION APPARATUS BY MECHANICAL VAPOR COMPRESSION METHOD

Номер: WO2006025117A1
Автор: KISHI, Masahiro
Принадлежит:

An evaporation chamber (3) used for a single stage flush evaporation method desalination apparatus by a mechanical vapor compression method which is disposed at a position higher than a heat exchange means (4) to provide a head difference (H) equal to or more than a difference between a saturated pressure at the temperature of a vapor (2) and a pressure in the evaporation chamber (3) to the heat exchange means (4) so as to hold the pressure of a brine in the separately installed heat exchange means (4) at a level equal to or more than the saturated pressure at the temperature of the vapor (2) leaving a mechanical vapor compression means (6) even when the circulation of the brine is stopped. The evaporation chamber comprises a nozzle (5) formed such that the cross section of a flow passage is gently reduced along a flow so that a part of the static pressure of the brine flowing into the evaporation chamber (3) can be efficiently changed to a dynamic pressure with a speed component in the ...

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15-12-2005 дата публикации

MULTIPURPOSE ADIABATIC POTABLE WATER PRODUCTION APPARATUS AND METHOD

Номер: WO2005119146A1
Автор: MERRITT, Thomas
Принадлежит:

Apparatus and methods for transforming water vapor into potable water by using a vapor compression refrigeration system which includes first and second cooling elements disposed in a closed loop air passage duct that provides a continuous air circulation pattern driven by a fan or IS-002 (PCT) similar device. Water is introduced into the circulating air and undergoes adiabatic cooling followed by two stage cooling, first at a temperature below the dew point and then at a lower temperature at or below freezing. Water is collected from the air in each step and the air is thereafter heated back up by the condensing element of the refrigeration system enabling it to absorb more water vapor at the point of introduction. The air is recirculated and processed as above to permit cyclical water recovery.

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20-09-2012 дата публикации

SEPARATION APPARATUS, AND SEPARATION METHOD

Номер: WO2012124550A1
Автор: MATSUURA, Kazuo
Принадлежит:

In order to minimize the energy required when implementing a separation technique by means of atomization, a separation apparatus is provided with: an atomization chamber (10) that atomizes a solution so as to produce a gas containing fine particles; a classifier (20) that classifies fine particles; a first tube (1) connecting the atomization chamber (10) and the classifier (20); a recovery tank (30) that condenses and recovers the gas containing fine particles; a second tube (2) connecting the classifier (20) and the recovery tank (30); and a third tube (3) connecting the recovery tank (30) and the atomization chamber (10). A blower (40) that pressurizes the gas exists midway along the second tube (2), and a pressure recovery device (50) and a heat exchanger (60), which straddle the second tube (2) and the third tube (3), are also provided. Pressure generated in the blower (40) is transferred from the gas in the third tube (3) to the gas in the second tube (2) by the pressure recovery ...

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10-03-2020 дата публикации

Water treatment system

Номер: US0010584041B2

The present disclosure relates a system for the treatment of water. The water treatment system may be linked an aquatic protection system or a water filtration system.

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21-12-2011 дата публикации

COMPACT WASTEWATER CONCENTRATOR USING WASTE HEAT

Номер: EP2396279A2
Принадлежит:

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19-12-2012 дата публикации

WATER TREATMENT PROCESS

Номер: EP2534104A1
Принадлежит:

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10-10-2008 дата публикации

УСТРОЙСТВО ДЛЯ РАЗБРЫЗГИВАНИЯ ЖИДКОСТИ И СПОСОБ ИСИСТЕМА ДЛЯ ОПРЕСНЕНИЯ СОЛЕНОЙ ВОДЫ, ИСПОЛЬЗУЮЩИЕУКАЗАННОЕ УСТРОЙСТВО ДЛЯ РАЗБРЫЗГИВАНИЯ ЖИДКОСТИ

Номер: RU2335345C2

Изобретение относится к устройству для разбрызгивания жидкости и к способу и устройству для опреснения соленой воды разбрызгиванием, в которых использовано указанное устройство для разбрызгивания жидкости. Устройство для разбрызгивания жидкости содержит форсунку с рабочей камерой, канал для подвода жидкости в указанную рабочую камеру форсунки, на выходе которой имеется сопло, и генератор давления. Генератор давления представляет собой импульсный генератор давления, установленный внутри рабочей камеры форсунки и соединенный с генератором электрических или электромагнитных импульсов. Техническим результатом изобретений является эффективное испарение капель, повышение эффективности процесса, достижение оптимального режима испарения, а также повышение производительности системы. 3 н. и 16 з.п. ф-лы, 5 ил.

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27-06-2012 дата публикации

СПОСОБ УДАЛЕНИЯ ФОСФОРА И МАГНИЯ ПРИ ОЧИСТКЕ СТОЧНЫХ ВОД АКТИВИРОВАННЫМ ИЛОМ И СИСТЕМА ВЫДЕЛЕНИЯ СТРУВИТА

Номер: RU2454374C2

Изобретение относится к способу очистки сточных вод илом. Система выделения струвита включает: первый осветлитель для получения первого ила и потока органических отходов из сточных вод; ферментер для ферментации органических отходов в потоке сточных вод для получения ферментированного ила и первый загуститель для загущения ферментированного ила; при этом ферментер и первый загуститель совместно образуют легко биоразлагаемые углеродсодержащие соединения из органических стоков в потоке сточных вод; аэротенк для реакций углеродсодержащих соединений из первого загустителя с твердыми материалами, суспендированными в смешанной жидкости, причем аэротенк соединен со вторым осветлителем, на выходе из которого получают активированный ил; сепаратор, соединенный с первым загустителем и вторым осветлителем, для получения потока, обогащенного фосфором и магнием, и отдельного потока, обедненного фосфором и магнием; реактор для ферментативного разложения, соединенный с сепаратором, для разложения потока ...

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10-10-2014 дата публикации

КОМПАКТНЫЙ КОНЦЕНТРАТОР СТОЧНЫХ ВОД, РАБОТАЮЩИЙ НА ОТБРОСНОМ ТЕПЛЕ

Номер: RU2530045C2

Изобретение относится к концентраторам жидкости, а точнее к компактным передвижным недорогим концентраторам сточных вод, которые легко можно подключать к источникам отбросного тепла и использовать их для концентрирования жидкости. Компактный передвижной концентратор жидкости содержит газовпускной патрубок, газовыпускное отверстие и проточный канал, соединяющий газовпускной патрубок и газовыпускное отверстие, причем проточный канал содержит суженный участок, который увеличивает скорость протекания газа по проточному каналу. Впускной патрубок жидкости впрыскивают жидкость в поток газа перед суженным участком таким образом, чтобы газожидкостная смесь полностью перемешивалась в проточном канале, вызывая частичное испарение жидкости. Туманоуловитель или газопромывной аппарат за суженным участком удаляет из потока газа унесенные им капельки жидкости и возвращает собранную жидкость во впускной патрубок жидкости по рециркуляционному контуру. Свежую жидкость, поступившую на концентрирование, также ...

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27-12-2009 дата публикации

СИСТЕМА ТРУДОПРОВОДОВ

Номер: RU2008125141A
Принадлежит:

... 1. Система трубопроводов, включающая в себя ! первый трубопровод, проходящий от источника соленой воды, для переноса соленой воды через него, ! по меньшей мере, один опреснитель соленой воды, соединенный по текучей среде с первым трубопроводом, что обеспечивает перемещение соленой воды из первого трубопровода к, по меньшей мере, одному опреснителю, ! каждый опреснитель соленой воды выполнен для опреснения, по меньшей мере, части воды, перемещенной из первого трубопровода, ! каждый опреснитель соединен по текучей среде со вторым трубопроводом, проходящим между каждым соответствующим опреснителем и целевым выходом так, что опресненная вода, которая опресняется в опреснителе, передается к второму трубопроводу, ! при этом, по меньшей мере, один опреснитель включает в себя опреснительную камеру, причем каждая камера включает в себя впуск воздуха, выполненный с возможностью при использовании подачи в камеру воздушного потока для генерации, в основном незавихренного, воздушного потока внутри камеры ...

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27-10-2013 дата публикации

СИСТЕМА И СПОСОБ КОНЦЕНТРИРОВАНИЯ СТОЧНЫХ ВОД

Номер: RU2012115489A
Принадлежит:

... 1. Выпарная установка для концентрирования загрязнений в неочищенной воде, содержащая:выпариватель неочищенной воды, включающий дымоход, подсоединенный к источнику горячего газа, представляющего собой газообразные продукты горения;систему распределения неочищенной воды для ее распределения внутри дымохода с увеличением площади поверхности; исистему сбора концентрированной неочищенной воды, подсоединенную к дымоходу для сбора концентрированной неочищенной воды из дымохода.2. Выпарная установка по п.1, дополнительно содержащая первый бак, функционально соединенный с выпаривателем неочищенной воды и предназначенный для приема и хранения неочищенной воды и концентрированной неочищенной воды.3. Выпарная установка по п.2, в которой в первом баке возможно расслоение неочищенной воды.4. Выпарная установка по п.3, в которой неочищенная вода имеет поверхность жидкости в первом баке и дополнительно содержащая заборный шланг, приспособленный плавать так, чтобы всасывать неочищенную воду из-под поверхности ...

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07-01-2009 дата публикации

Desalination method

Номер: GB0000821884D0
Автор:
Принадлежит:

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27-09-2006 дата публикации

Wastewater evaporation system

Номер: GB0002424377A
Принадлежит:

The water evaporation apparatus functions to increase the concentration strength of a contaminant solution. A blower 64 conveys an air stream along an air-conduit, over a nozzle or atomizer 32. The atomizer converts the incoming dilutely-contaminated water into fine droplets, and inject and distributes the droplets into the airstream. An air-heater 43 is located upstream of the atomizer, and heats the airstream to a temperature of 110�C at the atomizer. A droplet-collector 45 receives the airstream, and the droplets, and mechanically extracts the liquid droplets from the airsteam. The airstream leaves the droplet-collector at 65�C in a saturated condition. The droplets coalesce, and become the final-water 30, compriusing the strongly concentrated contaminant solution. An exhaust-conduit 28 conveys air that has passed through the droplet-collector to the air-outlet. A heat-exchanger 42 transfers heat from the exhaust airstream into the intake airstream, to supplement the air-heater.

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12-03-2020 дата публикации

Water management system

Номер: AU2018309556A1

An outdoor water management system including at least one reservoir configured to receive highly concentrated contaminated water, a weather proof cover, covering the reservoir to define at least one chamber and water vapour removal means, configured to remove evaporated water from the at least one chamber wherein the at least one chamber is configured to further concentrate the contaminated water while providing long-term weatherproof storage thereof.

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03-12-2020 дата публикации

Evaporator for ambient water bodies, and related system and method

Номер: AU2019253043A1
Принадлежит: FPA Patent Attorneys Pty Ltd

An evaporator is provided for evaporating water from an ambient body of water having a water surface. The evaporator includes a housing that has a proximal end proximate to the water surface, a distal end distal to the water surface, and a housing air flow channel directed toward the water surface. The housing is disposed on a support, such as a float assembly, that positions the housing above the water surface. The evaporator also includes an air flow induction device, preferably an impeller, disposed to direct an air flow stream from the distal end toward the proximal end through the housing air flow channel and toward the water surface so that the air contacts the water. The impeller preferably is made of a fiberglass material. The support preferably includes at least one float assembly air flow channel that receives the air flow stream from the housing and directs it outwardly from the evaporator. Water injection devices such as spray nozzles or atomizing nozzles preferably are disposed ...

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17-11-2011 дата публикации

Waste activated sludge phosphorus and magnesium stripping process and struvite production system

Номер: AU2009209439B2
Принадлежит:

A method of treating a mixture of microorganisms with readily biodegradable carbon compounds (RBCs) in the form of one or more volatile fatty acids (VFAs), by first inducing the mixture microorganisms to release phosphorus and magnesium which is then tapped o as the mixture is thickened, to produce a phosphorus/magnesium-nch liquid and a phosphorus/magnesium-reduced treated mixture This treated mixture is placed in an anaerobic digester where ammonia is formed, but combines very little with phosphorus or magnesium Next the high-ammonia mixture is dewatered to produce an ammonia-rich liquid, which is combined with the phosphorus and magnesium-rich liquid and reacted to form struvite In one preferred embodiment, VFAs are formed in situ via an upstream unified fermentation and thickening (UFAT) process and added to the waste sidestream to strip phosphorus and magnesium found therein In another preferred embodiment a usable struvite product is harvested.

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02-05-2013 дата публикации

Apparatus for purifying contaminated liquid

Номер: AU2008238608B2
Принадлежит:

An apparatus (10) for purifying contaminated liquid includes an airflow means (15) for creating an airstream. A disperser (19) creates droplets of the contaminated liquid in the airstream. A heater (30) is disposed upstream of the disperser (19) for heating the airstream. The apparatus (10) is operable within a range of predetermined conditions to cause only partial evaporation of water from a substantial proportion of the droplets. A condenser (22) is provided for condensing the evaporated water. The condenser (22) is spaced downstream from the heater (30) and/or the disperser (19) such that under the predetermined conditions, the droplets settle out of the air under gravity prior to reaching the condenser (22). A method of purifying contaminated liquid is also disclosed. The apparatus (10) may include multiple evaporation chambers (12) with a single return air duct (13). The apparatus (10) may have a closed airflow circuit defined by two elongate portions (12, 13) and two end sections ...

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30-04-2020 дата публикации

Fluid treatment systems and methods

Номер: AU2018335139A1
Принадлежит: FB Rice Pty Ltd

A system for concentrating wastewater with a heated gas is disclosed wherein a heated gas directed into a first wastewater heating chamber at a first velocity and a first wastewater stream is directed into the first wastewater heating chamber. A second wastewater heating chamber coupled to the first wastewater heating chamber and in fluid communication with the first wastewater heating chamber. A second wastewater stream is directed into the second wastewater heating chamber at a velocity that greater than the velocity of the heated gas directed into the first wastewater heating chamber.

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03-10-2020 дата публикации

METHOD TO SEPARATE AND REMOVE FLUORIDE FROM LITHIUM MINERAL SPRING WATER

Номер: CA0003038923A1
Автор: PAN GEORGE, PAN, GEORGE
Принадлежит: DEL VECCHIO, ORIN

A method for removing natural high concentrations of fluoride from natural lithium mineral spring water. The method including artificially concentrating the spring water where the calcium fluoride is precipitated and removed, leaving behind a solution with high concentrated lithium dissolved in it. This method includes providing natural lithium spring water and prepurified with sand and carbon filter to remove dirt, algea, odour, etc. A concentrated water solution or a powder product is created from the aqueous solution using water concentration processes. The concentrated water solution has a high concentration of lithium still dissolved therein and most of the calcium fluoride being precipitated due to CaF2 has much lower water solubility. Using a separation process, the precipitated calcium fluoride is removed from the concentrated water solution. This high concentration lithium solution is then diluted to the desired concentration for bottling.

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17-10-2019 дата публикации

EVAPORATOR FOR AMBIENT WATER BODIES, AND RELATED SYSTEM AND METHOD

Номер: CA0003096874A1
Принадлежит: RIDOUT & MAYBEE LLP

An evaporator is provided for evaporating water from an ambient water body. The evaporator includes a housing that in turn includes an air flow channel and an air flow exit. The evaporator also includes an air flow induction device, such as a fan or impeller, that facilitates the directing of an air flow stream through the air flow channel and out the air flow exit. A water injection device is in fluid communication with the air flow channel and is disposed to inject the water from the water body into the air flow stream at a water injection location within the air flow stream and proximate to the air flow exit. A water injection system for injecting water from an ambient water body into an air flow stream directed by an air flow channel of an evaporator also is disclosed, wherein the air flow channel is disposed about a longitudinal axis. The water injection system includes an elongated tubular member disposed parallel with respect to the longitudinal axis, a plurality of water injection ...

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24-10-2019 дата публикации

METHOD AND SYSTEM FOR DRYING MINE TAILINGS

Номер: CA3097086A1
Принадлежит:

A method and system to treat and dry fines tailings generated from mining operations, comprising spraying the tailings material into a vacuum chamber operated at less than atmospheric pressure to separate evaporated water from the residual solid materials.

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16-02-2017 дата публикации

APPARATUS, SYSTEMS AND METHODS FOR MANAGEMENT OF RAW WATER AND EMISSIONS UTILIZING HEAT AND/OR PRESSURE ENERGY WITHIN COMBUSTION GAS SOURCES

Номер: CA0002994872A1
Принадлежит:

The invention relates to methods, systems and apparatus for distributed management of raw water and internal combustion engine (ICE) gas emissions generated during industrial operations. One aspect of the invention at least partially utilizes a hot gas air knife to increase or partially increase surface area between a raw water and a hot gas in order to vaporize a proportion of the aqueous phase of the raw water and concentrate contaminants within a residual raw water concentrate. The water vapor generated by the vaporization process may be demisted, discharged directly to the atmosphere or alternatively condensed and captured for use. Another aspect relates to how the liquids and gasses interact to continuously flush the surfaces of the system which may help mitigate scaling issues. The invention may help facilitate rapid transfer of ICE combustion gas particulate and ICE combustion gas chemicals onto and into the raw water as it concentrates.

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06-08-2009 дата публикации

WASTE ACTIVATED SLUDGE PHOSPHORUS AND MAGNESIUM STRIPPING PROCESS AND STRUVITE PRODUCTION SYSTEM

Номер: CA0002686114A1
Автор: BAUR, ROBERT, BAUR ROBERT
Принадлежит:

A method of treating a mixture of microorganisms with readily biodegradab le carbon compounds (RBCs) in the form of one or more volatile fatty acids ( VFAs), by first inducing the mixture microorganisms to release phosphorus an d magnesium which is then tapped o as the mixture is thickened, to produce a phosphorus/magnesium-nch liquid and a phosphorus/magnesium-reduced treated mixture This treated mixture is placed in an anaerobic digester where ammoni a is formed, but combines very little with phosphorus or magnesium Next the high-ammonia mixture is dewatered to produce an ammonia-rich liquid, which i s combined with the phosphorus and magnesium-rich liquid and reacted to form struvite In one preferred embodiment, VFAs are formed in situ via an upstre am unified fermentation and thickening (UFAT) process and added to the waste sidestream to strip phosphorus and magnesium found therein In another prefe rred embodiment a usable struvite product is harvested.

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31-05-2007 дата публикации

A PIPELINE SYSTEM

Номер: CA0002630582A1
Принадлежит:

A desalination pipeline system (10) including a first pipeline (12) extending from a salt water source (14) for transferring salt water therethrough. The system includes at least one salt water desalinator (18) in fluid connection with the first pipeline (12), enabling salt water to be drawn from the first pipeline (12) to the at least one desalinator (18). Each of the salt water desalinators (18) is provided to desalinate at least part of the water drawn from the first pipeline (12). Each desalinator (18) is in fluid connection with a second pipeline (24) extending between the salt water source (14) and the target outlet (16), such that the water that has been desalinated in a desalinator (18) is transferred to the second pipeline (24).

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01-04-2014 дата публикации

METHOD, APPARATUS AND SYSTEM FOR CONCENTRATING SOLUTIONS USING EVAPORATION

Номер: CA0002816746C

The present disclosure is directed at a system, apparatus and method for concentrating a solution. The system includes a humidification device and a solution flow path for flow of a solution to be concentrated to the humidification device. The humidification device includes humidification media to facilitate evaporation of liquid from the solution to be concentrated to gas as the solution to be concentrated passes through the humidification media thereby concentrating the solution. The method includes flowing a solution to be concentrated along a flow path to a humidification device including humidification media, flowing a gas through the humidification media, and flowing the solution to be concentrated through the humidification media. There is evaporation of liquid from the solution to the gas as the solution passes through the humidification media thereby concentrating the solution and producing a humidified gas. The solution to be concentrated may be salt water and the gas may be air ...

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30-06-2014 дата публикации

METHOD AND DEVICE FOR REMOVING DISSOLVED ORGANIC COMPOUNDS FROM TECHNICAL WATER

Номер: EA0201490309A1
Автор:
Принадлежит:

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22-08-2012 дата публикации

Desalination

Номер: CN0101743204B
Автор: GARTH DAVEY, DAVEY GARTH
Принадлежит:

A desalination process comprising heating brine in a preheating chamber and transferring the brine to a rotary kiln to be sprayed against the wall structure of the rotary kiln to boil to steam and a residue of salt/impurities, the exiting steam being pressurised in a compressor and passed to an externally powered heater to be heated and then fed to a hollow wall structure of the rotating kiln in which the steam condenses to pure water to be transferred to the preheating chamber to preheat the incoming brine, the rotating kiln being arranged to rotate past a scraper to remove salt/impurities from the wall structure for collection at the base of the kiln.

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23-07-2010 дата публикации

Desalination and purification of wastewater, comprises filtrating water, fragmentizing water droplets to form system of drops, evaporating the water contained in the drops, and separating vapors and crystal salts in cyclone system

Номер: FR0002941224A1
Автор: UGOLIN NICOLAS
Принадлежит: UGOLIN NICOLAS

Cette invention consiste en un système permettant d'utiliser l'énergie calorifique d'origine solaire couplée à l'énergie électromagnétique, notamment des micro-ondes, et éventuellement les énergies produites durant la fermentation des produits organiques (biomasse, eaux usées) pour produire de l'eau douce à partir d'eaux salées, d'eaux usées, et de la vapeur d'eau contenue dans l'atmosphère. L'eau douce produite sera éventuellement rendue potable par ajout de sels minéraux à la concentration souhaitée provenant éventuellement de la cristallisation de sel lors de l'épuration. L'invention décrit un procédé et des réacteurs combinant des étapes de chauffage solaire et électromagnétique et éventuellement d'échanges thermiques avec un gaz chaud provenant d'une combustion, pour réaliser l'évaporation des gouttelettes d'un spray produit à partir d'eaux salées ou usées. La vapeur obtenue est séparée des particules de sels ou des impuretés agglomérées lors de l'évaporation par un système de cyclones ...

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26-07-2013 дата публикации

DEVICE OF NEBULATION Of a LIQUID

Номер: FR0002985919A1
Принадлежит: CHING, RENGGLI, PALLANCA

Le dispositif (100) de nébulisation d'un liquide comporte une cuve (110) ouverte dans sa partie supérieure et apte à contenir le liquide à nébuliser, au moins deux générateurs (120, 130) d'ondes ultrasonores destinés à émettre au moins deux fronts (122, 132) d'ondes ultrasonores dans le liquide, au moins deux moyens (134, 124) pour focaliser des ondes ultrasonores, coopérants chacun avec un dit générateur (120, 130) pour concentrer des ondes ultrasonores en un même point P à moins de dix millimètres de la surface libre du liquide.

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06-12-2012 дата публикации

SPRAY DRYING APPARATUS FOR FILTRATE FROM DESULFURIZATION WASTE WATER, AND EXHAUST GAS TREATMENT SYSTEM

Номер: WO2012165508A1
Принадлежит:

This spray drying apparatus is equipped with: a gas inlet (52) that is provided in a side wall (51b) in the vicinity of the top (lid) (51a) of the spray drying apparatus (50A), and introduces an exhaust gas (18) for drying a spray (33a) of filtrate (33); flow-adjusting panels (53) that are provided within the body of the spray drying apparatus to alter the flow of exhaust gas to a laminar flow (X) and decelerate the introduced exhaust gas (18); a spray nozzle for spraying the filtrate (33) from the desulfurization waste water (30) into the exhaust gas (18) that has a laminar flow (X); a gas discharge port (55) that is provided in a side wall (51c) in the vicinity of the bottom of the spray drying apparatus and discharges the exhaust gas (18) that contributed to the drying of the filtrate (33); and a discharge hopper (57) that is provided on the bottom-side of the spray drying apparatus and serves as a solids eliminating means for eliminating spray-dried solids such as ash (56).

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26-05-2006 дата публикации

LOW ENERGY VACUUM DISTILLATION METHOD AND APPARATUS

Номер: WO000002006055548A3
Принадлежит:

A subatmospheric pressure desalinating still employs a closed top, open bottom pipe filled with source water to be distilled, such as seawater, having a height greater than the height of a column of seawater that can be supported by the pressure at the bottom of the tank so that a subatmospheric pressure volume is formed at the top. Water from the source is also pumped into the subatmospheric volume and passed through an evaporator which enlarges its surface volume. A small percentage of the water is vaporized and the balance is cooled to provide the heat of vaporization and falls into the top of the seawater column, creating a downward flow. The vapor is drawn from the vacuum and condensed, preferably in a second subatmospheric volume above a column of fresh water. A degasser for the water to be distilled prevents the accumulation of gases dissolved in the seawater or the like in the subatmospheric volume.

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25-02-2010 дата публикации

METHOD FOR THE DESALINATION OR PURIFICATION OF WATER BY DISTILLATION OF A SPRAY (SPRAY PUMP)

Номер: WO2010020723A3
Автор: UGOLIN, Nicolas
Принадлежит:

The invention relates to a system enabling the use of solar heat energy together with electromagnetic energy, in particular microwaves, and optionally energy produced during the fermentation of organic products (biomass, wastewater) in order to produce fresh water from salt water, wastewater and water vapour contained in the atmosphere. The resulting fresh water can optionally be rendered drinkable by adding mineral salts at the desired concentration, said salts optionally originating from salt crystallisation during purification. The invention relates to a method and reactors combining electromagnetic and solar heating steps and optionally heat exchanges with a hot gas originating from a combustion, in order to evaporate droplets of a spray produced from salt water or wastewater. The vapour obtained is separated from the salt particles or agglomerated impurities during evaporation using a cyclone system. The vapour can then be transported over a large distance before being condensed by ...

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20-07-2006 дата публикации

LOW ENERGY VACCUM DISTILLATION METHOD AND APPARATUS

Номер: WO000002006076056A3
Принадлежит:

A sub-atmospheric pressure desalinating still employs a closed top, open bottom pipe filled with source water to be distilled, such as seawater, having a height greater than the height of a column of seawater that can be supported by the pressure at the bottom of the tank so that a subatmospheric pressure volume is formed at the top. Water from the source is also pumped into the subatmospheric volume and passed through an evaporator which enlarges its surface volume. A small percentage of the water is vaporized and the balance is cooled to provide the heat of vaporization and falls into the top of the seawater column, creating a downward flow. The vapor is drawn from the vacuum and condensed, preferably in a second subatmospheric volume above a column of fresh water.

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04-10-2012 дата публикации

Systems And Methods For Concentrating Waste Water Fluids

Номер: US20120247942A1
Принадлежит:

A method and apparatus for processing waste water generated during oilfield drilling operations with a mobile processing unit utilizing heat energy sourced from burning hydrocarbon fuel directly and/or capturing and using the exhaust heat energy generated by burning hydrocarbons in engines such as diesel engines in order to vaporize a dominant mass of the aqueous phase of the waste water while clarifying the heat source combustion gasses. The water vapor generated by the vaporization process may be discharged directly to the atmosphere or alternately condensed and captured for use as portable water. The residual waste water is thereby concentrated and the cost to dispose of the waste water is greatly reduced.

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25-02-2020 дата публикации

Low-temperature distillation plant

Номер: US0010569188B2

A low-temperature distillation facility for distilling a mixed fluid into a pure fluid. An aggregation device has an inlet connected to the vapour space of a supercooling chamber, wherein captured mixed fluid from an evaporator enters the supercooling chamber. The aggregation device's outlet is connected to the vapour space of a superheating chamber, wherein captured pure fluid from a condenser can be sprayed into the superheating chamber. An energy source cools the temperature in the supercooling chamber and heats the temperature in the superheating chamber. A heat exchanger is arranged between the exits of the supercooling chamber and of the superheating chamber. During the process, vapour flows from the supercooling chamber via the aggregation device to the superheating chamber.

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03-07-2014 дата публикации

METHOD AND SYSTEM FOR REMOVAL OF DISSOLVED ORGANIC COMPOUNDS IN PROCESS WATER

Номер: US20140183131A1
Принадлежит: PURETEQ A/S

The present invention relates to a method for removal of dissolved organic compounds, in particular bioaccumulative substances, in process water (eg. of the petrochemial industry) and to a system for carrying out the inventive method. Process water containing toxic and/or bioaccumulative substances is mixed in the mixing vessel (2) with an extractant. The resulting emulsion is directed into a separation vessel (3) to separate the aqueous phase from the organic phase. The aqueous phase is directed into a first distillation unit (5), where vaporisation of the extractant is carried out. The organic phase is directed to a second distillation unit (7). The resulting distillate is recirculated via a condenser unit (8) into the mixing vessel (2).

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13-09-2023 дата публикации

ENERGY SAVING DESALINATION SYSTEM

Номер: EP3553031B1
Автор: WENG, Lin Song

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20-01-2016 дата публикации

УСТАНОВКА И СПОСОБ КОНЦЕНТРИРОВАНИЯ ЗАГРЯЗНЕНИЙ В СТОЧНЫХ ВОДАХ

Номер: RU2573471C2

Изобретение относится к обработке сточных вод с использованием установки, использующей тепловую энергию, получаемую при прямом сжигании углеводородного топлива и/или путем использования тепловой энергии отработавших газов, образующихся присжигании углеводородов в двигателях. Выпарная установка для концентрирования загрязнений в неочищенной воде содержит выпариватель 110 неочищенной воды, включающий дымоход, подсоединенный к источнику горячего газа; систему распределения неочищенной воды внутри дымохода с увеличением ее площади поверхности; систему управления, включающую по меньшей мере один пункт контроля для мониторинга температуры внутри дымохода и по меньшей мере один насос для регулирования потока неочищенной воды, направляемого в систему распределения неочищенной воды; и систему сбора, подсоединенную к дымоходу для сбора воды с концентрированными загрязнениями из дымохода. Изобретение позволяет сократить количество загрязнений в отработавших газах, которые могут быть выпущены в атмосферу ...

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25-04-2019 дата публикации

Номер: RU2017125371A3
Автор:
Принадлежит:

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20-03-2014 дата публикации

КОМПАКТНЫЙ КОНЦЕНТРАТОР СТОЧНЫХ ВОД И ГАЗООЧИСТИТЕЛЬ

Номер: RU2012137951A
Принадлежит:

... 1. Способ удаления загрязняющих веществ из воды отработки скважины природного газа, в котором используется концентратор сточных вод, включающий отверстие ввода газа, отверстие выпуска газа и секцию концентрирования между отверстием ввода газа и отверстием выпуска газа, обладающую сужающейся частью, включающий:смешивание реактива с водой отработки скважины природного газа, реакцию реактива с химическими соединениями, растворимыми в воде отработки скважины с образованием нерастворимого химического соединения;объединение газа и воды отработки скважины в секции концентрирования с образованием смеси газа с захваченной водой отработки скважины, которая содержит нерастворимое химическое соединение;подачу смеси газа с захваченной водой отработки скважины в каплеуловитель, в котором, по меньшей мере, часть захваченной воды отработки скважины удаляется из газа и собирается в отстойнике каплеуловителя;удаление части воды отработки скважины в отстойник каплеуловителя и подача части воды отработки скважины ...

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09-09-2019 дата публикации

УСТРОЙСТВО, СИСТЕМЫ И СПОСОБЫ УПРАВЛЕНИЯ НЕОЧИЩЕННОЙ ВОДОЙ И ВЫБРОСАМИ С ИСПОЛЬЗОВАНИЕМ ЭНЕРГИИ ТЕПЛА И/ИЛИ ДАВЛЕНИЯ В ИСТОЧНИКАХ ДЫМОВОГО ГАЗА

Номер: RU2018108138A

РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2018 108 138 A (51) МПК B01D 1/14 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ЗАЯВКА НА ИЗОБРЕТЕНИЕ (21)(22) Заявка: 2018108138, 08.08.2016 (71) Заявитель(и): КЛИНТЕК ИНДАСТРИС ИНК. (CA) Приоритет(ы): (30) Конвенционный приоритет: 07.08.2015 US 62/202,663 (85) Дата начала рассмотрения заявки PCT на национальной фазе: 07.03.2018 R U (43) Дата публикации заявки: 09.09.2019 Бюл. № 25 (72) Автор(ы): КЁРЛЕТТ Джошуа (CA), ВАНЛЕН Юг (CA) (86) Заявка PCT: (87) Публикация заявки PCT: WO 2017/024398 (16.02.2017) R U (54) УСТРОЙСТВО, СИСТЕМЫ И СПОСОБЫ УПРАВЛЕНИЯ НЕОЧИЩЕННОЙ ВОДОЙ И ВЫБРОСАМИ С ИСПОЛЬЗОВАНИЕМ ЭНЕРГИИ ТЕПЛА И/ИЛИ ДАВЛЕНИЯ В ИСТОЧНИКАХ ДЫМОВОГО ГАЗА (57) Формула изобретения 1. Адаптер для соединения источника газа от соответствующего источника газа с системой для испарения неочищенной воды (СИНВ), содержащий: газовую трубу, содержащую газовый соединитель на впускном отверстии для соединения трубы с трубопроводом источника газа; воздушный нож на выходном конце газовой трубы, причем газовая труба имеет выходное отверстие для соединения с камерой сдвига слоев СИНВ, выполненное с возможностью направления по меньшей мере части газа в газовой трубе внутрь камеры сдвига слоев для осуществления сдвига слоев неочищенной воды. 2. Адаптер по п. 1, выполненный с возможностью сужения потока газа, которое позволяет увеличивать скорость газа на выходном отверстии по сравнению со скоростью на впускном отверстии адаптера. 3. Адаптер по п. 1, в котором источник газа представляет собой одно или более из следующего: система выхлопных газов двигателя; система выхлопных газов ДВС; система выхлопных газов турбинного двигателя и дымовой газ от пламени. 4. Адаптер по п. 1, выполненный с возможностью соединения с системой газовых труб и включающий «У»-образную или «Т»-образную трубу, причем газовая труба включает: выпускной клапан, выполненный таким образом, что при его открытии обеспечена возможностью выпускания газа из ...

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10-12-2011 дата публикации

СПОСОБ УДАЛЕНИЯ ФОСФОРА И МАГНИЯ ПРИ ОЧИСТКЕ СТОЧНЫХ ВОД АКТИВИРОВАННЫМ ИЛОМ И СИСТЕМА ВЫДЕЛЕНИЯ СТРУВИТА

Номер: RU2010122665A
Принадлежит:

... 1. Способ переработки отходов, включающий: ! (a) получение первой смеси твердых материалов, микроорганизмов и жидкости из сточных вод, в которой микроорганизмы содержат фосфор и магний; ! (b) удаление фосфора и магния из микроорганизмов и растворение удаленного фосфора и магния в жидкой части первой смеси, причем стадия удаления включает добавление легко биоразлагаемых углеродсодержащих соединений к первой смеси с образованием обработанной смеси, содержащей растворенный магний и фосфор; ! (c) ферментацию и обогащение обработанной смеси с образованием обогащенной фосфором и магнием жидкости, которую отделяют от остальной смеси, обедненной фосфором и магнием; ! (d) анаэробную обработку смеси, обедненной фосфором и магнием, с образованием смеси, обогащенной аммиаком и обедненной фосфором и магнием; ! (e) обезвоживание обогащенной аммиаком смеси с образованием обогащенной аммиаком жидкости; и ! (f) смешение обогащенной аммиаком жидкости с обогащенной фосфором и магнием жидкостью с образованием ...

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21-05-2019 дата публикации

Способ предварительной обработки и активации воздухом морской воды перед ее опреснением

Номер: RU2688617C1

FIELD: water treatment. SUBSTANCE: invention relates to pretreatment of sea water before desalination in adiabatic multi-stage desalter by its hydrodynamic cavitation treatment and activation by atmospheric air. Initial sea water is supplied through tangential nozzles into internal part of hydrodynamic cavitation device, and due to formed rarefaction atmospheric air is introduced into it with formation of small air bubbles, which intensifies oxidation of chemical compounds contained in sea water, primarily sodium chloride and magnesium chloride. Thereafter, solid components are removed from the mechanical filter. Then purified sea water is supplied to adiabatic multi-stage distiller (evaporator). EFFECT: method of preliminary preparation of sea water with its purification before clarification. 1 cl РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 688 617 C1 (51) МПК C02F 1/04 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (52) СПК C02F 1/00 (2019.02); C02F 1/04 (2019.02); C02F 1/12 (2019.02); B01D 3/00 (2019.02); B01D 3/10 (2019.02); B05B 1/00 (2019.02); B05B 1/08 (2019.02) (21)(22) Заявка: 2018145335, 18.12.2018 18.12.2018 Дата регистрации: 21.05.2019 (73) Патентообладатель(и): федеральное государственное автономное образовательное учреждение высшего образования "Самарский национальный исследовательский университет имени академика С.П. Королёва" (RU), Акционерное общество "Металлист-Самара" (RU) (45) Опубликовано: 21.05.2019 Бюл. № 15 Адрес для переписки: 443086, г. Самара, Московское ш., 34, Самарский университет, управление обеспечения инновационной деятельности C 1 2 6 8 8 6 1 7 R U 2013315 C1, 30.05.1994. RU 2498158 C1, 10.11.2013. RU 2525177 C2, 10.08.2014. US 5207928 A1, 04.05.1993. US 6299735 B1, 09.10.2001. RU 2284966 C2, 10.10.2006. (54) Способ предварительной обработки и активации воздухом морской воды перед ее опреснением (57) Реферат: Изобретение относится к области мелких воздушных пузырьков, что ...

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30-05-2001 дата публикации

Method of treating waste water and apparatus for treating waste water using the method

Номер: GB0000109110D0
Автор:
Принадлежит:

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23-01-2002 дата публикации

Method of treating waste water and apparatus for the use of said method

Номер: GB0002364301A
Принадлежит:

A method for the treatment of waste water containing nitrogen-containing organic compounds comprises spraying the water into a heated space in order to gasify substantially all of the said waste water to waste gas. The gas is then oxidised by contacting with a catalyst to convert the gas into nitrogen, carbon dioxide and water vapour. The catalyst may comprise an oxide including titania and/or titania-silica, an oxide of at least one metal selected from vanadium, tungsten, molybdenum, cerium and iron, and at least one metal selected from platinum, palladium, iridium, rhodium, ruthenium, manganese, chromium, and copper, or an oxide thereof. Apparatus for performing the method is also disclosed.

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24-04-2014 дата публикации

A water atomisation device

Номер: AU2012238201A1
Принадлежит:

A WATER ATOMISATION DEVICE Abstract A water atomisation device (10) for water evaporation and/or dust control. The device (10) -includes: a generally longitudinally hollow housing (12); a fan (18); a motor (20); and a hollow manifold (22). The housing (12) extends between an inlet end (12a) and an outlet end (12b), with the inlet end (1 2a) defining a first air inlet to an interior of the housing (12). The fan (18) is within the housing (12), between the inlet end (12a) and the outlet end (12b). The motor (20) drives the fan (18). The manifold (22) is shaped to generally correspond to that of the outlet end (12b) and has a plurality of water injector nozzles (24) directed substantially inwardly and away from the outlet end (12b). A distal edge of the outlet end (12b) is longitudinally spaced apart from a proximal edge of the manifold (22) to define a second air entrainment inlet (25) to an interior of the manifold (22). d'% r-J C*4 ...

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20-02-2014 дата публикации

Method and system for removal of dissolved organic compounds in process water

Номер: AU2012285743A1
Принадлежит:

The present invention relates to a method for removal of dissolved organic compounds, in particular bioaccumulative substances, in process water (eg. of the petrochemial industry) and to a system for carrying out the inventive method. Process water containing toxic and/or bioaccumulative substances is mixed in the mixing vessel (2) wih an extractant. The resulting emulsion is directed into a separation vessel (3) to separate the aqueous phase from the organic phase. The aqueous phase is directed into a first distillation unit (5), where vaporisation of the extractant is carried out. The organic phase is directed to a second distillation unit (7). The resulting distillate is recirculated via a condenser unit (8) into the mixing vessel (2).

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05-02-2015 дата публикации

Thermodynamic balancing of combined heat and mass exchange devices

Номер: AU2013290626B2
Принадлежит:

A carrier-gas mixture is directed through a fluid flow path (16, 18) in a combined heat and mass transfer device (12, 14), which can be operated at sub-atmospheric pressure. Heat and mass are transferred from/ to the carrier-gas mixture via interaction with a liquid composition including a vaporizable component in a liquid state to substantially change the content of the vaporizable component in the carrier-gas mixture via evaporation or condensation. The mass flow rate of the carrier-gas mixture is varied by extracting/injecting (60, 62, 64) the carrier-gas mixture from at least one intermediate location in the fluid flow path, and/or the mass flow rate of the liquid composition is varied by extracting/injecting the liquid composition from at least one intermediate location in the fluid flow path. The flow of the carrier-gas mixture or the liquid composition is regulated to reduce the average local enthalpy pinch.

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22-03-2012 дата публикации

Water purifying device

Номер: AU2009349828A1
Принадлежит:

A water purifying device for efficiently producing purified water from raw water. A water purifying device is provided with a case (11) having a circulation route, a splitter device (15) provided in the case (11), breaking the raw water into liquid drops, and creating a carrier gas flow (A1) capable of circulating in the circulation route and of carrying water vapor evaporated from the liquid drops (D1), and a condenser (19) provided in the case (11) so as to be located on the carrier gas flow downstream of the splitter device (15) and condensing the water vapor to create purified water. The splitter device (15) has a rotating shaft (15a) extending in the top-bottom direction of the case (11), and also has blades (152A-152Q) mounted radially to the rotating shaft (15a) and provided with projections and recesses (152p, 152q, 152r, 152s, 152t).

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08-08-2019 дата публикации

A SYSTEM AND A METHOD FOR GENERATION AND DELIVERY OF THERMAL ENERGY

Номер: AU2019200317A1
Принадлежит: Baxter Patent Attorneys Pty Ltd

Abstract A system (1200) for delivery of thermal energy, comprises piping 5 (1202) for carrying a pressurized gas, the piping (1202) forming a closed loop and having an inlet for receiving the pressurized gas, one or more velocity and pressure enhancers (1208) connected along the piping (1202) and a heat exchanger (1206) connected along the piping (1202). The piping (1202) is configured to receive the pressurized gas via the inlet and 10 recirculate the pressurized gas inside the closed loop. The one or more velocity and pressure enhancers (1208) are configured to maintain flow, velocity and thermal energy of the pressurized gas to predetermined values of the flow, the velocity and the thermal energy, inside the closed loop. Also, the heat exchanger (1206) is configured to transfer at least a 15 part of the thermal energy of the pressurized gas to a process application. NOliVOIlddVSS30M~d -- --- -- N' ...

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30-01-2020 дата публикации

Thermal separation process and apparatus

Номер: AU2018299217A1
Принадлежит: Phillips Ormonde Fitzpatrick

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15-12-2016 дата публикации

CONTAINERIZED SYSTEM AND METHOD FOR SPRAY EVAPORATION OF WATER

Номер: CA0003018529A1
Принадлежит:

A system for spray evaporating water comprising: a wastewater inlet; a pump, where an outlet of the wastewater inlet is fluidly connected to an inlet of the pump and wherein an outlet of the pump is fluidly connected to an inlet of a manifold; a spray nozzle, wherein an outlet of the manifold is fluidly connected to an inlet of the spray nozzle; a container, wherein an upper portion of the container is enclosed with a demister element and wherein the outlet of the spray nozzle discharges into the container; and a discharge outlet, wherein a bottom of the container is fluidly connected to the discharge outlet. A method of spray evaporating water is also disclosed.

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05-03-2019 дата публикации

PROCESS TO OBTAIN THIN LAYERS OF DRIED AND CONSOLIDATED MATURE FINES TAILINGS

Номер: CA0003016259A1
Принадлежит: MLT AIKINS LLP

A process to treat fines tailings generated from mining operations, wherein tailings material is sprayed onto a solid substrate as a thin layer and allowed to dry. The spray may be re-applied on top of the dried tailings film leading to multiple layers of dried tailings solids. The method may yield a solid, dry, and consolidated tailings material.

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05-12-2010 дата публикации

APPARATUS AND METHOD FOR RECLAMATION OF TREATABLE WATER

Номер: CA0002678531A1
Принадлежит:

The present invention relates to an apparatus and method to reclaim water. The water that may be reclaimed begins as untreated treatable water, which is water having solids, particulates, or minerals not originally in the water. Untreated treatable water is also natural water having solids, particulates, or minerals that are undesired. The invention provides for removal of the totally dissolved solids from the water by micronizing the water in a chamber having a first temperature, and condensing the water in a second chamber having an interior surface that is cooled to the ambient wet-bulb temperature of the surrounding environment. Reclaimed treatable water from this invention becomes usable water.

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14-01-2014 дата публикации

METHOD, APPARATUS AND SYSTEM FOR CONCENTRATING SOLUTIONS USING EVAPORATION

Номер: CA0002821453C

The present disclosure is directed at a system, apparatus and method for concentrating a solution. The system includes a humidification device and a solution flow path for flow of a solution to be concentrated to the humidification device. The humidification device includes humidification media to facilitate evaporation of liquid from the solution to be concentrated to gas as the solution to be concentrated passes through the humidification media thereby concentrating the solution. The method includes flowing a solution to be concentrated along a flow path to a humidification device including humidification media, flowing a gas through the humidification media, and flowing the solution to be concentrated through the humidification media. There is evaporation of liquid from the solution to the gas as the solution passes through the humidification media thereby concentrating the solution and producing a humidified gas. The solution to be concentrated may be salt water and the gas may be air ...

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08-07-2014 дата публикации

METHOD, APPARATUS AND SYSTEM FOR CONCENTRATING SOLUTIONS USING EVAPORATION

Номер: CA0002821458C

The present disclosure is directed at a system, apparatus and method for concentrating a solution. The system includes a humidification device and a solution flow path for flow of a solution to be concentrated to the humidification device. The humidification device includes humidification media to facilitate evaporation of liquid from the solution to be concentrated to gas as the solution to be concentrated passes through the humidification media thereby concentrating the solution. The method includes flowing a solution to be concentrated along a flow path to a humidification device including humidification media, flowing a gas through the humidification media, and flowing the solution to be concentrated through the humidification media. There is evaporation of liquid from the solution to the gas as the solution passes through the humidification media thereby concentrating the solution and producing a humidified gas. The solution to be concentrated may be salt water and the gas may be air ...

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24-05-2007 дата публикации

RAPID NON-EQUILIBRIUM DECOMPRESSION OF MICROORGANISM-CONTAINING WASTE STREAMS

Номер: CA0002629315A1
Принадлежит:

A process for treating a microorganism-containing stream includes the steps of passing the stream (12) through a chamber (14), pressurizing the stream (12) in the chamber to a pressure greater than 14.7 p.s.i.g., introducing a feed gas (16) into the pressurized stream (12) such that the feed gas (16) is soluable within the microorganisms, and depressurizing the stream (12) so as to cause the soluablized feed gas (16) to expand within the microorganisms so as to rupture the cell walls of the microorganisms. The feed gas (16) can be carbon dioxide, air, nitrogen, methane, or mixtures thereof.

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06-11-2018 дата публикации

Desulfurization waste water zero-emission treatment device and treatment method

Номер: CN0108751306A
Принадлежит:

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16-07-2013 дата публикации

EXHAUST GAS PROCESSING SYSTEM AND METHOD, SPRAY-DRYING DEVICE AND METHOD FOR DEHYDRATED FILTRATE FROM DESULFURIZATION WASTEWATER

Номер: KR1020130081283A
Автор:
Принадлежит:

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19-08-2010 дата публикации

COMPACT WASTEWATER CONCENTRATOR USING WASTE HEAT

Номер: WO2010093958A3
Принадлежит:

A compact and portable liquid concentrator includes a gas inlet, a gas exit and a flow corridor connecting the gas inlet and the gas exit, wherein the flow corridor includes a narrowed portion that accelerates the gas through the flow corridor. A liquid inlet injects liquid into the gas stream at a point prior to the narrowed portion so that the gas-liquid mixture is thoroughly mixed within the flow corridor, causing a portion of the liquid to be evaporated. A demister or fluid scrubber downstream of the narrowed portion removes entrained liquid droplets from the gas stream and re-circulates the removed liquid to the liquid inlet through a re-circulating circuit. Fresh liquid to be concentrated is also introduced into the re-circulating circuit at a rate sufficient to offset the amount of liquid evaporated in the flow corridor.

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24-01-2013 дата публикации

METHOD AND SYSTEM FOR REMOVAL OF DISSOLVED ORGANIC COMPOUNDS IN PROCESS WATER

Номер: WO2013011129A2
Автор: SØGAARD, Dennis
Принадлежит:

The present invention relates to a method for removal of dissolved organic compounds, in particular bioaccumulative substances, in process water and to a system for carrying out the inventive method. A unique sequence of unit operations including the recycling of an organic extractant enables a particularly efficient removal of said substances from process water. The present method is particularly suited for treating process water of the petrochemical industry.

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15-10-2019 дата публикации

Systems and methods for concentrating waste water fluids

Номер: US0010441894B2
Принадлежит: CLEANTEK Industries Inc., CLEANTEK IND INC

A method and apparatus for processing waste water generated during oilfield drilling operations with a mobile processing unit utilizing heat energy sourced from burning hydrocarbon fuel directly and/or capturing and using the exhaust heat energy generated by burning hydrocarbons in engines such as diesel engines in order to vaporize a dominant mass of the aqueous phase of the waste water while clarifying the heat source combustion gasses. The water vapor generated by the vaporization process may be discharged directly to the atmosphere or alternately condensed and captured for use as potable water. The residual waste water is thereby concentrated and the cost to dispose of the waste water is greatly reduced.

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13-09-2018 дата публикации

METHODS AND SYSTEMS FOR ENHANCING COOLING POND PERFORMANCE AND SALT PRODUCTION IN A SOLUTION MINING OPERATION

Номер: US20180257000A1
Принадлежит: The Mosaic Company

A cooling pond system and related methods of improving cooling performance in a cooling pond system using one or more submerged dams to increase cooling performance within the cooling pond system, and increase salt precipitation or recovery. The inclusion of one or more submerged dams within an existing cooling pond system can reduce an outflow temperature by 1-5° F. as compared to the same cooling pond system without any submerged dams. In addition or alternatively, pond depth can be controlled to enhance flow mixing and convection cooling. As the temperature is reduced throughout the cooling pond system, more potassium containing salts are precipitated from the brine solution resulting in increased production or recovery within the same cooling footprint. 1. A cooling pond system , comprising:at least one cooling pond, the cooling pond having a brine inlet stream and an outlet stream, the cooling pond defining a pond length, a pond width and a pond depth; andat least one submerged dam positioned across at least a portion of the pond width, the at least one submerged dam having an upper dam surface located below a pond surface.2. The cooling pond system of claim 1 , wherein the at least one submerged dam extends fully across the pond width.3. The cooling pond system of claim 1 , wherein the at least one submerged dam extends only across a portion of the pond width claim 1 , said at least one submerged dam defining a dam opening.4. The cooling pond system of claim 1 , wherein the upper dam surface is positioned below the pond surface at a depth of about 1 foot to about 5 feet in depth.5. The cooling ponds system of claim 1 , wherein the pond is filled with a brine solution claim 1 , said brine solution wherein a more concentrated brine layer resides proximate a pond floor claim 1 , and wherein the at least one submerged dam causes an increase in the Reynolds number or vertical mixing of the brine solution such that the more concentrated brine layer is forced to the ...

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19-08-2004 дата публикации

Method and system for desalinating water

Номер: US2004159615A1
Автор:
Принадлежит:

A desalination system for removing at least a substantial amount of salt from a saltwater. In at least one embodiment, the desalination system may inject the saltwater with one or more ionized gases for removing contaminants from the saltwater. The desalination system may include one or more ionized gas generators for generating one or more ionized gases to be mixed with the saltwater. The desalination system may inject a disinfectant into the saltwater to disinfect the saltwater. The desalination system may generate one or more disinfectants from saltwater using a disinfectant generator. In at least one embodiment, the disinfectant generator may separate disinfectants from saltwater using electrolysis.

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02-07-2020 дата публикации

Water Treatment System and Method of Use Thereof

Номер: US20200207641A1
Принадлежит: Renew Health Limited

The present disclosure relates a system for the treatment of water. The water treatment system may be linked an aquatic protection system or a water filtration system. 1. A water treatment device , comprising:at least one tank;at least one heating element;at least one evaporator;at least one heat exchanger;at least one vacuum source;at least one power source; andat least one pump.2. The water treatment system of wherein said at least one vacuum source is a vacuum pump.3. The water treatment system of wherein said vacuum source is a supercharger.4. The water treatment system of wherein said evaporator is a plurality of plates.5. The water treatment system of wherein said plurality of plates have a thickness of from about 0.1 to 0.25 mm.6. The water treatment system of wherein said at least one heat exchangers is selected from the group of falling film type claim 1 , rising film type claim 1 , plate exchanger and combinations thereof.7. The water treatment system of further comprising a circulator placed within said at least one tank.8. The water treatment system of further comprising a baffle placed within said at least one tank9. The water treatment system of wherein said evaporator is a metal pipe.10. The water treatment system of wherein said water treatment system is linked to a second water treatment system.11. The water treatment system of wherein said water treatment system and second water system share a vacuum source.12. The water treatment system of wherein treatment of a source water with said water treatment system reduces total dissolved solids by at least 80%.13. The water treatment system of wherein treatment of a source water with said water treatment system reduces total dissolved solids by at least 90%.14. A system for treating salinated water claim 1 , comprising: at least one tank;', 'at least one heating element;', 'at least one evaporator;', 'at least one heat exchanger;', 'at least one vacuum source;', 'at least one power source;', 'at least ...

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12-07-2012 дата публикации

Water Purifying Apparatus

Номер: US20120175237A1
Автор: Takashi Yabe
Принадлежит: CIP SOFTWARE Co Ltd

Provided is a water purifying apparatus capable of efficiently producing purified water from raw water. The water purifying apparatus comprises: a casing ( 11 ) having a circulation path; a splitter device ( 15 ) disposed within the casing ( 11 ) and adapted to split raw water into droplets and create a carrier airflow (A 1 ) capable of circulating along the circulation path and carrying water vapor evaporated from the droplets (D 1 ); and a condenser ( 19 ) disposed within the casing ( 11 ) at a position downstream of the splitter device ( 15 ) in a direction of the carrier airflow and adapted to condense the water vapor to create purified water. The splitter device ( 15 ) comprises a rotary shaft ( 15 a ) extending in an up-down direction of the casing ( 11 ), and a blade ( 152 A to 152 Q) radially attached to the rotary shaft ( 15 a ) and having irregularities ( 152 p, 152 q, 152 r, 152 s, 152 t ).

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16-01-2014 дата публикации

Thermodynamic Balancing of Combined Heat and Mass Exchange Devices

Номер: US20140014212A1

A carrier-gas mixture is directed through a fluid flow path in a combined heat and mass transfer device, which can be operated at sub-atmospheric pressure. Heat and mass are transferred from or to the carrier-gas mixture via interaction with a liquid composition that includes a vaporizable component in a liquid state to substantially change the content of the vaporizable component in the carrier-gas mixture via evaporation or condensation. The mass flow rate of the carrier-gas mixture is varied by extracting or injecting the carrier-gas mixture from at least one intermediate location in the fluid flow path, and/or the mass flow rate of the liquid composition is varied by extracting or injecting the liquid composition from at least one intermediate location in the fluid flow path; and the flow of the carrier-gas mixture or the liquid composition is regulated to reduce the average local enthalpy pinch in the device.

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06-02-2014 дата публикации

Water Supply Systems

Номер: US20140034477A1
Автор: Mads Landrok
Принадлежит: Individual

A water supply system, the system comprising: an evaporation station, the evaporation station comprising a water inlet, an air conduit, and a water evaporation system coupled to the water inlet and to the air conduit for converting water from the water inlet into water vapour and for providing the water vapour onto the air conduit to provide humidified air; a condensation station having an air inlet to receive the humidified air, a water outlet, and a water condensation system coupled to the air inlet and to the water outlet to extract water from the humidified air and provide the extracted water to the water outlet; a pipe coupled between the air conduit of the evaporation station and air inlet of the condensation station; and a system for driving an airflow through the air conduit of the evaporation station past the water evaporation system to enhance the spray evaporation.

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13-02-2014 дата публикации

Compact wastewater concentrator using waste heat

Номер: US20140041811A1
Принадлежит: HEARTLAND TECHNOLOGY PARTNERS LLC

A compact and portable liquid concentrator includes a gas inlet, a gas exit and a flow corridor connecting the gas inlet and the gas exit, wherein the flow corridor includes a narrowed portion that accelerates the gas through the flow corridor. A liquid inlet injects liquid into the gas stream at a point prior to the narrowed portion so that the gas-liquid mixture is thoroughly mixed within the flow corridor, causing a portion of the liquid to be evaporated. A demister or fluid scrubber downstream of the narrowed portion removes entrained liquid droplets from the gas stream and re-circulates the removed liquid to the liquid inlet through a re-circulating circuit. Fresh liquid to be concentrated is also introduced into the re-circulating circuit at a rate sufficient to offset the amount of liquid evaporated in the flow corridor.

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20-02-2014 дата публикации

Seawater desalination apparatus

Номер: US20140048467A1
Автор: Kazuo Matsuura
Принадлежит: NANOMIST TECHNOLOGIES Co Ltd

A seawater desalination apparatus includes a spray ( 1 ), a gas supplier ( 9 ), an atomizing electrode ( 2 ), a high voltage power supply ( 3 ), a mist classifier ( 4 ), and a mist collector ( 5 ). The spray includes apertures for producing a seawater mist. The supplier supplies gas for carrying the mist from the spray. The electrode electrostatically produces fine droplets from the mist from the spray. The power supply is connected to the electrode and the spray, and applies high voltage between the electrode and the spray for the production of fine droplets from the mist from the atomizer. The classifier separates the fine droplets in the mist from the electrode. The collector collects the mist discharged from the classifier thereby producing fresh water.

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27-03-2014 дата публикации

SPRAY DRYING APPARATUS OF DEHYDRATION FILTRATE FROM DESULFURIZATION WASTE WATER, AND AIR POLLUTION CONTROL SYSTEM

Номер: US20140083629A1
Принадлежит: MITSUBISHI HEAVY INDUSTRIES, LTD.

A spray drying apparatus includes a gas inlet provided on a side wall in the vicinity of a top portion of the spray drying apparatus, for introducing a flue gas for drying a spray liquid of a dehydration filtrate; a rectifying plate provided in a spray drying apparatus main body, for decelerating the introduced flue gas so as to alter the flue gas flow to a laminar flow; a spray nozzle for spraying the dehydration filtrate emitted from the desulfurization waste water into the flue gas altered to the laminar flow; a gas outlet provided in the vicinity of a bottom portion of the spray drying apparatus main body, for discharging the flue gas contributed to drying of the dehydration filtrate; and a discharge hopper provided on the bottom portion side of the spray drying apparatus main body, for discharging an ash as a spray-dried solid. 1. A spray drying apparatus of dehydration filtrate from desulfurization waste water comprising:a gas inlet provided on a side wall in the vicinity of a top portion of a spray drying apparatus main body, for introducing a flue gas for drying a spray liquid;a rectifying plate provided in the spray drying apparatus main body, for decelerating the introduced flue gas so as to alter the flue gas flow to a laminar flow;a spray nozzle for spraying the dehydration filtrate emitted from the desulfurization waste water into the flue gas altered to the laminar flow;a gas outlet provided on a side wall in the vicinity of a bottom portion of the spray drying apparatus main body, for discharging the flue gas contributed to drying of the dehydration filtrate; anda solid discharging means provided on the bottom portion of the spray drying apparatus main body, for discharging a spray-dried solid.2. The spray drying apparatus of according to claim 1 , further comprising:a protective plate provided in the vicinity of a flue gas introduction region in the spray drying apparatus main body, for preventing wear of an inner wall surface due to a solid content ...

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04-01-2018 дата публикации

SYSTEM AND METHOD FOR SORBTION DISTILLATION

Номер: US20180002193A1
Автор: Yuh Howard Y.
Принадлежит:

A system and method for distilling water is disclosed. The system comprises a heat source, and a plurality of open-cycle adsorption stages, each stage comprising a plurality of beds and an evaporator and a condenser between a first bed and a second bed, wherein each bed comprises at least two vapor valves, a plurality of hollow tubes, a plurality of channels adapted for transferring water vapor to and from at least one of the condenser or the evaporator, a porous media, a hygroscopic material, and a plurality of graphite flakes, and wherein each vapor valve connects a bed to either the condenser or the evaporator. The method utilizes a number of open-cycle adsorption stages operate in an alternating cycle of forcing and relaxing, whereby both the latent heat of vaporization and the latent heat of adsorption are multiply reused to distill water. 1. A distillation system , comprising:a heat source; a plurality of beds; and', 'an evaporator and a condenser are operatively connected to a first bed of the plurality of beds and a second bed of the plurality of beds;, 'a plurality of open-cycle adsorption stages, each stage comprisingwherein each bed comprises at least a first and a second vapor valve, at least one hollow tube, at least one channel adapted for transferring water vapor to and from at least one of the condenser or the evaporator, a porous media, a hygroscopic material, and a plurality of graphite flakes, andwherein the first vapor valve connects the bed the condenser and the second vapor valve connects the bed to the evaporator.2. The distillation system of claim 1 , wherein each evaporator and condenser is located between the first bed and second bed of each of the respective stage.3. The distillation system of claim 1 , wherein the hollow tubes are comprised of at least one material selected from the group of copper claim 1 , aluminum claim 1 , or steel claim 1 , the porous media is comprised of silica gel claim 1 , and the hygroscopic material is ...

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03-02-2022 дата публикации

EVAPORATION PANEL ASSEMBLIES, SYSTEMS, AND METHODS

Номер: US20220033281A1
Автор: Patey Michael J.
Принадлежит: ECOVAP, INC.

The present disclosure is drawn to evaporation panel assemblies, systems, and methods. For example, a modular evaporation panel system can include a plurality of evaporation panels with individual evaporation panels including evaporation shelves that are laterally elongated, vertically stacked, and spaced apart; vertical support columns positioned along the evaporation shelves to vertically support and separate the evaporation shelves; female-receiving openings defined by multiple evaporation shelves and multiple support columns; and male connectors positioned at lateral ends of the evaporation panels. The male connectors can be releasably receivable by the female-receiving openings of an adjacent evaporation panel, thereby providing modular assembly and disassembly of multiple evaporation panels relative to one another. 1. A modular evaporation panel system , comprising a plurality of evaporation panels , wherein individual evaporation panels of the plurality include:evaporation shelves that are laterally elongated, vertically stacked, and spaced apart;vertical support columns positioned along the evaporation shelves to vertically support and separate the evaporation shelves;female-receiving openings defined by multiple evaporation shelves and multiple support columns; andmale connectors positioned at lateral ends of the evaporation panels, wherein the male connectors are releasably receivable by the female-receiving openings of an adjacent evaporation panel, thereby providing modular assembly and disassembly of multiple evaporation panels relative to one another.2. The modular evaporation panel system of claim 1 , wherein the male connectors of a first evaporation panel are releasably receivable by the female-receiving openings of a second evaporation panel when the first and second evaporation panels are orthogonally oriented with respect to one another.3. The modular evaporation panel system of claim 1 , wherein all of the individual evaporation panels include ...

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25-01-2018 дата публикации

WASTE SYSTEM UTILIZING WASTE HEAT TO REDUCE WATER CONTENT IN WASTE

Номер: US20180021690A1
Автор: Stultz David
Принадлежит: Stultman, LLC

According to an embodiment of the disclosure, a system reduces or eliminates the volume of waste or sewage by taking thermal energy from a waste heat source and applying it to waste or sewage. In particular configurations, the waste or sewage is homogenized and condensed prior to being sprayed across the waste heat. In particular configurations, the waste heat may be sprayed once a threshold amount of energy is contained in the waste heat. 1. A system comprising:a pre-processing unit configured to make the waste more uniform;a source of thermal energy; andan evaporative processing unit, the evaporative processing unit configured to receive an output of the pre-processing unit and the source of thermal energy to yield dehydrated waste and evaporated water.2. The system of claim 1 , wherein at least a portion of the source of thermal energy is waste heat.3. The system of claim 1 , wherein the evaporative processing unit is reduced to a subambient pressure.4. The system of claim 1 , wherein at least a portion of the dehydrated waste provides an energy source to at least partially power a unit to reduce the evaporative processing unit to a subambient pressure.5. The system of claim 1 , wherein the waste is sprayed into the evaporative processing unit.6. The system of claim 1 , wherein at least a portion of the dehydrated waste provides an energy source to at least partially power a unit to spray the waste into the evaporative processing unit.7. The system of claim 1 , further comprising:a condensing unit that condenses evaporated water.8. The system of claim 6 , wherein the condensed evaporative water is potable.9. The system of claim 1 , wherein at least a portion of the dehydrated waste is returned to supply at least a portion of the source of thermal energy. This application is related to U.S. Provisional Application Nos. 62/365,343 (filed on Jul. 21, 2016) and 62/444,299 (filed on Jan. 9, 2017) both of which are incorporated by reference herein for all purposes. The ...

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26-01-2017 дата публикации

Aerobic Treatment System

Номер: US20170022080A1
Принадлежит:

An aerobic treatment system is disclosed herein in which an aerobic holding treatment tank, having an inlet adapted to receive wastewater and an outlet adapted to discharge treated wastewater therefrom, is in communication with an aeration pump having an inlet nozzle in communication with the aerobic holding treatment tank for providing a source of air to the contents of the aerobic holding treatment tank. The aerobic treatment system may further include a generation pump disposed below ground level and in fluid communication with the aerobic holding treatment tank. The generation pump is provided in fluid communication with a high pressure pump in fluid access with an evaporator fan and misting nozzle. The system may further include electronics to connect to grid power, backup electronics for connection to auxiliary power sources, and at least one solar collector for providing a source of electricity. 1. A wastewater treatment system , comprising:a waste holding tank, having an inlet for receiving a waste stream, and an outlet for directing a fraction of the waste stream from the waste holding tank;a waste stream purification device having an inlet for receiving the fraction of the waste stream from the waste holding tank; anda pressure pump having an inlet provided in fluid communication with an outlet of the waste stream purification device for directing a purified water stream to an elevated evaporation module,wherein the elevated evaporation module comprises at least one fan and at least one fluid directing nozzle adjacent the at least one fan, the at least one fluid directing nozzle configured for directing the purified water stream from the waste stream purification device and pumped by the pressure pump to the at least one fan, andwherein the at least one fan and the at least one nozzle are configured to form a mist from the purified water stream.2. The wastewater treatment system of claim 1 , wherein the waste holding tank comprises a primary settling tank ...

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30-01-2020 дата публикации

SEAWATER DESALINATION DEVICE OF INDUSTRIAL EXHAUST HEAT-DRIVEN EJECTOR REFRIGERATION AND APPLICATION METHOD THEREOF

Номер: US20200031688A1
Принадлежит: Dongguan University of Technology

The present invention relates to the fields of energy technology and seawater desalination, and more specifically, relates to a seawater desalination device of industrial exhaust heat-driven ejector refrigeration and an application method thereof The seawater desalination device comprises a seawater collecting pool, a low-pressure seawater storage tank, an ejector refrigeration system and a fresh water storage tank which are successively connected; the ejector refrigeration system comprising a nozzle for spraying low-pressure vapor, a mixing chamber, a diffuser, a first heat-exchanger, a condenser, a condensate pump and a generator; bottom of the low-pressure seawater storage tank being connected with a second heat-exchanger; the mixing chamber being connected with the nozzle, the diffuser and the low-pressure seawater storage tank, respectively; and the diffuser, the first heat-exchanger, the condenser and the fresh water storage tank being successively connected. The present invention provides a seawater desalination device of industrial exhaust heat-driven ejector refrigeration, which achieves efficient recovery and utilization of industrial exhaust heat, and the fresh water and cooling load can be provided for users, thus effectively utilizing the industrial exhaust heat, reducing the environmental pollution and cost, and enhancing the energy efficiency. 1135755253545556573652515335354557. A seawater desalination device of industrial exhaust heat-driven ejector refrigeration , characterized in that , the seawater desalination device comprises a seawater collecting pool () , a low-pressure seawater storage tank () , an ejector refrigeration system () and a fresh water storage tank () which are successively connected; the ejector refrigeration system () comprising a nozzle for spraying low-pressure vapor , a mixing chamber () , a diffuser () , a first heat-exchanger () , a condenser () , a condensate pump () and a generator (); bottom of the low-pressure seawater ...

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09-02-2017 дата публикации

Assembly and Method for Treating Raw Water

Номер: US20170036140A1
Принадлежит:

An assembly and a method for treating raw water wherein the raw water is heated on the heating side of a heat pump and at least partially evaporated into an air stream. At least part of the raw water evaporated into the air stream is separated in a suitable device. In addition, the heat pump is provided with heat on the cooling side by means of heated raw water that has not been evaporated into the air stream, and the heat pump has a thermal coupling in a coldest section of its cooling side, in order to provide cooling for external applications. 1. An assembly for treating a raw water havinga heat pump having a heating side and a cooling side and designed to heat the raw water on the heating side;a vaporizer which is designed to vaporize the heated raw water partly into an air stream; anda device which is connected downstream of the vaporizer and is suitable for separating out at least in part the raw water present in the air stream,wherein the heat pump is designed to be supplied with heat on the cooling side via heated raw water that has not been vaporized into the air stream; andwherein the heat pump, in a coldest subregion of the cooling side, has a thermal coupling which is suitable for providing cooling for external applications.2. The assembly as claimed in claim 1 , wherein a compressing means is connected upstream of the device that is suitable for separating out the raw water present in the air stream claim 1 , which compressing means is suitable for compressing the air stream.3. The assembly as claimed in claim 1 , wherein the device that is suitable for separating out the raw water present in the air stream comprises a carrier assembly having a number of carriers.4. The assembly as claimed in claim 3 , wherein the carriers are porously knitted flexible plastic tubings that have been subjected to a heat treatment for mechanical stabilization.5. The assembly as claimed in claim 3 , wherein the carriers are porous flexible tubings having an interior and a ...

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06-02-2020 дата публикации

System and method for sorbtion distillation

Номер: US20200039842A1
Автор: Howard Y. Yuh
Принадлежит: Howard Y. Yuh

A system for distilling water is disclosed. The system comprises a heat source, and a plurality of open-cycle adsorption stages, each stage comprising a plurality of beds and an evaporator and a condenser between a first bed and a second bed, wherein each bed comprises at least two vapor valves, a plurality of hollow tubes, a plurality of channels adapted for transferring water vapor to and from at least one of the condenser or the evaporator, a thermally conductive water vapor adsorbent, and wherein each vapor valve connects a bed to either the condenser or the evaporator.

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18-02-2021 дата публикации

EVAPORATOR FOR AMBIENT WATER BODIES, AND RELATED SYSTEM AND METHOD

Номер: US20210046397A1
Принадлежит:

An evaporator is provided for evaporating water from an ambient water body. The evaporator includes a housing that in turn includes an air flow channel and an air flow exit. The evaporator also includes an air flow induction device, such as a fan or impeller, that facilitates the directing of an air flow stream through the air flow channel and out the air flow exit. A water injection device is in fluid communication with the air flow channel and is disposed to inject the water from the water body into the air flow stream at a water injection location within the air flow stream and proximate to the air flow exit. A water injection system for injecting water from an ambient water body into an air flow stream directed by an air flow channel of an evaporator also is disclosed, wherein the air flow channel is disposed about a longitudinal axis. The water injection system includes an elongated tubular member disposed parallel with respect to the longitudinal axis, a plurality of water injection nodes disposed at the tubular member and spaced from one another longitudinally, and a support for positioning the elongated tubular member within or proximate to the air flow channel so that the plurality of water injection nodes are positioned within the air flow stream. 1. An evaporator for evaporating water from an ambient water body , the evaporator comprising:a housing comprising an air flow channel and an air flow exit;an air flow induction device that facilitates the directing of an air flow stream through the air flow channel and out the air flow exit; anda water injection device in fluid communication with the air flow channel and disposed to inject the water from the water body into the air flow stream at a water injection location within the air flow stream and proximate to the air flow exit.2. An evaporator as recited in claim 1 , wherein:the air flow channel is disposed longitudinally about a longitudinal axis; andthe water injection location comprises a location at ...

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25-02-2021 дата публикации

Water management system

Номер: US20210053844A1
Принадлежит: Dmac Ip Pty Ltd

An outdoor water management system including at least one reservoir configured to receive highly concentrated contaminated water, a weather proof cover, covering the reservoir to define at least one chamber and water vapour removal means, configured to remove evaporated water from the at least one chamber wherein the at least one chamber is configured to further concentrate the contaminated water while providing long-term weatherproof storage thereof.

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22-02-2018 дата публикации

CEMENT SOLIDIFICATION DEVICE FOR WASTE AND METHOD THEREFOR, AND ZERO-LIQUID DISCHARGE AIR POLLUTION CONTROL SYSTEM AND METHOD THEREFOR

Номер: US20180050302A1
Принадлежит: Mitsubishi Hitachi Power Systems, Ltd.

A cement solidification device for waste includes a slurrying vessel that dissolves and slurries waste containing harmful substances and deliquescent compounds in solvent water to obtain slurried material ; an iron-based additive supply unit that adds an iron-based additive to the slurrying vessel ; a cement kneading vessel that adds a cement solidifying agent from a cement-solidifying agent supply unit to the slurried material in which the iron-based additive is mixed to obtain a cement kneaded product ; and a cement solidification unit that cures the cement kneaded product to form a cement solidified product 1. A cement solidification device for waste , the cement solidification device comprising:a slurrying vessel that dissolves and slurries waste containing harmful substances and deliquescent compounds in solvent water to obtain slurried material;a cement kneading vessel that adds a cement solidifying agent to slurried material in which an iron-based additive is mixed to obtain a cement kneaded product;an iron-based additive supply unit that adds the iron-based additive to either one or both of the slurrying vessel and the cement kneading vessel; anda cement solidification unit that cures the cement kneaded product to form a cement solidified product.2. The cement solidification device for waste according to claim 1 , wherein the iron-based additive is an inorganic ferrous salt.3. A cement solidification method for waste containing heavy metals and deliquescent compounds claim 1 , the cement solidification method comprising:dissolving and slurrying waste that contains heavy metals and deliquescent compounds in solvent water to obtain slurried material;adding a cement solidifying agent to slurried material in which an iron-based additive is mixed and that contains heavy metals, followed by kneading;adding the iron-based additive to the slurried material or a cement kneaded product that contains harmful substances and the deliquescent compounds; andcuring the ...

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21-02-2019 дата публикации

LOW-TEMPERATURE DISTILLATION PLANT

Номер: US20190054392A1
Автор: LEHMANN MARKUS
Принадлежит:

A low-temperature distillation facility for distilling a mixed fluid into a pure fluid. An aggregation device has an inlet connected to the vapour space of a supercooling chamber, wherein captured mixed fluid from an evaporator enters the supercooling chamber. The aggregation device's outlet is connected to the vapour space of a superheating chamber, wherein captured pure fluid from a condenser can be sprayed into the superheating chamber. An energy source cools the temperature in the supercooling chamber and heats the temperature in the superheating chamber. A heat exchanger is arranged between the exits of the supercooling chamber and of the superheating chamber. During the process, vapour flows from the supercooling chamber via the aggregation device to the superheating chamber. 1. A low-temperature distillation facility (LTD) with one or more stages having different mean temperatures T , for distilling a mixed fluid into a pure fluid , wherein each stage comprises:an evaporator with a vapour space and with a warmer Ti+ΔT mixed fluid which can be introduced,{'sub': 'i', 'a condenser with a vapour space and with a cooler T−ΔT pure fluid which can be sprayed in, and'}wherein the vapour spaces of the evaporator and of the condenser are connected to one another into a common vapour space by way of vapour connections, in a manner such that the pressure and the temperature therein can equalise at all times in an unhindered manner,at least one aggregation device which at the entry side is connected to the vapour space of a supercooling chamber, wherein captured mixed fluid from an evaporator, with several evaporators from that of the coolest stage, can be brought into the supercooling chamber, and said aggregation device at the exit side is connected to the vapour space of a superheating chamber,wherein captured pure fluid from a condenser, with several condensers from that of the warmest stage can be sprayed into the superheating chamber,wherein the aggregation device ...

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04-03-2021 дата публикации

AN APPARATUS FOR MAXIMIZING EFFLUENT LIQUID EVAPORATION

Номер: US20210060452A1
Принадлежит:

The present invention generally relates to a system for treating effluent water. More particularly, it provides a robust apparatus for treating waste liquid by optimizing solar and wind energy to maximize the evaporation rate as compare to natural evaporation rate. The main object of the present invention is to provide a system for evaporating RO reject and other effluent liquid and other liquids, by optimizing system to solar and wind energy to maximize vaporization rate and recovery rate at marginal operational cost. 1200100201202208205100. A high efficiency system () for evaporation of an effluent liquid , said system having a flush ratio of 1 at an effluent temperature of 70 deg Celsius and a steam ratio of up to 14 at consumption of 10 KWHr/KL of effluent when measured at 25 deg Celsius temperature and a relative humidity of 60; said system comprising an apparatus () , an effluent holding tank () with or without a heat exchanger () , a control panel () and an effluent management system () , wherein said apparatus () comprising:{'b': '110', 'a) a housing with a rear end and at least one fan duct () at an end opposite to the rear duct,'}{'b': '101', 'b) a plurality of pans () positioned between the rear duct and the at least one fan duct; and'}{'b': '201', 'c) an injection system for supplying with controlled amount of effluent liquid to said plurality of pans from the effluent holding tank (),'}wherein,{'b': '104', 'the at least one fan duct comprises at least one fan ();'}{'b': '101', 'the plurality of pans () having a top surface and a bottom surface, said top surface having guides and/or curvature to maintain uniform layer of effluent liquid on it;'}{'b': 105', '101', '106', '107', '111, 'the injection system comprises an injection line () to guide the effluent liquid to pan (), an overflow line () to prevent effluent from spilling over from pan, and a flush line () to drain unevaporated effluent from the pan, said injection line comprising a plurality of ...

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19-03-2015 дата публикации

Water Treatment Device

Номер: US20150075963A1
Автор: Takashi Yabe
Принадлежит: Yts Science Properties Pte. Ltd.

A water treatment system ( 220 ) heats raw water, gasifies a portion thereof by an evaporator ( 34 ), and condenses the gasified steam at a condensation area ( 240 ) to obtain condensed water. The water treatment system ( 220 ) includes a heater ( 32 ) for heating raw water, a steam conducting part ( 35, 36 ) for conducting, to the condensation area ( 240 ), steam gasified from the raw water heated by the heater ( 32 ), and a pipe ( 221 ) for conducting circulating water from the condensation area ( 240 ) to the evaporator ( 34 ), causing heat exchange between the steam conducted to the condensation area ( 240 ) by the steam conducting part ( 35, 36 ) and the circulating water, as well as causing heat exchange between the raw water and the circulating water at the evaporator ( 34 ).

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07-03-2019 дата публикации

PROCESS TO OBTAIN THIN LAYERS OF DRIED AND CONSOLIDATED MATURE FINES TAILINGS

Номер: US20190071323A1
Принадлежит:

A process to treat fines tailings generated from mining operations, wherein tailings material is sprayed onto a solid substrate as a thin layer and allowed to dry. The spray may be re-applied on top of the dried tailings film leading to multiple layers of dried tailings solids. The method may yield a solid, dry, and consolidated tailings material. 1. A method for partially dewatering fluid fines tailings , the method comprising the steps of:transporting the fluid fines tailings to a point vertically spaced above a substrate;ejecting the fluid fines tailings at the point into the air above the substrate to form dispersed fines tailings droplets comprising water; andallowing the dispersed fines tailings droplets to contact the substrate with inertial force at a contact velocity, the contact velocity sufficient to cause the dispersed fines tailings droplets to flatten on the substrate and release some of the water, forming partially dewatered fluid fines tailings.2. The method of further comprising a step after step c. of allowing the partially dewatered fluid fines tailings to further dry.3. The method of wherein the further drying is achieved by ambient atmospheric conditions or application of heat to the partially dewatered fluid fines tailings.4. The method of wherein the fluid fines tailings are ejected through a nozzle to atomize the fluid fines tailings and thus form the dispersed fines tailings droplets.5. The method of wherein the point is rotated around a central axis during ejection of the fluid fines tailings to form the dispersed fines tailings droplets claim 1 ,6. The method of wherein the step of ejecting comprises directing the fluid fines tailings generally upwardly.7. The method of wherein the step of ejecting comprises directing the fluid fines tailings generally downwardly.8. The method of wherein the fluid fines tailings are held within a tank and subsequently pumped to the point for ejecting.9. The method of further comprising the steps of: ...

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16-03-2017 дата публикации

WASTE WATER EVAPORATOR

Номер: US20170073247A1
Принадлежит:

An atomizer for use in waste water evaporation includes a motor having a rotor shaft, at least one conduit for receiving the waste water, a housing supporting the motor and the at least one conduit, and a hub having a plurality of holes for distributing waste water in the form of water droplets. The motor is a variable speed motor and is cooled by waste water flowing through the at least one conduit. The hub is connected to the rotor shaft and spins at a variable speed with the rotor shaft. The atomizer may be used in a waste water evaporation system that further includes an anemometer and a control system. The control system receives a wind speed input from the anemometer and provides a signal to the variable speed motor to adjust the speed of the variable speed motor and hub, thereby adjusting the water droplet size in response to varying wind conditions. 1. A method for evaporating waste water , comprising: a variable speed motor comprising a rotor shaft, the rotor shaft comprising a longitudinal axis;', 'at least one conduit for receiving waste water;', 'a housing supporting the motor and at the at least one conduit within the housing such that the at least one conduit is positioned in proximity to the motor to absorb heat produced by the motor; and', 'a cylindrical hub comprising a central axis and an outer surface disposed around and spaced apart from the central axis, and a plurality of holes in the outer surface for distributing the waste water as water droplets, the water droplets comprising a droplet size;', 'wherein the motor is cooled by the waste water flowing through the at least one conduit and the hub is connected to the rotor shaft such that the central axis of the cylindrical hub is aligned with the longitudinal axis of the rotor shaft, and the hub is configured to spin about the central axis at a variable speed with the rotor shaft;, 'providing an atomizer assembly for placement on a surface of a waste water pond, the atomizer assembly comprising ...

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05-03-2020 дата публикации

NON-WASTE WATER FLUE GAS TREATMENT SYSTEM AND NON-WASTE WATER FLUE GAS TREATMENT METHOD

Номер: US20200071207A1
Принадлежит: Mitsubishi Hitachi Power Systems, Ltd.

An apparatus is disclosed including a desulfurization device which removes sulfur oxides contained in boiler flue gas, a spray drying device which sprays desulfurization waste water discharged from the desulfurization device and which dries the waste water by introducing a drying gas, a flue gas supplying line Lwhich returns, to a main flue L, flue gas obtained after the desulfurization waste water is evaporated and dried, an alkaline agent supplying unit which adds an alkaline agent to a desulfurization waste water line L, and a pH meter which measures the pH in the desulfurization waste water at locations before and after the alkaline agent supplying unit in the desulfurization waste water line L, wherein the alkaline agent is added in accordance with a measurement result of a measured pH to cause the desulfurization waste water added with the alkaline agent to have a pH fall within a predetermined pH. 111-. (canceled)12. A non-waste water flue gas treatment system , comprising:a boiler configured to combust fuel;a heat recovering device provided in a main flue that discharges a boiler flue gas from the boiler and configured to recover heat of the boiler flue gas;a desulfurization device configured to remove a sulfur oxide contained in the boiler flue gas with a desulfurization absorbing liquid;a spray drying device configured to spray waste water including desulfurization waste water discharged from the desulfurization device;a flue gas introduction line configured to introduce a drying gas for evaporating and drying the desulfurization waste water into the spray drying device;a flue gas supplying line configured to return a flue gas obtained after the desulfurization waste water being evaporated and dried in the spray drying device back to the main flue;an alkali supplying unit configured to add an alkaline agent to a desulfurization waste water line that connects the desulfurization device and the spray drying device; anda pH meter configured to measure a pH in ...

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18-03-2021 дата публикации

Method and apparatus with outlet for extracting molten salt

Номер: US20210077917A1
Автор: Herbert Huening
Принадлежит: Christof Clean City Holding Ltd

The invention relates to a device for drawing off liquid salt, particularly for facilities for purifying wastewater, said device comprising a heating chamber. The heating chamber comprises an inlet for introducing a salt-containing substance and is connected to an outlet for a salt melt. The outlet comprises an outlet channel and an outlet channel end, a cooling region for cooling the salt melt being provided down-stream of the outlet channel end. The outlet channel is peripherally surrounded by an outlet wall at least along a section, the outlet comprising heating element.

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12-06-2014 дата публикации

Water Supply Systems

Номер: US20140158516A1
Автор: Landrok Mads
Принадлежит:

Water supply systems use readily available heat sources like the sun and waste heat from industrial plants to heat intake air and water so more water can be used to saturate the intake air. That extra water is condensed out at another place even miles away where the now distilled water would be more useful. 1. An improved water supply system that includes an evaporation station , a connecting air transport pipe for humidified air , and a condensation station , the improvement comprising:a number of spray nozzles for evaporating an intake of salty water into a humidified airflow; andan intake air duct configured to increase the air pressure before and proximate to the spray nozzles, and to thereafter drop the air pressure of the humidified airflow;wherein, the combination is configured to produce fresh water from a continuous raw water input supply.2. The improved water supply system of claim 1 , further comprising:at least one airflow balancing mechanism inserted between the evaporation station and condensation station to maintain a quasi constant airflow through the connecting air transport pipe, wherein the cross-sectional areas are configured to balance out pressure excursions.3. The improved water supply system of claim 1 , further comprising:a spiral conduit configured to replace the connecting air transport pipe for humidified air;wherein, a more compact water desalination system is made possible.4. The improved water supply system of claim 1 , further comprising:an evaporation spiral conduit configured to replace the connecting air transport pipe for humidified air;a heating device arranged to input heat into the evaporation spiral conduit and thereby instigate evaporation within the evaporation spiral conduit;a condensation spiral conduit connected to receive the humidified air from the evaporation spiral conduit;a cooling device arranged to take away heat from the condensation spiral conduit and thereby initiate condensation;wherein, a more compact water ...

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22-03-2018 дата публикации

METHOD FOR PROCESSING A LIQUID MEDIUM AND PROCESSING PLANT

Номер: US20180080646A1
Принадлежит: SIEMENS AKTIENGESELLSCHAFT

A method for processing a liquid medium, wherein the medium to be processed is conducted through a liquid circuit and the medium to be processed is heated up in the liquid circuit with the aid of a heat exchanger. A liquid-vapor separation process is carried out in a separating device, and a liquid obtained in the liquid-vapor separation process is conducted into the heat exchanger as a heating medium. 115.-. (canceled)16. A method for processing a liquid medium , the method comprising: 'heating the medium to be processed in the liquid circuit with the aid of a heat exchanger, carrying out a liquid-steam separation in a separation device,', 'conducting the medium to be processed through a liquid circuit,'}introducing a liquid which is produced during the liquid-steam separation into the heat exchanger as heating medium,conducting a gaseous carrier medium through an evaporator and a condenser in a cooling circuit,dispersing the medium to be processed in the evaporator by an atomizing device, wherein at least some of the dispersed medium to be processed is evaporated and picked up by the gaseous carrier medium, andcondensing at least some of the evaporated medium to be processed, which is picked up by the carrier medium, in the condenser.17. The method as claimed in claim 16 , further comprising:introducing a contaminated liquid from a steam drum in which a first pressure prevails into the separation device, wherein steam is separated from the contaminated liquid during the liquid-steam separation, andintroducing the separated steam from the separation device into an element of a steam generator, wherein a second pressure, which is lower than the first pressure, prevails in the element, and the liquid which is produced during the liquid-steam separation is produced from the contaminated liquid.18. The method as claimed in claim 17 ,wherein the element of the steam generator, into which the separated steam from the separation device is introduced, is an additional ...

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19-06-2014 дата публикации

Subterranean Well Production Saltwater Evaporation Station

Номер: US20140166210A1
Автор: Hudgens Dennis
Принадлежит: HUDGENS HOLDINGS, LLC

A production saltwater disposal facility comprising a separator configured to receive production saltwater from a pipeline or a vehicle and separate hydrocarbons from the production saltwater, wherein the production saltwater received from the pipeline or vehicle is substantially the same composition as when the production saltwater was located in a subterranean formation, a hydrocarbon storage tank configured to receive hydrocarbons from the separator, a settling pit configured to receive the production saltwater from the separator and separate metals and/or other solids from the saltwater, an evaporator in fluid communication with the settling pit and comprising a nozzle configured to emit a stream of the saltwater along a path in air such that water in the saltwater evaporates, and a collection pit positioned under the path and configured to collect the salt from the saltwater after the water has evaporated. 1. A production saltwater evaporation apparatus , comprising:an evaporator configured to emit a stream of saltwater along a path in air such that at least some of the water in the saltwater evaporates; anda collection area positioned under the path and configured to collect the salt and any remaining water from the saltwater after the at least some water has evaporated.2. The production saltwater evaporation apparatus of claim 1 , further comprising a solids separator positioned upstream of the evaporator claim 1 , wherein the solids separator is configured to separate metals and/or other solids from production saltwater to produce the saltwater.3. The production saltwater evaporation apparatus of claim 2 , wherein the solids separator comprises a settling pit claim 2 , and wherein the saltwater emitted by the evaporator consists essentially of salt and water.4. The production saltwater evaporation apparatus of claim 2 , wherein the separator comprises a settling tank claim 2 , and wherein the saltwater emitted by the evaporator consists essentially of salt ...

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19-03-2020 дата публикации

Desalinization Device and Method of Using the Same

Номер: US20200087167A1
Автор: Liu Depei
Принадлежит:

The invention is a high-salt waste water air powered low temperature evaporating device and method of use. A tray is mounted on a lifting platform; an air inlet and a water inlet are on the tray. Air distributing pipes are arranged at the center of the nested column tubes (). A groove () is installed at the top of the tray, and mounting points are accompanied by multiple nested column tubes (). The nested column tubes () are connected with the air inlet. An atomizer is arranged inside the air distributing pipes; and the atomizer is connected with the water distributing pipes. Using air power evaporates concentrated waste water multiple times so that the salt in the wastewater reaches saturated concentration, and therefore, the wastewater temperature is reduced, salt is crystallized and separated out, liquid is continuously evaporated, and the wastewater can be completely treated. 120. A high-salt wastewater air powered low-temperature evaporation device () , comprising:{'b': '1', 'a steel structure frame ();'}{'b': '2', 'a lifting platform and a tray ();'}{'b': '3', 'a nested tube column ();'}{'b': '33', 'nested column tubes ()'}{'b': '8', 'a plurality of atomizer(s) ();'}{'b': '6', 'a plurality of air distribution pipe(s) ();'}{'b': '7', 'a plurality of water distribution pipe(s) ();'}{'b': '9', 'a water inlet ();'}{'b': '5', 'an air inlet ();'}{'b': '12', 'a gas collecting cover ();'}{'b': '13', 'an air exhaust outlet ();'}{'b': '4', 'a concentrated liquid waste collecting groove ();'}{'b': '11', 'claim-text': {'b': '12', 'wherein the demister is provided inside the cover ();'}, 'a demister (),'}{'b': '10', 'a concentrated liquid outlet ();'}{'b': '30', 'a crystallization tank ();'}a blower; anda hot air blower;{'b': 3', '5', '6', '7, 'the nested tube column () being installed inside the steel structure frame, the tray is mounted on the lifting platform; and the air inlet () is provided above an air distributing pipe () and a water distributing pipe (),'}{'b': 5', ...

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06-04-2017 дата публикации

Vacuum Filter Press with High Volume Filter Chambers and Liquid Injection System

Номер: US20170095751A1
Автор: Simpson Daniel J.
Принадлежит:

A vacuum filter press system may comprise: a frame; a liquid injection system for controllably injecting liquid directly into each of a multiplicity of chambers; a plurality of filter plates configured to form a stack of parallel plates, each of the filter plates being movably attached to the frame and configured to form the multiplicity of chambers, each of the chambers being formed by adjacent filter plates, each of the chambers being lined by filter cloths, wherein the plurality of filter plates, the multiplicity of chambers and the filter cloths are configured to allow water vapor to escape from the chambers while retaining solids from the liquid to form a filter cake; and a vacuum pump connected to the multiplicity of chambers. Furthermore, wherein each filter plate has spacers attached to both sides, for enlarging the width, and hence capacity of the filter chambers. 1. A vacuum filter press system comprising:a frame;a liquid injection system for controllably injecting liquid directly into each of a multiplicity of chambers;a plurality of filter plates configured to form a stack of parallel plates, each of said plurality of filter plates being movably attached to said frame, said plurality of filter plates further being configured to form said multiplicity of chambers, each of said multiplicity of chambers being formed by adjacent filter plates of said plurality of filter plates, each of said multiplicity of chambers being lined by filter cloths, wherein said plurality of filter plates, said multiplicity of chambers and said filter cloths are configured to allow vapor to escape from said chambers while retaining solids from said liquid to form a filter cake; anda vacuum pump connected to said multiplicity of chambers.2. The vacuum filter press system of claim 1 , wherein each of said plurality of filter plates has spacers attached to both sides claim 1 , for enlarging the capacity of each of said multiplicity of chambers.3. The vacuum filter press system of ...

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26-03-2020 дата публикации

METHODS AND SYSTEMS FOR ENHANCING COOLING POND PERFORMANCE AND SALT PRODUCTION IN A SOLUTION MINING OPERATION

Номер: US20200094158A1
Принадлежит:

A cooling pond system and related methods of improving cooling performance in a cooling pond system using one or more submerged dams to increase cooling performance within the cooling pond system, and increase salt precipitation or recovery. The inclusion of one or more submerged dams within an existing cooling pond system can reduce an outflow temperature by 1-5° F. as compared to the same cooling pond system without any submerged dams. In addition or alternatively, pond depth can be controlled to enhance flow mixing and convection cooling. As the temperature is reduced throughout the cooling pond system, more potassium containing salts are precipitated form the brine solution resulting in increased production or recovery within the same cooling footprint. 1. A cooling pond system , comprising:at least one cooling pond, the cooling pond having a brine inlet stream and an outlet stream, the cooling pond defining a pond length, a pond width and a pond depth; andat least one submerged dam positioned across at least a portion of the pond width, the at least one submerged dam having an upper dam surface located below a pond surface.2. The cooling pond system of claim 1 , wherein the at least one submerged dam extends fully across the pond width.3. The cooling pond system of claim 1 , wherein the at least one submerged dam extends only across a portion of the pond width claim 1 , said at least one submerged dam defining a dam opening.4. The cooling pond system of claim 1 , wherein the upper dam surface is positioned below the pond surface at a depth of about 1 foot to about 5 feet in depth.5. The cooling ponds system of claim 1 , wherein the pond is filled with a brine solution claim 1 , said brine solution wherein a more concentrated brine layer resides proximate a pond floor claim 1 , and wherein the at least one submerged dam causes an increase in the Reynolds number or vertical mixing of the brine solution such that the more concentrated brine layer is forced to the ...

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08-04-2021 дата публикации

High Recovery Desalination and Mineral Production System and Method

Номер: US20210101814A1

A system and method for increasing the water production efficiency of a desalination plant and producing concentrated calcium and magnesium is provided. A saline source water is preferably subjected to a first treatment such a passage through a first desalination unit, followed by dual treatment of the first treatment reject stream using physicochemical adsorption and electrodialysis to remove scale-forming calcium and magnesium. The reject stream from the dual treatment may then be received by a second desalination unit. Due to the removal of the majority of the saline source water's scale-forming minerals, the second desalination unit may be operated at higher operating limits than in conventional desalination units without significant concern for fouling due to scaling. The approach of the present system and method efficiently increases the fresh water production ratio from the source saline water while generating commercially attractive concentrated calcium and magnesium products.

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27-04-2017 дата публикации

Subterranean Well Production Saltwater Evaporation Station with Saltwater Recycle

Номер: US20170114271A1
Автор: Hudgens Dennis
Принадлежит:

A process comprising spraying production saltwater comprising water and dissolved salt through an evaporator to evaporate a portion of the water, collecting unevaporated saltwater which is an unevaporated portion of the saltwater that remains after being sprayed through the evaporator, and adjusting a salinity of at least a portion of the unevaporated saltwater to yield an adjusted brine product. 1. A process comprising:spraying production saltwater comprising water and dissolved salt through an evaporator to evaporate a portion of the water;collecting unevaporated saltwater which is an unevaporated portion of the saltwater that remains after being sprayed through the evaporator; andadjusting a salinity of at least a portion of the unevaporated saltwater to yield an adjusted brine product.2. The process of wherein the adjusting comprises increasing the salinity of the unevaporated saltwater by addition of salt to the unevaporated saltwater.3. The process of wherein the adjusting comprises increasing the salinity of the unevaporated saltwater by addition of a concentrated brine having a salinity that is greater than the salinity of the unevaporated saltwater.4. The process of wherein the adjusting comprising decreasing the salinity of the unevaporated water by addition of fresh water to the unevaporated saltwater.5. The process of wherein the adjusting comprises decreasing the salinity of the unevaporated saltwater by addition of a diluted brine having a salinity that is less than the salinity of the unevaporated saltwater.6. The process of wherein the adjusted brine product has a salinity of from about 1 lb/bbl to about 10 lbs/bbl.7. The process of further comprising mixing a gel system and a proppant material with the adjusted brine product to yield a fracturing fluid.8. The process of wherein the gel system comprises guar gum or their derivatives claim 7 , a cross-linker claim 7 , a breaker claim 7 , a surfactant claim 7 , or combinations thereof.9. The process of ...

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13-05-2021 дата публикации

EVAPORATOR

Номер: US20210139345A1
Автор: VUDRAG Peter Joseph
Принадлежит:

A process for separating distillate and waste from a water stream comprising: spraying the water stream together with compressed steam through one or more dual phase nozzles down into one or more vertical tubes contained in a shell and tube heat exchanger; evaporating water condensing the distillate; and ejecting the waste. 1. A process for separating distillate and waste from a water stream comprising:spraying the water stream together with compressed steam through one or more dual phase nozzles down into one or more vertical tubes contained in a shell and tube heat exchanger;evaporating water condensing the distillate;ejecting the waste; andpassing the steam over spiral fins attached to the outer surface of the vertical tubes.2. The process of claim 1 , wherein the spiral fins include slots.3. The process of claim 1 , wherein the distillate is passed through a plate heat exchanger to pre heat the water stream.4. The process of claim 1 , wherein steam is sucked from the shell heat exchanger tubes into a compressor which recycles the compressed steam to the shell and tube heat exchanger.5. The process as claimed in claim 1 , wherein the waste at least partially comprises solids.6. The process of claim 1 , wherein at least some of the condensed distillate is fed back into the water stream.7. A device for separating distillate and waste from a water stream including:a plate heat exchanger arranged to receive a water stream, heat the water stream and feed the water stream to a first manifold;a shell and tube heat exchanger including one or more vertical tubes, the shell and tube heat exchanger being arranged to receive the water stream from the first manifold and expand the water to release steam and solid waste; anda mist eliminator arranged to filter the steam and feed it through a compressor and into a steam manifold;wherein the steam manifold is arranged to feed the steam into the shell and tube heat exchanger; andwherein at least one fin attached to an outside ...

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25-08-2022 дата публикации

HOT AIR FLOW-CIRCULATION WITHIN A SOLAR DESALINATION SYSTEM

Номер: US20220267170A1
Автор: Samad Nidal, SUBAIEI Faleh
Принадлежит: Saudi Arabian Oil Company

A method for circulating hot air in a solar desalination system includes providing a desalination structure having an air flow path defined between an external surface layer and an internal surface layer. A return flow conduit provides an internal fluid flow path. Saline water is pumped through a center column in a direction from the base towards the peak. The saline water is delivered through a nozzle that extends through a sidewall of the center column to provide a mist within the desalination structure exterior of the center column. An air flow within the air flow path is heated to form a hot air supply. The mist is heated with the hot air supply to form an evaporated fluid. A diverted portion of the hot air supply is delivered into the return flow conduit and mixed with an ambient air to form and heat the air flow. 1. A method for circulating hot air in a solar desalination system , the method including: an inclined outer surface with a base that is larger in diameter than a peak, the inclined outer surface having an external surface layer that is transparent, and an internal surface layer that is dark in color, with an air flow path defined between the external surface layer and the internal surface layer providing an external fluid flow path from the base towards the peak;', 'a return flow conduit, the return flow conduit providing an internal fluid flow path in a direction from the peak towards the base; and', 'a center column having an internal bore and located along an axis of the desalination structure;, 'providing a desalination structure, the desalination structure havingpumping a saline water through the center column in a direction from the base towards the peak;delivering the saline water through a nozzle that extends through a sidewall of the center column to provide a mist within the desalination structure exterior of the center column;heating an air flow from a base within the air flow path to form a hot air supply;heating the mist with the hot air ...

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25-08-2022 дата публикации

Control of hot air flow circulation within a solar desalination system

Номер: US20220267171A1
Автор: Thamer AL-MUTAIRI
Принадлежит: Saudi Arabian Oil Co

Methods and systems for circulating hot air in a solar desalination system include a desalination structure having an air flow path defined between an external surface layer and an internal surface layer. A return flow conduit has a fan, a check valve, and a control valve. Saline water is delivered through a nozzle to provide a mist. An air flow within the air flow path is heated to form a hot air supply. The mist is heated with the hot air supply to form an evaporated fluid. The fan is operated to divert a diverted portion of the hot air supply into the return flow conduit to be mixed with an ambient air to form and heat the air flow. The volume of the diverted portion can be controlled with the control valve. The check valve prevents ambient air from entering the return flow conduit at a base end.

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25-04-2019 дата публикации

SYSTEM AND METHOD FOR SORBTION DISTILLATION

Номер: US20190119126A1
Автор: Yuh Howard Y.
Принадлежит:

A system for distilling water is disclosed. The system comprises a heat source, and a plurality of open-cycle adsorption stages, each stage comprising a plurality of beds and an evaporator and a condenser between a first bed and a second bed, wherein each bed comprises at least two vapor valves, a plurality of hollow tubes, a plurality of channels adapted for transferring water vapor to and from at least one of the condenser or the evaporator, a thermally conductive water vapor adsorbent, and wherein each vapor valve connects a bed to either the condenser or the evaporator. 1. A distillation system , comprising: a plurality of operatively connected beds; and', 'an evaporator and a condenser operatively connected to a first bed of', 'the plurality of beds and a second bed of the plurality of beds;, 'a plurality of operatively connected open-cycle adsorption stages, each stage comprisinga switchable heat source configured to provide heat to one of the plurality of operatively connected beds in one of the plurality of operatively connected open-cycle adsorption stages only during a first operating phase; anda switchable heat exhaust configured to remove heat from another of the plurality of operatively connected beds in one of the plurality of operatively connected open-cycle adsorption stages only during the first operating phase;wherein each bed comprises at least a first, second, and third vapor valve, at least one hollow tube, at least one channel adapted for transferring water vapor to and from at least one of the condenser or the evaporator, a thermally conductive water vapor adsorbent, andwherein the first vapor valve connects the bed to the condenser, the second vapor valve connects the bed to the evaporator, and the third vapor valve connects a volume inside the hollow tubes of the first bed with a volume inside the hollow tubes of the second bed.2. The distillation system of claim 1 , wherein each evaporator and condenser is shared between the first bed and ...

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27-05-2021 дата публикации

METHOD AND SYSTEM FOR DRYING MINE TAILINGS

Номер: US20210154592A1
Принадлежит:

A method and system to treat and dry fines tailings generated from mining operations, comprising spraying the tailings material into a vacuum chamber operated at less than atmospheric pressure to separate evaporated water from the residual solid materials. 1. A method for at least partially drying tailings materials from a mining operation , the tailings materials comprising water and solids , the method comprising the steps of:a. generating droplets of the tailings materials;b. introducing the droplets into a partial vacuum environment; andc. allowing at least some of the water in the droplets to evaporate to produce a water vapour and a solids-dominant residual material.2. The method of wherein the step of generating droplets is achieved by spraying.3. The method of wherein the spraying is atomizing.4. The method of further comprising the step after step c. of extracting the water vapour from the partial vacuum environment and allowing the water vapour to condense into liquid water.5. The method of further comprising the step after step c. of extracting the solids-dominant residual material from the partial vacuum environment.6. The method of further comprising introducing at least one chemical additive to the tailings materials before the step of generating the droplets.7. The method of wherein the at least one chemical additive is selected from the group consisting of gases claim 6 , salt solutions claim 6 , acids claim 6 , bases claim 6 , polymers and flocculants.8. The method of further comprising the step of heating the tailings materials before the step of generating the droplets.9. The method of further comprising the step of heating the partial vacuum environment.10. The method of further comprising transporting the tailings materials from a storage pond prior to generating the droplets.11. The method of further comprising obtaining the tailings materials directly from an extraction process.12. The method of further comprising the step after step c. of ...

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23-04-2020 дата публикации

TREATMENT OF PRODUCED WATER FROM A SUBTERRANEAN FORMATION

Номер: US20200123021A1
Автор: Noles Jerry W.
Принадлежит: Noles Intellectual Properties, LLC

Systems for water treatment may include a drying tunnel, wherein the drying tunnel may comprise: a blower, wherein the blower may be fluidly coupled to an end of the drying tunnel; nozzles disposed between the distal end of the drying tunnel and the blower; and a chamber configured to collect solids; wherein the drying tunnel may be configured to evaporate water. 1. A drying tunnel for evaporating and treating contaminated water comprising:a hollow conduit with a proximal end and a distal end spaced apart from the proximal end;a blower fluidly coupled to the proximal end of the drying tunnel and configured to provide a stream of air into the drying tunnel;at least one nozzle configured to be coupled to a source of contaminated water, the at least one nozzle disposed between the distal end and the blower and configured to provide the contaminated water into the drying tunnel and the stream of air passing therethrough; and, a chamber coupled to and disposed exterior to the drying tunnel, the chamber configured to collect solids falling out of solution from the contaminated water as the contaminated water is evaporated.2. The drying tunnel of claim 1 , wherein the at least one nozzle has an ability to adjust a rate of the contaminated water entering into the drying tunnel to compensate for the stream of air temperature to reach full evaporation.3. The drying tunnel of claim 1 , wherein the at least one nozzle is coupled to a pump via a line.4. The drying tunnel of claim 1 , wherein the number of the at least one nozzle is 32.5. The drying tunnel of claim 1 , wherein the blower is configured to move over 100 claim 1 ,000 cubic feet of air per minute.6. The drying tunnel of claim 1 , wherein at least one of the blower and the drying tunnel has an inner diameter from about 8 feet to about 12 feet.7. The drying tunnel of claim 1 , wherein a length of the drying tunnel is about 50 feet to about 200 feet.8. The drying tunnel of claim 1 , wherein the drying tunnel is disposed ...

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30-04-2020 дата публикации

Treatment of Produced Water From A Subterranean Formation

Номер: US20200131048A1
Автор: Noles Jerry W.
Принадлежит: Noles Intellectual Properties, LLC

Systems for water treatment may include an evaporation unit, wherein the evaporation unit comprises: a first blower; a spacer, wherein the spacer may be fluidly coupled to the first blower; a diffuser fluidly coupled to the spacer, at least one arm fluidly coupled to and disposed radially around the diffuser. The at least one arm is configured to rotate to create a negative pressure as to allow the air mass to be drafted out into the contaminated water. 1. A system for aerating , evaporating , and treating contaminated water comprising: a first blower configured to suction an air mass proximate the contaminated water; and', 'a spacer fluidly coupled to the first blower;', 'a diffuser fluidly coupled to the spacer; and,', 'at least one arm fluidly coupled to and disposed radially around the diffuser, wherein the at least one arm is hollow and is configured to allow the air mass to pass through the at least one arm;, 'at least one evaporation unit, wherein the at least one evaporation unit compriseswherein the at least one arm is configured to rotate to create a negative pressure as to allow the air mass to be drafted out into the contaminated water.2. The system of claim 1 , wherein the at least one arm has a plurality of apertures.3. The system of claim 2 , wherein each of the plurality of apertures has a diameter about 1 inch to about 2 inches.4. The system of claim 2 , wherein each of the plurality of apertures provides an air flow at an angle relative to a central axis of the at least one arm.5. The system of claim 4 , wherein the angle is about 10° to about 90°.6. The system of claim 4 , wherein the angle is about 40° to about 50°.7. The system of claim 4 , wherein the angle is about 45°.8. The system of claim 1 , further comprising a venturi fluidly coupled to a distal end of the at least one arm.9. The system of claim 1 , further comprising a screen fluidly coupled to a distal end of the at least one arm.10. The system of claim 9 , wherein a mesh size of the ...

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16-05-2019 дата публикации

COMPACT WASTEWATER CONCENTRATOR USING WASTE HEAT

Номер: US20190143241A1
Принадлежит:

A compact and portable liquid concentrator includes a gas inlet, a gas exit and a flow corridor connecting the gas inlet and the gas exit, wherein the flow corridor includes a narrowed portion that accelerates the gas through the flow corridor. A liquid inlet injects liquid into the gas stream at a point prior to the narrowed portion so that the gas-liquid mixture is thoroughly mixed within the flow corridor, causing a portion of the liquid to be evaporated. A demister or fluid scrubber downstream of the narrowed portion removes entrained liquid droplets from the gas stream and re-circulates the removed liquid to the liquid inlet through a re-circulating circuit. Fresh liquid to be concentrated is also introduced into the re-circulating circuit at a rate sufficient to offset the amount of liquid evaporated in the flow corridor. 1. A liquid concentrator system , comprising: a gas inlet,', 'a gas outlet,', 'a mixing corridor disposed between the gas inlet and the gas outlet, the mixing corridor having a narrowed portion in which gas flow within the mixing corridor accelerates when traveling from the gas inlet to the gas outlet; and', 'a liquid inlet through which liquid to be concentrated is injected into the mixing corridor, the liquid inlet disposed in the mixing corridor between the gas inlet and the narrowed portion;, 'a concentrator section including;'} a demister gas flow passage coupled to the gas outlet of the concentrator section,', 'a liquid collector disposed in the demister gas flow passage to remove liquid from gas flowing in the demister gas flow passage, and', 'a reservoir that collects the liquid removed from the gas flowing in the demister gas flow passage by the liquid collector; and, 'a demister disposed downstream of the concentrator section, the demister including;'}a fan coupled to the demister to assist gas flow through the mixing corridor and the gas flow passage.2. The liquid concentrator system of claim 1 , further including a re-circulating ...

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24-06-2021 дата публикации

Fluid Treatment Apparatus and Methods

Номер: US20210187410A1
Принадлежит:

A system for concentrating wastewater with a heated gas is disclosed wherein a heated gas directed into a wastewater heating chamber having a cooling assembly for minimizing scale buildup. 1. An apparatus for concentrating wastewater with a heated gas , comprising:a hollow member having a longitudinal axis that is parallel with a direction of gravity, said hollow member comprising a wastewater;a source of heated gas disposed about the cylindrical hollow member and above the waste water inlet, said source of heated gas configured to propagate heated gas into a center of the hollow member;a cooling apron coupled to the hollow member and disposed above the waste water inlet and below the source of heated gas, said cooling apron comprising a top surface, a bottom surface, and a lip, wherein the lip extends downward beyond the bottom surface of the apron.2. The apparatus of claim 1 , wherein a void within the cooling apron is in fluid communication with a heat transfer fluid that is circulated about a portion of the cooling apron.3. The apparatus of claim 1 , wherein the bottom surface of the cooling apron comprises a first section that couples to an internal side surface of the cylindrical hollow member and a second section that couples to an internal side surface of the lip.4. The apparatus of claim 3 , wherein the first section is oriented at an angle ranging from between 15 and 45 degrees from an imaginary plane normal to a direction of gravity passing through the cylindrical hollow member claim 3 , said first section extending upward and away from the cylindrical hollow member.5. The apparatus of claim 3 , wherein the first section comprises a first end coupled to an internal side surface of the cylindrical hollow member and a second end coupled to a first end of the second section claim 3 , the second section comprising a first end coupled to the second end of the first section and a second end coupled to the lip.6. The apparatus of claim 5 , wherein the second ...

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24-06-2021 дата публикации

Fluid Treatment Systems and Methods

Номер: US20210187411A1
Принадлежит:

A system and method for concentrating wastewater with a heated gas is disclosed wherein a heated gas directed into a first wastewater heating chamber at a first velocity and a first wastewater stream is directed into the first wastewater heating chamber. A second wastewater heating chamber coupled to the first wastewater heating chamber and in fluid communication with the first wastewater heating chamber is disclosed. The wastewater streams and heated gas are propagated to optimize the water drop size within the heating chambers. 1. A method for concentrating wastewater with a heated gas , comprising:propagating a wastewater stream at a first velocity downward into a vertical heating chamber through an inlet;propagating a volume of heated gas downward through the wastewater stream at a second velocity, wherein the second velocity is less than the first velocity;creating a flow of wastewater within the vertical heating chamber wherein the water ligaments comprise a sauter mean diameter ranging from 800 to 1000 micrometers.2. The method of claim 1 , wherein the wastewater stream forms a cone.3. The method of claim 2 , further comprising:first and second wastewater streams, wherein the first wastewater stream is propagated downward into the vertical heating chamber, and the second wastewater stream is propagated downward into a vertical evaporation stack, the vertical evaporation stack being in fluid communication with the vertical heating chamber;wherein a volume of the heated gas propagated downward into the vertical heating chamber is propagated upward through the vertical evaporation stack;wherein the water ligaments of the second wastewater stream in the vertical evaporation stack comprise a sauter mean diameter ranging from 800 to 1000 micrometers.4. The method of claim 3 , wherein the velocity of the first wastewater stream propagated downward in the vertical heating chamber is 25 to 80 percent greater than the velocity of the heated gas propagated downward ...

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14-06-2018 дата публикации

System and method for reducing liquid discharge from one or more devices

Номер: US20180161725A1

The present invention relates generally to the field of emission control equipment for boilers, heaters, kilns, or other flue gas-, or combustion gas-, generating devices (e.g., those located at power plants, processing plants, etc.) and, in particular to a new and useful method and apparatus for reducing and/or eliminating various liquid discharges from one or more emission control equipment devices (e.g., one or more wet flue gas desulfurization (WFGD) units). In another embodiment, the method and apparatus of the present invention is designed to reduce and/or eliminate the amount of liquid waste that is discharged from a WFGD unit by subjecting the WFGD liquid waste to one or more drying processes, one or more spray dryer (or spray dry) absorber processes, and/or one or more spray dryer (or spray dry) evaporation processes.

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01-07-2021 дата публикации

Compact Wastewater Concentrator Using Waste Heat

Номер: US20210197097A1
Принадлежит:

A compact and portable liquid concentrator includes a gas inlet, a gas exit and a flow corridor connecting the gas inlet and the gas exit, wherein the flow corridor includes a narrowed portion that accelerates the gas through the flow corridor. A liquid inlet injects liquid into the gas stream at a point prior to the narrowed portion so that the gas-liquid mixture is thoroughly mixed within the flow corridor, causing a portion of the liquid to be evaporated. A demister or fluid scrubber downstream of the narrowed portion removes entrained liquid droplets from the gas stream and re-circulates the removed liquid to the liquid inlet through a re-circulating circuit. Fresh liquid to be concentrated is also introduced into the re-circulating circuit at a rate sufficient to offset the amount of liquid evaporated in the flow corridor. 1. A liquid concentrator system , comprising: a gas inlet,', 'a gas outlet,', 'a mixing corridor disposed between the gas inlet and the gas outlet, the mixing corridor having a narrowed portion in which gas flow within the mixing corridor accelerates when traveling from the gas inlet to the gas outlet; and', 'a liquid inlet through which liquid to be concentrated is injected into the mixing corridor, the liquid inlet disposed in the mixing corridor between the gas inlet and the narrowed portion;, 'a concentrator section including;'} a demister gas flow passage coupled to the gas outlet of the concentrator section,', 'liquid collector disposed in the demister gas flow passage to remove liquid from gas flowing in the demister gas flow passage, and, 'a demister disposed downstream of the concentrator section, the demister including;'}a reservoir that collects the liquid removed from the gas flowing in the demister gas flow passage by the liquid collector; anda fan coupled to the demister to assist gas flow through the mixing corridor and the gas flow passage, the fan being connected to a variable frequency drive motor that operates to vary the ...

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30-06-2016 дата публикации

WATER TREATMENT SYSTEM AND METHOD

Номер: US20160185619A1
Принадлежит: MITSUBISHI HEAVY INDUSTRIES, LTD.

A water treatment system of the present invention for effluent generated in a plant facility includes: a flue gas treatment system that performs treatment of boiler flue gas from a boiler; and a spray drying device that includes a spraying unit, which sprays effluent generated, for example, in a cooler of the plant facility, and that performs spray drying using part of the boiler flue gas. The water treatment system draws the effluent is discharged into the spray drying device so as to dry the sprayed liquid by the part of the flue gas. 1. A water treatment system comprising:a flue gas treatment system that performs treatment of boiler flue gas; anda spray drying device that includes a spraying unit, which sprays effluent generated in a plant facility, and that performs spray drying using some of the boiler flue gas.2. The water treatment system according to claim 1 , further comprising a desalination device that removes salt content present in the effluent claim 1 , whereinthe spray drying device performs spray drying of concentrated water from which salt content has been concentrated by the desalination device.3. The water treatment system according to claim 2 , wherein the desalination device includes a membrane separating unit.4. The water treatment system according to claim 2 , wherein the desalination device removes bivalent salt content present in the effluent.5. The water treatment system according to claim 1 , whereinthe flue gas treatment system includes a wet desulfurization device, andthe spraying unit of the spray drying device has separator liquid, which is obtained by separating gypsum from the wet desulfurization device, introduced thereto and performs spray drying of the separator liquid along with the effluent.6. A water treatment method comprising:flue gas-treating that includes performing treatment of boiler flue gas; andspray-drying that includes spray drying using a spray drying device that has a spraying unit, which sprays effluent generated ...

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09-07-2015 дата публикации

Subterranean Well Production Saltwater Evaporation Station with Iodine Separator

Номер: US20150190728A1
Автор: Hudgens Dennis
Принадлежит:

A production saltwater evaporation apparatus, comprising a separation and storage area comprising an iodine separation unit configured to remove iodine from production saltwater and produce saltwater, and an evaporator configured to emit a stream of the saltwater along a path in air such that at least some of the water in the saltwater evaporates. Included is a production saltwater evaporation apparatus, comprising a saltwater clarifying unit configured to separate metals from production saltwater and produce saltwater, and an evaporator configured to emit a stream of the saltwater along a path in air such that at least some of the water in the saltwater evaporates. 1. A production saltwater evaporation apparatus , comprising:a separation and storage area comprising an iodine separation unit configured to remove iodine from production saltwater and produce saltwater; andan evaporator configured to emit a stream of the saltwater along a path in air such that at least some of the water in the saltwater evaporates.2. The production saltwater evaporation apparatus of claim 1 , wherein the separation and storage area further comprises a hydrocarbon separator configured to separate hydrocarbons from the production saltwater.3. The production saltwater evaporation apparatus of claim 1 , wherein the iodine separation unit is configured to separate the iodine from the production saltwater using an anion exchange resin as an absorption media.4. The production saltwater evaporation apparatus of claim 1 , wherein the iodine separation unit is configured to separate the iodine from the production saltwater using physical filtration.5. The production saltwater evaporation apparatus of claim 1 , wherein the separation and storage area further comprises a saltwater clarifying unit configured to separate metals from production saltwater to produce the saltwater.6. The production saltwater evaporation apparatus of claim 1 , further comprising a collection area positioned under the ...

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07-07-2016 дата публикации

SYSTEM AND METHOD FOR ON SITE AERIAL DISSEMINATION AND ATMOSPHERIC DISPOSAL OF ALL LEACHATES AND WASTEWATERS

Номер: US20160194216A1
Автор: Houston Kelly K.
Принадлежит:

A method and system for on-site aerial dissemination of oxidatively converted particles with substantial atmospheric disposal of the water component of all regulated and defined leachates and regulated and defined wastewaters. These leachates and wastewaters (defined as water containing 2 or more detectable regulated, defined and known contaminants) may include collecting the leachate or wastewater, having multiple contaminating suspended and perhaps precipitated solids therein, and aerially disseminating and disposing of said leachate or wastewater on the site of its generation. The defined leachate or wastewater is directed to an “Integrated Mobile Aerosolization System (IMAS)” having a turbine and being fully integrated and mobile. Thereafter, the mixture is directed from the IMAS and the contaminants aerially disseminated and disposed of over a defined and designated area on the site where the defined leachate or wastewater is created. 1. An aerial method of disseminating and disposing of an unfiltered or unprepared or pre-conditioned regulated and defined wastewater (defined as water containing 2 or more detectable and regulated , defined and known contaminants) having multiple regulated suspended and possibly precipitated solids: directing this wastewater to an independent integrated and mobile aerosolization system (IMAS); driving a turbine associated with the IMAS and generating a system of air that moves through the IMAS; pumping the wastewater under some level of pressure to a series of nozzles associated with the IMAS and creating and atmospheric conversion or high volume or air/liquid flow rate liquid with large clumped particle release or Oxidative Diffusion (OD) or commonly known as aerosolizing the wastewater directed from the nozzles into the system of air passing through the IMAS to form an Atmospheric Conversion (AC) in this air-raw wastewater mixture; and directing the air-raw wastewater mixture from the IMAS and aerially disseminating the air-raw ...

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05-07-2018 дата публикации

Treatment of Produced Water From A Subterranean Formation

Номер: US20180186658A1
Автор: JR. Jerry W., Noles
Принадлежит: Noles Intellectual Properties, LLC

Systems for water treatment may include a drying tunnel, wherein the drying tunnel may comprise: a blower, wherein the blower may be fluidly coupled to an end of the drying tunnel; a heater coupled to an exterior surface of the drying tunnel; nozzles disposed between the heater and the blower; and a chamber configured to collect solids; wherein the drying tunnel may be configured to evaporate water. 1. A drying tunnel comprising:a blower, wherein the blower is fluidly coupled to an end of the drying tunnel;a heater coupled to an exterior surface of the drying tunnel;a nozzle disposed between the heater and the blower;a chamber configured to collect solids; andwherein the drying tunnel is configured to evaporate water.2. The drying tunnel of claim 1 , wherein the blower is configured to move over 100 claim 1 ,000 cubic feet of air per minute.3. The drying tunnel of claim 1 , wherein the blower has an inner diameter from about 8 feet to about 12 feet.4. The drying tunnel of claim 1 , wherein a length of the drying tunnel is about 50 feet to about 200 feet.5. The drying tunnel of claim 1 , wherein the drying tunnel is disposed on a trailer.6. The drying tunnel of claim 1 , wherein the drying tunnel has an inner diameter from about 8 feet to about 12 feet.7. The drying tunnel of claim 1 , wherein the drying tunnel is positioned at angle from about 30° to about 90° relative to horizontal.8. A system comprising: a blower, wherein the blower is fluidly coupled to an end of the drying tunnel;', 'a heater coupled to an exterior surface of the drying tunnel;', 'a nozzle disposed between the heater and the blower;', 'a chamber configured to collect solids; and', 'wherein the drying tunnel is configured to evaporate water., 'a plurality of drying tunnels, wherein each drying tunnel comprises9. The system of claim 8 , wherein the blower is configured to move over 100 claim 8 ,000 cubic feet of air per minute.10. The system of claim 8 , wherein the blower has an inner diameter ...

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05-07-2018 дата публикации

Treatment of Produced Water From A Subterranean Formation

Номер: US20180186659A1
Автор: JR. Jerry W., Noles
Принадлежит: Noles Intellectual Properties, LLC

Systems for water treatment may include an evaporation unit, wherein the evaporation unit may comprise: a first blower; a spacer, wherein the spacer may be fluidly coupled to the first blower; wherein the evaporation unit may be configured to aerate and evaporate water; and a drying tunnel, wherein the drying tunnel may comprise: a second blower, wherein the second blower may be fluidly coupled to an end of the drying tunnel; a heater coupled to an exterior surface of the drying tunnel; nozzles disposed between the heater and the second blower; and a chamber configured to collect solids; wherein the drying tunnel may be configured to evaporate water. 1. A system comprising: a first blower; and', 'a spacer, wherein the spacer is fluidly coupled to the first blower;', 'wherein the evaporation unit is configured to aerate and evaporate water; and, 'an evaporation unit, wherein the evaporation unit comprises a second blower, wherein the second blower is fluidly coupled to an end of the drying tunnel;', 'a heater coupled to an exterior surface of the drying tunnel;', 'a nozzle disposed between the heater and the second blower;', 'a chamber configured to collect solids; and', 'wherein the drying tunnel is configured to evaporate water., 'a drying tunnel, wherein the drying tunnel comprises2. The system of claim 1 , wherein the evaporation unit further comprises a diffuser claim 1 , wherein the diffuser is fluidly coupled to the spacer claim 1 , wherein the diffuser comprises a plurality of arms.3. The system of claim 1 , wherein the evaporation unit is positioned in a storage tank claim 1 , wherein the storage tank comprises a body of water.4. The system of claim 1 , wherein the evaporation unit is positioned in a storage pit claim 1 , wherein the storage pit comprises a body of water.5. The system of claim 1 , wherein the spacer is submerged in a body of water.6. The system of claim 1 , wherein the blower is positioned on top of a storage tank claim 1 , wherein the ...

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20-06-2019 дата публикации

Efficient and energy-saving wastewater evaporation crystallizer

Номер: US20190184307A1

The present disclosure relates to a wastewater flue evaporating device. An wastewater evaporation crystallizer is provided, including an evaporating tube inlet, an inlet flange, an inlet chamber, a pneumatic inlet baffle, an evaporating tube body, a pneumatic outlet baffle, an outlet chamber, an outlet flange, and an evaporating tube outlet which are successively coupled, where the evaporating tube inlet is connected to provide a gas pipeline; the gas pipeline is connected on a flue between an external denitration device and an air preheater; the evaporating tube outlet is communicated with an inlet flue of a dust collector; the evaporating tube body is provided with a wastewater nozzle; and the wastewater nozzle is communicated with a pretreated waste pipe. The present disclosure provides an efficient and energy-saving wastewater evaporation crystallizer which increases evaporation efficiency by bringing in a high-temperature gas at a front end of the air preheater.

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19-07-2018 дата публикации

COMPACT WASTEWATER CONCENTRATOR UTILIZING A LOW TEMPERATURE THERMAL ENERGY SOURCE

Номер: US20180200643A1
Принадлежит:

A compact and portable liquid concentrator includes a gas inlet, a gas exit and a flow corridor connecting the gas inlet and the gas exit, wherein the flow corridor includes a narrowed portion that accelerates the gas through the flow corridor. A liquid inlet injects liquid into the gas stream at a point prior to the narrowed portion so that the gas-liquid mixture is thoroughly mixed within the flow corridor, causing a portion of the liquid to be evaporated. A demister or fluid scrubber downstream of the narrowed portion removes entrained liquid droplets from the gas stream and re-circulates the removed liquid to the liquid inlet through a re-circulating circuit. A source of low energy gas, such as low pressure steam from a power plant, is connected to the liquid to be concentrated to heat the liquid to be concentrated before or during the concentration process. 1. A liquid concentrator , comprising: a gas inlet,', 'a gas outlet,', 'a mixing corridor disposed between the gas inlet and the gas outlet, the mixing corridor having a narrowed portion in which gas flow within the mixing corridor accelerates when traveling from the gas inlet to the gas outlet; and', 'a liquid inlet through which liquid to be concentrated is injected into the mixing corridor, the liquid inlet disposed in the mixing corridor between the gas inlet and the narrowed portion;, 'a concentrator section including;'} a demister gas flow passage coupled to the gas outlet of the concentrator section,', 'a liquid collector disposed in the demister gas flow passage to remove liquid from gas flowing in the demister gas flow passage, and', 'a reservoir that collects the liquid removed from the gas flowing in the demister gas flow passage by the liquid collector; and, 'a demister disposed downstream of the concentrator section, the demister including;'}a heat exchanger fluidly connected to the reservoir, the heat exchanger being fluidly coupled to a source of low temperature gas.2. The liquid concentrator ...

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28-07-2016 дата публикации

SPRAY DRYING APPARATUS FOR DEHYDRATED FILTRATE FROM DESULFURIZATION WASTE WATER, AND AIR POLLUTION CONTROL SYSTEM

Номер: US20160214027A1
Принадлежит: Mitsubishi Hitachi Power Systems, Ltd.

A spray drying apparatus includes: a gas inlet provided in a side wall in the vicinity of a top (lid) portion of the spray drying apparatus, for introducing a flue gas for drying a spray of dehydrated filtrate; flow-adjusting plates provided in a body of the spray drying apparatus, for decelerating the introduced flue gas so as to change the flow of the flue gas to a laminar flow; a spray nozzle for spraying the dehydrated filtrate from the desulfurization waste water into the flue gas having been changed to the laminar flow; and a joining unit for joining a bottom portion of the body of the spray drying apparatus to a gas supply line that is a main flue gas duct for the flue gas so as to discharge spray-dried solids to the main flue gas duct. 1. A spray drying apparatus , comprising:a body portion, a top portion and a bottom portion;a gas inlet, for introducing a flue gas, being provided in the body portion;a spray nozzle for spraying waste water of desulfurization into the flue gas in order to evaporate and dry the waste water of desulfurization; andan outlet duct connected to the bottom portion of the spray drying apparatus.2. The spray drying apparatus as set forth in claim 1 , whereinthe gas inlet being provided in the body portion in the vicinity of the top portion of the spray drying apparatus.3. The spray drying apparatus as set forth in claim 1 , wherein:the flue gas and spray-dried solids are discharged from the body portion to the outlet duct of the spray drying apparatus.4. The spray drying apparatus as set forth in claim 1 , wherein:the outlet duct and the body portion of the spray drying apparatus are configured so that the flow direction of the flue gas and spray-dried solids flow is perpendicular to the extending direction of the outlet duct.5. The spray drying apparatus as set forth in claim 1 , wherein:the outlet duct including a portion extending substantially orthogonal to the body portion.6. The spray drying apparatus as set forth in claim 1 , ...

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04-07-2019 дата публикации

APPARATUS, SYSTEMS AND METHODS FOR MANAGEMENT OF RAW WATER AND EMISSIONS UTILIZING HEAT AND/OR PRESSURE ENERGY WITHIN COMBUSTION GAS SOURCES

Номер: US20190202713A1
Принадлежит:

The invention relates to methods, systems and apparatus for distributed management of raw water and internal combustion engine (ICE) gas emissions generated during industrial operations. One aspect of the invention at least partially utilizes a hot gas air knife to increase or partially increase surface area between a raw water and a hot gas in order to vaporize a proportion of the aqueous phase of the raw water and concentrate contaminants within a residual raw water concentrate. The water vapor generated by the vaporization process may be demisted, discharged directly to the atmosphere or alternatively condensed and captured for use. Another aspect relates to how the liquids and gasses interact to continuously flush the surfaces of the system which may help mitigate scaling issues. The invention may help facilitate rapid transfer of ICE combustion gas particulate and ICE combustion gas chemicals onto and into the raw water as it concentrates. 1121-. (canceled)122. An adaptor for connecting a gas source from an associated gas source to a raw water vaporization system , the adaptor comprising:a gas conduit having a gas connector at an inlet orifice for connecting the conduit to gas source piping;an air knife at an outflow end of the gas conduit, the gas conduit having an outflow orifice for connection to a shearing chamber of a raw water vaporization system and configured to direct at least a section of the gas within the gas conduit to within the shearing chamber to effect raw water shearing.123. The adaptor as in claim 122 , wherein the adaptor is configured to constrict gas flow enabling an increase in gas velocity at the outflow orifice in relation to the velocity of the inlet orifice of the adaptor.124. The adaptor as in claim 122 , wherein the gas source is one or more of: an engine exhaust; an internal combustion engine exhaust; a turbine engine exhaust; and a combustion gas from a flame.125. The adaptor as in claim 122 , wherein the adaptor is configured to ...

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02-08-2018 дата публикации

APPARATUS, SYSTEMS AND METHODS FOR MANAGEMENT OF RAW WATER AND EMISSIONS UTILIZING HEAT AND/OR PRESSURE ENERGY WITHIN COMBUSTION GAS SOURCES

Номер: US20180215632A1
Принадлежит:

The invention relates to methods, systems and apparatus for distributed management of raw water and internal combustion engine (ICE) gas emissions generated during industrial operations. One aspect of the invention at least partially utilizes a hot gas air knife to increase or partially increase surface area between a raw water and a hot gas in order to vaporize a proportion of the aqueous phase of the raw water and concentrate contaminants within a residual raw water concentrate. The water vapor generated by the vaporization process may be demisted, discharged directly to the atmosphere or alternatively condensed and captured for use. Another aspect relates to how the liquids and gasses interact to continuously flush the surfaces of the system which may help mitigate scaling issues. The invention may help facilitate rapid transfer of ICE combustion gas particulate and ICE combustion gas chemicals onto and into the raw water as it concentrates. 1. A raw water vaporization system comprising:a shearing chamber comprising:a gas connector for connecting the shearing chamber to a gas source and for introducing gas into the shearing chamber;the shearing chamber containing a raw water influx system operatively positioned adjacent the gas connector to enable rapid interaction between input raw water and gas for:i) increasing interfacial surface area between the input raw water and the gas andii) enabling rapid heat transfer between the input raw water and the gas to effect vaporization of water from the raw water and the concentration of raw water contaminants.2. The raw water vaporization system as in claim 1 , wherein the gas is introduced into the shearing chamber under positive pressure derived from operation of an associated engine.3. The raw water vaporization system as in claim 1 , wherein the gas connector is an air knife having an inlet orifice connected to a gas conduit and an outflow orifice operatively connected to the shearing chamber.4. The raw water ...

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10-08-2017 дата публикации

SYSTEM AND METHODS FOR LIQUID PURIFICATION

Номер: US20170225096A1
Автор: ROCK Kelly P.
Принадлежит:

An apparatus includes an atomizer with a first flow member defining a first flow path and a second flow member defining a second flow path such that a solution and an inlet gas can flow in the first and second flow path to a mixing volume defined by the first flow member. A vane of the second flow member redirects a portion of at least one of a tangential velocity component or a circumferential velocity component of the flow to produce a rotational velocity component therein. The solution and the inlet gas mix within the mixing volume to produce a mixture. A separator is fluidically coupled to the second flow member to receive the mixture. The separator produces a first flow including a vaporized portion of a solvent from the solution and a second flow including a liquid portion of the solvent and a solute from the solution. 1. An apparatus , comprising:an atomizer configured to mix a solution and a flow of an inlet gas to produce an atomized mixture of the solution and the inlet gas, the atomizer including a first flow member and a second flow member, the first flow member having an outer surface and defining an outlet opening, the outer surface of the first flow member including a vane defining at least a portion of a first flow path, the second flow member having a first surface and a second surface and defining a second flow path therebetween, a portion of the first surface defining a mixing volume,the second flow path configured to convey a flow of the solution and the inlet gas to the mixing volume, at least a portion of the flow being conveyed to the first flow path via the second flow path such that the vane redirects a portion of at least one of a tangential velocity component or a circumferential velocity component of the flow as the solution and the inlet gas flow within the first flow path to produce a rotational velocity component within the flow when the flow is conveyed to the mixing volume, the solution and the inlet gas configured to mix within the ...

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17-08-2017 дата публикации

DESALINATION SYSTEM FOR THE PRODUCTION OF POTABLE WATER

Номер: US20170233264A1
Автор: Boylan David Bradley
Принадлежит:

An evaporation and condensing system having a structure including an evaporator section and a condenser section. A first nozzle system is disposed in the evaporator section. The first nozzle system is in communication with a first feed pipe disposed at least partially in the structure, the first feed pipe is adapted to be in communication with a first substance. A second nozzle system is disposed in the condenser section. The second nozzle system is in communication with a second feed pipe disposed at least partially in the structure. The second feed pipe is adapted to be in communication with a second substance. A first porous knockout panel is disposed proximate the evaporator section. A second porous knockout panel is disposed proximate the condenser section. A first substance drain is disposed in the evaporator section. A second substance drain is disposed in the condenser section. 1. An evaporation and condensing system comprising:a structure having an evaporator section and a condenser section;a first nozzle system is disposed in the evaporator section; the first nozzle system is in communication with a first feed pipe disposed at least partially in the structure, the first feed pipe is adapted to be in communication with a first substance;a second nozzle system is disposed in the condenser section; the second nozzle system is in communication with a second feed pipe disposed at least partially in the structure, the second feed pipe is adapted to be in communication with a second substance;a first porous knockout panel is disposed proximate the evaporator section;a second porous knockout panel is disposed proximate the condenser section;a first substance drain is disposed in the evaporator section; anda second substance drain is disposed in the condenser section.2. The evaporation and condensing system of claim 1 , wherein the first feed pipe is in communication with an evaporator feed tank; the evaporator feed tank includes a first heat exchanger for heating ...

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25-07-2019 дата публикации

SYSTEM AND A METHOD FOR GENERATION AND DELIVERY OF THERMAL ENERGY

Номер: US20190225507A1
Автор: Hiremath Rajeev
Принадлежит:

A system for delivery of thermal energy, comprises piping for carrying a pressurized gas, the piping forming a closed loop and having an inlet for receiving the pressurized gas, one or more velocity and pressure enhancers connected along the piping and a heat exchanger connected along the piping. The piping is configured to receive the pressurized gas via the inlet and recirculate the pressurized gas inside the closed loop. The one or more velocity and pressure enhancers are configured to maintain flow, velocity and thermal energy of the pressurized gas to predetermined values of the flow, the velocity and the thermal energy, inside the closed loop. Also, the heat exchanger is configured to transfer at least a part of the thermal energy of the pressurized gas to a process application. 112001200. A system () for delivery of thermal energy , the system () comprising:{'b': 1202', '1202, 'piping () for carrying a pressurized gas, the piping () forming a closed loop and having an inlet for receiving the pressurized gas;'}{'b': 1208', '1202, 'one or more velocity and pressure enhancers () connected along the piping (); and'}{'b': 1206', '1202, 'a heat exchanger () connected along the piping ();'}{'b': '1202', 'wherein the piping () is configured to receive the pressurized gas via the inlet and recirculate the pressurized gas inside the closed loop;'}{'b': '1208', 'wherein the one or more velocity and pressure enhancers () are configured to maintain flow, velocity and thermal energy of the pressurized gas to predetermined values of the flow, the velocity and the thermal energy, inside the closed loop; and'}{'b': '1206', 'wherein the heat exchanger () is configured to transfer at least a part of the thermal energy of the pressurized gas to a process application.'}21200. The system () as claimed in claim 1 , wherein the pressurized gas includes one or more of air claim 1 , CO claim 1 , Nand O.3120012011202. The system () as claimed in claim 1 , further comprising a valve () ...

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16-07-2020 дата публикации

COMPACT WASTEWATER CONCENTRATOR USING WASTE HEAT

Номер: US20200222826A1
Принадлежит:

A compact and portable liquid concentrator includes a gas inlet, a gas exit and a flow corridor connecting the gas inlet and the gas exit, wherein the flow corridor includes a narrowed portion that accelerates the gas through the flow corridor. A liquid inlet injects liquid into the gas stream at a point prior to the narrowed portion so that the gas-liquid mixture is thoroughly mixed within the flow corridor, causing a portion of the liquid to be evaporated. A demister or fluid scrubber downstream of the narrowed portion removes entrained liquid droplets from the gas stream and re-circulates the removed liquid to the liquid inlet through a re-circulating circuit. Fresh liquid to be concentrated is also introduced into the re-circulating circuit at a rate sufficient to offset the amount of liquid evaporated in the flow corridor. 1. A liquid concentrator system , comprising: a gas inlet,', 'a gas outlet,', 'a mixing corridor disposed between the gas inlet and the gas outlet, the mixing corridor having a narrowed portion in which gas flow within the mixing corridor accelerates when traveling from the gas inlet to the gas outlet; and', 'a liquid inlet through which liquid to be concentrated is injected into the mixing corridor, the liquid inlet disposed in the mixing corridor between the gas inlet and the narrowed portion;, 'a concentrator section including;'} a demister gas flow passage coupled to the gas outlet of the concentrator section,', 'a liquid collector disposed in the demister gas flow passage to remove liquid from gas flowing in the demister gas flow passage, and', 'a reservoir that collects the liquid removed from the gas flowing in the demister gas flow passage by the liquid collector; and, 'a demister disposed downstream of the concentrator section, the demister including;'}a fan coupled to the demister to assist gas flow through the mixing corridor and the gas flow passage, the fan being connected to a variable frequency drive motor that operates to vary ...

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25-08-2016 дата публикации

APPARATUS AND METHOD FOR EVAPORATING WASTE WATER AND REDUCING ACID GAS EMISSIONS

Номер: US20160243494A1
Принадлежит:

An apparatus for evaporating waste water and reducing flue gas acid gas emissions includes an evaporator device configured to receive a portion of flue gas emitted from a combustion unit and waste water for direct contact of the flue gas with the waste water to cool and humidify the flue gas, and to evaporate the waste water. An alkaline reagent as well as activated carbon may be mixed with the waste water prior to waste water contact with the flue gas. Solid particulates that are dried and entrained within the cooled and humidified flue gas can be separated from the flue gas via a particulate collector. 1. A method for evaporating waste water and reducing acid gas emissions in a combustion flue gas , comprising:supplying waste water to a heat exchanger for heating of the waste water to produce heated waste water;evaporating the heated waste water in a flash vessel collecting remaining waste water in the flash vessel;supplying the remaining waste water to an evaporator device arranged with a flow of the flue gas through the evaporator device for evaporation of the remaining waste water in the evaporator device; andsupplying the flue gas to a wet flue gas desulfurization system for absorption of acid gas from the flue gas to produce treated flue gas for release to the environment.2. The method of claim 1 , further comprising:adding at least one from a group consisting of activated carbon, activated coke, alkaline reagent, and anti-scaling agent, to the waste water prior to heating and evaporation of the waste water.3. The method of claim 1 , further comprising:supplying an absorbent liquid to the wet flue gas desulfurization system for absorption of acid gas from the flue gas upon contact with the flue gas.4. The method of claim 1 , wherein heating of the waste water in the heat exchanger is at a temperature of about 175° F. to about 350° F. claim 1 , or about 80° C. to about 180° C.5. The method of claim 1 , wherein heating of the waste water in the heat exchanger ...

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26-08-2021 дата публикации

HIGH-EFFICIENCY DESALINATION

Номер: US20210262736A1
Автор: Lum Gary, Thiers Eugene
Принадлежит:

Embodiments of the invention provide systems and methods for heat transfer systems at temperatures in the range of 20 C to 800 C. The systems consist of heat pipes configured such that they fit inside conventional heat exchangers, and more effectively transfer or recover heat from hot fluids, and that operate without user intervention over long periods of time. 1. A system , comprising:a first heat source;a heating vessel containing a saline solution having a first salinity;a first plurality of heat pipes, wherein a first portion of each heat pipe is in thermal communication with the first heat source and a second portion of each heat pipe is in thermal communication with the saline solution in the heating vessel;a forward osmosis vessel containing a semipermeable membrane;a draw solution vessel containing a draw solution having a second salinity, wherein the second salinity is higher than the first salinity; anda draw solution recovery system.2. The system of wherein the system is configured to heat the saline solution in the heating vessel to form a heated saline solution claim 1 , to receive the heated saline solution in the forward osmosis vessel where water is removed from the heated saline solution and combined with the draw solution to form a dilute draw solution claim 1 , to receive the diluted draw solution into the draw solution recovery system where water is removed from the diluted draw solution to recover the draw solution claim 1 , and to receive the draw solution into the draw solution vessel.3. The system of claim 2 , further comprising a second plurality of heat pipes claim 2 , wherein a first portion of each heat pipe is in thermal communication with a second heat source claim 2 , and a second portion of each heat pipe is in thermal communication with the draw solution recovery system.4. The system of wherein the second plurality of heat pipes is configured to heat the diluted draw solution in the draw solution recovery system.5. The system of ...

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01-09-2016 дата публикации

Air pollution control system, air pollution control method, spray drying device of dewatering filtration fluid from desulfurization discharged water, and method thereof

Номер: US20160250588A1
Принадлежит: Mitsubishi Hitachi Power Systems Ltd

To include a boiler 11 that burns fuel F, an air heater 13 that recovers heat of flue gas 18 from the boiler 11 , a first precipitator 14 that reduces dust in the flue gas 18 after heat recovery, a desulfurizer 15 that reduces sulfur oxides in the flue gas 18 after dust reduction by an absorbent, a dewaterer 32 that reduces gypsum 31 from desulfurization discharged water 30 discharged from the desulfurizer 15 , a spray drying device 34 including an atomizer that atomizes a dewatering filtration fluid 33 discharged from the dewaterer 32 , and a flue-gas introducing line L 11 that introduces a part of the flue gas 18 into the spray drying device 34.

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08-08-2019 дата публикации

SOLAR HUMIDIFIER AND DEHUMIDIFIER DESALINATION METHOD AND SYSTEM FOR THE DESALINATION OF SALINE WATER

Номер: US20190241444A1
Принадлежит:

A solar powered humidification-dehumidification desalination system comprises or consists of a supply of seawater or brackish water referred to hereinafter as saline water passing through a dehumidifier condenser. The saline water passes a dehumidifier condenser and is preheated in the dehumidifier condenser or immediately before the dehumidifier condenser and thereafter due to the condensation process. A single humidification stage or multiple humidification stages include humidifier(s) and respective solar collectors. The solar collectors heat water and the heated water passes through the respective dehumidifiers to evaporate the preheated saline water to thereby separate pure water from the brine. The heated air is reheated and recirculated through the humidifying stages and dehumidifier and the desalinated water from condensation in the dehumidifier is collected and processed. Recirculating the brine from each humidifier utilizes the latent heat therein for more efficient evaporation and less energy consumption. 1. A solar humidifier-dehumidifier desalination system for desalination of saline water , adjacent a source of seawater or the like , said system comprising:a plurality of evacuated tubular collectors, a first storage tank for cold seawater and a second storage tank for heated seawater, a humidifier, and a condenser/dehumidifier;pumping means for moving saline water from said source of seawater or the like to and through said solar thermal collectors for heating said saline water to a temperature within a range of between about 50° C. and 90° C. and moving said heated and humidified air from said humidifier to and into said condenser/dehumidifier;separating and delivering desalinated water to a first outlet and hot seawater to a second outlet for preheating seawater to said hot water storage tank and returning a portion of said concentrated seawater to a disposal; andsizing said system to maintain its operation during periods of darkness.2. The solar ...

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14-09-2017 дата публикации

WATER ATOMISATION DEVICE

Номер: US20170259283A1
Автор: BIRD Garth John
Принадлежит:

A water atomisation device for water evaporation and/or dust control. The device includes: a generally longitudinally hollow housing; a fan; a motor; and a hollow manifold. The housing extends between an inlet end and an outlet end, with the inlet end defining a first air inlet to an interior of the housing. The fan is within the housing, between the inlet end and the outlet end. The motor drives the fan. The manifold is shaped to generally correspond to that of the outlet end and has a plurality of water injector nozzles directed substantially inwardly and away from the outlet end. A distal edge of the outlet end is longitudinally spaced apart from a proximal edge of the manifold to define a second air entrainment inlet to an interior of the manifold. 1. A water atomisation device for water evaporation and/or dust control , the device including:a generally longitudinally hollow housing extending between an inlet end and an outlet end, the inlet end defining a first air inlet to an interior of the housing;a fan within the housing between the inlet end and the outlet end;a motor for driving the fan; anda hollow manifold shaped to generally correspond to that of the outlet end and having a plurality of water injector nozzles directed substantially inwardly and away from the outlet end.wherein a distal edge of the outlet end is longitudinally spaced apart from a proximal edge of the manifold to define a second air entrainment inlet to an interior of the manifold.2. The water atomisation device as claimed in claim 1 , wherein the distal edge of the outlet end is longitudinally spaced apart from the proximal edge of the manifold by about 35 mm.3. The water atomisation device as claimed in claim 1 , wherein the housing is generally cylindrical.4. The water atomisation device as claimed in claim 1 , wherein the housing inlet end includes a venturi part claim 1 , converging towards the outlet end.5. The water atomisation device as claimed in claim 1 , wherein the housing ...

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28-10-2021 дата публикации

SYSTEM AND METHOD FOR SORBTION DISTILLATION

Номер: US20210331944A1
Автор: Yuh Howard Y.
Принадлежит:

A system for distilling water is disclosed. The system comprises a heat source, and a plurality of open-cycle adsorption stages, each stage comprising a plurality of beds and an evaporator and a condenser between a first bed and a second bed, wherein each bed comprises at least two vapor valves, a plurality of hollow tubes, a plurality of channels adapted for transferring water vapor to and from at least one of the condenser or the evaporator, a thermally conductive water vapor adsorbent, and wherein each vapor valve connects a bed to either the condenser or the evaporator. 1. A method of distilling water , comprising the steps of:a. providing a plurality of stages, each stage comprising a hot adsorbent bed and a cold adsorbent bed, and each stage has an upper and lower operating temperature limit, the difference between the upper and lower operating temperature limit being less than about 20° C.; i. providing an external heat source to heat the hot bed of a first stage to a first temperature;', 'ii. desorbing water vapor from the hot bed of the first stage and flowing water vapor into a first condenser;', 'iii. condensing water vapor in the first condenser to form a liquid water and removing at least some of the liquid water from the first condenser;', 'iv. providing a solution comprising water and at least one dissolved impurity to a first evaporator, the solution having a temperature predetermined to suit the equilibrium uptake of an adsorbent, where a suitable temperature is predetermined by first selecting both a desired operational temperature range and uptake range for the adsorbent, then selecting the solution temperature such that the saturated water vapor partial pressure corresponds to the desired adsorbent temperature and uptake range;', 'v. transferring a forcing phase latent heat of vaporization from vapor condensing in the first condenser to the first evaporator to evaporate the solution comprising water and at least one dissolved impurity to form ...

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21-09-2017 дата публикации

Compact wastewater concentrator using waste heat

Номер: US20170266581A1
Принадлежит: Heartland Water Technology Inc

A compact and portable liquid concentrator includes a gas inlet, a gas exit and a flow corridor connecting the gas inlet and the gas exit, wherein the flow corridor includes a narrowed portion that accelerates the gas through the flow corridor. A liquid inlet injects liquid into the gas stream at a point prior to the narrowed portion so that the gas-liquid mixture is thoroughly mixed within the flow corridor, causing a portion of the liquid to be evaporated. A demister or fluid scrubber downstream of the narrowed portion removes entrained liquid droplets from the gas stream and re-circulates the removed liquid to the liquid inlet through a re-circulating circuit. Fresh liquid to be concentrated is also introduced into the re-circulating circuit at a rate sufficient to offset the amount of liquid evaporated in the flow corridor.

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05-09-2019 дата публикации

SPRAY DRYING SYSTEM

Номер: US20190270049A1
Принадлежит: Mitsubishi Hitachi Power Systems, Ltd.

A spray flying system for drying wastewater to be dried includes: an exhaust as introduction line for introducing the exhaust gas discharged from an exhaust gas generation source, the exhaust gas introduction line being connected to a plurality of exhaust gas ducts for allowing the exhaust gas to flow through; and at least one spray drying device connected to the exhaust gas introduction line and configured to bring the exhaust gas introduced from the exhaust gas introduction line into contact with the wastewater. The number of spray drying device is smaller than the number of the plurality of exhaust gas ducts. 1. A spray drying system for drying wastewater to be dried , the spray drying system comprising:an exhaust gas introduction line for introducing the exhaust gas discharged from an exhaust gas generation source, the exhaust gas introduction line being connected to a plurality of exhaust gas ducts for allowing the exhaust gas to flow through; andat least one spray drying device connected to the exhaust gas introduction line and configured to bring the exhaust gas introduced from the exhaust gas introduction line into contact with the wastewater,wherein the number of spray drying device is smaller than the number of the plurality of exhaust gas ducts.2. The spray drying system according to claim 1 ,wherein the exhaust gas introduction line is connected to each of the plurality of exhaust gas ducts.3. The spray drying system according to claim 2 , an upstream-side exhaust gas introduction line connected to each of the plurality of exhaust gas ducts;', 'an introduction-side merge part at which each of the upstream-side exhaust gas introduction line merges; and', 'a single downstream-side exhaust gas introduction line connecting the introduction-side merge part and the spray drying device., 'wherein the exhaust gas introduction line includes4. The spray drying system according to claim 2 ,wherein a heat exchanger configured to exchange heat with the exhaust gas is ...

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05-10-2017 дата публикации

Efficient and Energy-Saving Wastewater Evaporation Crystallizer

Номер: US20170282094A1

The present disclosure relates to a wastewater flue evaporating device. An wastewater evaporation crystallizer is provided, including an evaporating tube inlet, an inlet flange, an inlet chamber, a pneumatic inlet baffle, an evaporating tube body, a pneumatic outlet baffle, an outlet chamber, an outlet flange, and an evaporating tube outlet which are successively coupled, where the evaporating tube inlet is connected to provide a gas pipeline; the gas pipeline is connected on a flue between an external denitration device and an air preheater; the evaporating tube outlet is communicated with an inlet flue of a dust collector; the evaporating tube body is provided with a wastewater nozzle; and the wastewater nozzle is communicated with a pretreated waste pipe. The present disclosure provides an efficient and energy-saving wastewater evaporation crystallizer which increases evaporation efficiency by bringing in a high-temperature gas at a front end of the air preheater.

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03-09-2020 дата публикации

EVAPORATION PANEL SYSTEMS AND ASSEMBLIES

Номер: US20200277200A1
Автор: Patey Michael J.
Принадлежит: ECOVAP, INC.

The present disclosure evaporation panel systems including plurality of evaporation panels, wherein a first evaporation panel and a second evaporation panel of the plurality of evaporation panels each include evaporation shelves and support columns to support and separate to the evaporation shelves. At least a portion of the support columns include evaporation fins so that wastewater is loadable along the support column. The first evaporation panel and the second evaporation panel in this example are releasably connectable to one another to form a sub-assembly. 1. An evaporation panel system , comprising a plurality of evaporation panels , wherein a first evaporation panel and a second evaporation panel of the plurality of evaporation panels each include:evaporation shelves; andsupport columns to support and separate to the evaporation shelves, wherein at least a portion of the support columns include evaporation fins so that wastewater is loadable along the support column,wherein the first evaporation panel and the second evaporation panel are releasably connectable to one another to form a sub-assembly.2. The evaporation panel system of claim 1 , wherein the evaporation fins at an individual support column are vertically aligned and spaced apart so that when wastewater is received at the support column claim 1 , a vertical water column along the individual evaporation fin is formed.3. The evaporation panel system of claim 1 , wherein the evaporation fins have a shape of a perpendicular cross-section of an airfoil taken from a leading edge to a trailing edge thereof.4. The evaporation panel system of claim 1 , wherein the plurality of evaporation panels further includes a third evaporation panel which also includes evaporation shelves support columns configured the same as the first evaporation panel and the second evaporation panel claim 1 , and wherein the third evaporation panel is releasably connectable to the first evaporation panel and the second evaporation ...

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03-09-2020 дата публикации

EVAPORATION PANELS

Номер: US20200277201A1
Автор: Patey Michael J.
Принадлежит: ECOVAP, INC.

An evaporation panel can include a first evaporation shelf including a first upper surface and a first lower surface, a second evaporation shelf positioned beneath the first evaporation shelf and having a second upper surface, and a support column disposed between the first evaporation shelf and the second evaporation shelf. In this example, the support column can include an evaporation fin. 1. An evaporation panel , comprising:a first evaporation shelf including a first upper surface and a first lower surface;a second evaporation shelf positioned beneath the first evaporation shelf, the second evaporation shelf having a second upper surface; anda support column disposed between the first evaporation shelf and the second evaporation shelf, wherein the support column includes an evaporation fin.2. The evaporation panel of claim 1 , comprising a plurality of support columns disposed between the first evaporation shelf and the second evaporation shelf claim 1 , wherein the first lower surface claim 1 , the second upper surface claim 1 , and two support columns of the plurality of support columns define a female-receiving opening.3. The evaporation panel of claim 2 , wherein the first evaporation shelf and the second evaporation shelf are laterally elongated and horizontally oriented claim 2 , the evaporation panel further comprising a first male connector positioned on a first lateral end of the evaporation panel and a second male connector positioned on a second lateral end of the evaporation panel claim 2 , wherein the first male connector and the second male connector are configured to be received by a female receiving of another evaporation panel having the same configuration as the evaporation.4. The evaporation panel of claim 1 , comprising multiple evaporation fins positioned along a support column claim 1 , wherein the multiple fins are spaced apart at from 0.2 cm to 1 cm so that when wastewater is loaded at the support column claim 1 , the evaporation fins ...

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03-09-2020 дата публикации

WASTEWATER EVAPORATIVE SEPARATION SYSTEMS

Номер: US20200277202A1
Автор: Patey Michael J.
Принадлежит: ECOVAP, INC.

A wastewater evaporative separation system can include an evaporation panel assembly having a plurality of individual evaporation panels laterally and releasably joined together, the evaporation panel assembly configured for receiving wastewater from a body of wastewater and evaporating water therefrom as the wastewater cascades down the evaporation panel assembly and contaminants become more concentrated. The system also includes a wastewater delivery system fluidly associated with the body of wastewater with a fluid directing assembly delivering the wastewater from the body of wastewater to an upper portion of the evaporation panel assembly. 1. A wastewater evaporative separation system , comprising:an evaporation panel assembly including a plurality of individual evaporation panels laterally and releasably joined together, the evaporation panel assembly configured for receiving wastewater from a body of wastewater and evaporating water therefrom as the wastewater cascades down the evaporation panel assembly and contaminants become more concentrated; anda wastewater delivery system fluidly associated with the body of wastewater, the wastewater delivery system including a fluid directing assembly delivering wastewater from the body of wastewater to an upper portion of the evaporation panel assembly.2. The wastewater evaporative separation system of claim 1 , wherein the evaporation panel assembly includes at least 10 discrete evaporation panels claim 1 , a first portion of which are laterally joined together and a second portion of which are laterally joined together stacked on top of the first portion.3. The wastewater evaporative separation system of claim 1 , wherein the evaporation panel assembly includes at least 50 discrete evaporation panels claim 1 , a first portion of which are laterally joined together claim 1 , a second portion of which are laterally joined together stacked on top of the first portion claim 1 , and a third portion of which are laterally ...

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20-10-2016 дата публикации

METHOD FOR ON-SITE AERIAL DISSEMINATION AND ATMOSPHERIC DISPOSAL OR "AEROSOLIZATION" OF THE WATER COMPONENT OF ALL LEACHATES AND WASTEWATERS

Номер: US20160304357A1
Автор: Houston Kelly K.
Принадлежит:

A method for on-site aerial dissemination of Oxidatively Converted particles of contamination with substantial atmospheric disposal, commonly known as aerosolization, of the water component of all untreated or partially treated leachates and all untreated or partially treated wastewaters. These leachates and wastewaters (defined as water containing 2 or more detectable and known contaminants) are collected on site and the defined leachate or defined wastewater, having multiple defined and known contaminating suspended and perhaps precipitated solids therein, and aerially disseminating or aerially oxidizing or commonly known aerosolizing said contaminants over a chosen contaminant collections area (defined as 1-300 meters from the nozzles) and disposing of the water component of the leachate or wastewater through atmospheric disposal and lastly evaporation on the site of the leachate or wastewaters' generation. The commercial process can be known as “AerosoliZLD” leachate or wastewater disposal under the intent of Federal Zero Liquid Discharge (ZLD) regulations. 1. A method of disseminating and disposing of wastewater containing contaminating suspended solids by an aerosolization process , comprising:generating a system of air;pumping the wastewater and contaminating suspended solids to a series of nozzles configured and designed to enhance oxidation of the contaminating suspended solids emitted from the nozzles;emitting the wastewater and contaminating suspended solids from the nozzles and mixing the wastewater and contaminating suspended solids with the system of air to form an aerosolized wastewater-air mixture;propelling the aerosolized wastewater-air mixture through the atmosphere and over a defined solids collection area and as the contaminating suspended solids in the wastewater-air mixture move through the atmosphere; causing the oxidation of the contaminating suspended solids and causing the now oxidized contaminating suspended solids to become larger and ...

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03-10-2019 дата публикации

COMPACT CONTAINERIZED SYSTEM AND METHOD FOR SPRAY EVAPORATION OF WATER

Номер: US20190299114A1
Принадлежит: Energy Water Solutions, LLC

A wastewater evaporation system for spray evaporating water comprising: a wastewater feed inlet; a pump, wherein an outlet of the wastewater inlet is fluidly connected to an inlet of the pump and wherein an outlet of the pump is fluidly connected to an inlet of a manifold; a drip orifice, wherein an outlet of the manifold is fluidly connected to an inlet of the drip orifice; a container, wherein an upper portion of the container is enclosed with a demister element; a packing system and/or a tray system disposed within the container, wherein the outlet of the drip orifice discharges water droplets onto the packing system and/or the tray system; a discharge outlet, wherein a bottom of the container is fluidly connected to the discharge outlet; and an air system comprising an air blower and optionally an air preheater, wherein the air system is disposed through a wall of the container and wherein the air system discharges air flow counter to the water droplets from the drip orifice. A method of spray evaporating water while limiting emission of particles regulated as pollutants is also disclosed. 1. A wastewater evaporation system for spray evaporating water comprising:a. a wastewater feed inlet;b. a pump, wherein an outlet of the wastewater inlet is fluidly connected to an inlet of the pump and wherein an outlet of the pump is fluidly connected to an inlet of a manifold;c. a drip orifice, wherein an outlet of the manifold is fluidly connected to an inlet of the drip orifice;d. a container, wherein an upper portion of the container is enclosed with a demister element;e. a packing system and/or a tray system disposed within the container, wherein the outlet of the drip orifice discharges wastewater and/or water droplets onto the packing system and/or tray system;f. a discharge outlet, wherein a bottom of the container is fluidly connected to the discharge outlet; andg. an air system comprising an air blower and, optionally, an air preheater, wherein the air system is ...

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10-11-2016 дата публикации

SPRAY DRYING APPARATUS AND AIR POLLUTION CONTROL SYSTEM

Номер: US20160325203A1
Принадлежит: Mitsubishi Hitachi Power Systems, Ltd.

A spray drying apparatus includes: a gas inlet provided in a side wall in the vicinity of a top (lid) portion of the spray drying apparatus, for introducing a flue gas for drying a spray of dehydrated filtrate; flow-adjusting plates provided in a body of the spray drying apparatus, for decelerating the introduced flue gas so as to change the flow of the flue gas to a laminar flow; a spray nozzle for spraying the dehydrated filtrate from the desulfurization waste water into the flue gas having been changed to the laminar flow; and a joining unit for joining a bottom portion of the body of the spray drying apparatus to a gas supply line that is a main flue gas duct for the flue gas so as to discharge spray-dried solids to the main flue gas duct. 1. A spray drying apparatus , comprising:a body;a gas inlet provided to the body and introducing a flue gas;a spray nozzle for spraying waste water into the flue gas in order to evaporate and dry the waste water;a flue gas introduction line connected to the gas inlet and supplying the flue gas; anda main flue gas duct connected to a bottom of the body of the spray drying apparatus,wherein an upstream end of the flue gas introduction line is connected to and branches from an upstream portion of the main flue gas duct.2. The spray drying apparatus as set forth in claim 1 , whereinthe gas inlet is provided to the body in the vicinity of a top portion of the spray drying apparatus.3. The spray drying apparatus as set forth in claim 1 , wherein:the flue gas and spray-dried solids are discharged from the body to the main flue gas duct.4. The spray drying apparatus as set forth in claim 1 , wherein:the main flue gas duct and the body of the spray drying apparatus are connected so that flow direction of the flue gas and spray-dried solids flow is perpendicular to an extending direction of the main flue gas duct.5. The spray drying apparatus as set forth in claim 1 , wherein:the main flue gas duct includes a portion extending ...

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23-11-2017 дата публикации

Systems And Methods For Concentrating Waste Water Fluids

Номер: US20170333807A1
Принадлежит:

A method and apparatus for processing waste water generated during oilfield drilling operations with a mobile processing unit utilizing heat energy sourced from burning hydrocarbon fuel directly and/or capturing and using the exhaust heat energy generated by burning hydrocarbons in engines such as diesel engines in order to vaporize a dominant mass of the aqueous phase of the waste water while clarifying the heat source combustion gasses. The water vapor generated by the vaporization process may be discharged directly to the atmosphere or alternately condensed and captured for use as potable water. The residual waste water is thereby concentrated and the cost to dispose of the waste water is greatly reduced. 1. An evaporator for vaporizing raw water from oilfield operations and concentrating contaminants within the raw water , where the raw water contains oil , salt and particulate contaminants comprising:an internal combustion engine configured to provide a hot gas source;a raw water evaporator having a stack and a flue connected to the hot gas source and wherein the stack is operatively positioned over and surrounding the flue;a raw water distribution system configured to distribute raw water within the hot combustion gas within the stack to increase raw water surface area;a control system and pump operatively connected to the raw water distribution system, the control system and pump operable to distribute a flow rate of raw water through the raw water distribution system within the stack while maintaining raw water flow sufficient to minimize scaling within the raw water evaporator during operation to enable optimum evaporation of water within the flue; anda concentrated raw water collection system connected to the stack for collecting concentrated raw water from the stack and recirculating raw water to the stack.2. The evaporator of claim 1 , further comprising a first tank operatively connected to the raw water evaporator claim 1 , the first tank for receiving ...

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22-11-2018 дата публикации

WASTEWATER EVAPORATIVE SEPARATION SYSTEMS

Номер: US20180334393A1
Автор: Patey Michael J.
Принадлежит: ECOVAP, INC.

A wastewater evaporative separation system can include an evaporation panel assembly and a wastewater delivery system. The evaporative panel assembly can include at least 10 individual evaporation panels laterally joined together and fluidly coupled to a body of wastewater. The evaporation panel assembly can be configured for receiving wastewater from the body of wastewater and evaporating water therefrom as the wastewater cascades down the evaporation panel assembly and contaminants generally become more concentrated. The wastewater delivery system can be associated with the body of wastewater and can include a fluid directing assembly delivering wastewater from the body of wastewater to an upper portion of the evaporation panel assembly. 1. A wastewater evaporative separation system , comprising:an evaporation panel assembly including at least 10 individual evaporation panels laterally joined together and fluidly coupled to a body of wastewater, the evaporation panel assembly configured for receiving wastewater from the body of wastewater and evaporating water therefrom as the wastewater cascades down the evaporation panel assembly and contaminants generally become more concentrated; anda wastewater delivery system fluidly associated with the body of wastewater, the wastewater delivery system including a fluid directing assembly delivering wastewater from the body of wastewater to an upper portion of the evaporation panel assembly.2. The wastewater evaporative separation system of claim 1 , wherein the evaporation panel assembly includes at least 50 discrete evaporation panels claim 1 , a first portion of which are laterally joined together and a second portion of which are laterally joined together stacked on top of the first portion.3. The wastewater evaporative separation system of claim 1 , wherein the evaporation panel assembly includes at least 500 discrete evaporation panels claim 1 , a first portion of which are laterally joined together claim 1 , a second ...

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08-12-2016 дата публикации

Production Salt Water Recycle/Disposal Process

Номер: US20160355408A1
Автор: J. Keith Betts
Принадлежит: Individual

A method for recycling production salt water comprises receiving production salt water from an oil well. The production salt water is separated into separate streams of salt water and oil. The salt water is pre-heated to a temperature no less than 2 degrees Fahrenheit below the boiling point of the salt water. The pre-heated salt water is transferred to a separation tank, and the heated salt water is separated in the separation tank into steam and salt by boiling water.

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07-12-2017 дата публикации

APPARATUS AND METHOD FOR CONCENTRATING BRINE

Номер: US20170349452A1
Принадлежит:

An apparatus and process are provided for concentrating oil and gas production brine. The apparatus comprises a brine feed system, a hot air generation system, a concentrated brine collection and recirculation system, and an evaporation tower. The evaporation tower includes a brine inlet coupled to the brine feed system, a hot air inlet coupled to the hot air generation system and positioned below the brine inlet, a steam discharge, a concentrated brine outlet, a plurality of distillation trays, and a concentrated brine reservoir in the lower portion of the tower. The evaporation tower also has a distributor at the brine inlet adapted to distribute brine onto the trays and may have a plurality of spray nozzles disposed above the hot air inlet to distribute a spray of recirculated concentrated brine. Water evaporates from the brine and the entering hot air temperature is modulated by evaporation. 1. An apparatus for concentrating oil and gas production brine , the apparatus comprising: '(i) a brine inlet coupled to the brine feed system, (ii) a hot air inlet coupled to the hot air generation system and positioned lower than the brine inlet, (iii) a steam discharge, (iv) a concentrated brine outlet, (v) at least one distillation tray positioned below the brine inlet and above the hot air inlet, (vi) a distributor coupled to the brine inlet and adapted to distribute brine onto the at least one distillation tray, and (vii) a lower portion of the tower configured to house a concentrated brine reservoir; and', '(a) a brine feed system, (b) a hot air generation system, (c) a concentrated brine collection and recirculation system, and (d) an evaporation tower includingwherein the apparatus is adapted to remove a portion of water from the oil and gas production brine to produce a concentrated brine.2. The apparatus of claim 1 , wherein the concentrated brine collection and recirculation system further comprises a plurality of spray nozzles disposed above the hot air inlet ...

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06-12-2018 дата публикации

EVAPORATION PANELS

Номер: US20180345165A1
Автор: Patey Michael J.
Принадлежит: ECOVAP, INC.

The present disclosure is drawn to an example evaporation panel, which can include an evaporation shelf that is laterally elongated and horizontally oriented and can include an upper surface and a lower surface. A second evaporation shelf can also be included that is laterally elongated and positioned in parallel beneath the evaporation shelf. The second evaporation shelf can have a second upper surface. The evaporation panel can further include a support column between the first evaporation shelf and the second evaporation shelf. The support column can include a plurality of stacked and spaced apart evaporation fins oriented in parallel with the evaporation shelf. 1. An evaporation panel , comprising:an evaporation shelf that is laterally elongated and horizontally oriented, the evaporation shelf including an upper surface and a lower surface;a second evaporation shelf that is laterally elongated and is positioned in parallel beneath the evaporation shelf, the second evaporation shelf having a second upper surface; anda support column between the first evaporation shelf and the second evaporation shelf, wherein the support column includes a plurality of stacked and spaced apart evaporation fins oriented in parallel with the evaporation shelf.2. The evaporation panel of claim 1 , wherein the first lower surface includes a downwardly extending ridge that is laterally elongated along the first lower surface claim 1 , and wherein the second upper surface includes an upwardly extending ridge that is laterally elongated along the second upper surface.3. The evaporation panel of claim 2 , wherein the first lower surface and the second upper surface partially define a female-receiving opening.4. The evaporation panel of claim 1 , further comprising a first column of male connectors positioned on a first lateral end of the evaporation panel and a second column of male connectors positioned on a second lateral end of the evaporation panel claim 1 , wherein all of the male ...

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06-12-2018 дата публикации

EVAPORATION PANEL SYSTEMS AND ASSEMBLIES

Номер: US20180345166A1
Автор: Patey Michael J.
Принадлежит: ECOVAP, INC.

The present disclosure evaporation panel systems including a plurality of evaporation panels. The evaporation panels can include a plurality of evaporation shelves that are laterally elongated, vertically stacked, spaced apart from one another, and horizontally oriented; and a plurality of vertical support columns positioned laterally along the plurality of evaporation shelves to provide support and separation to the plurality of evaporation shelves. The evaporation panels can also include a plurality of female-receiving openings which are individually bordered by two evaporation shelves and two support columns; and a plurality of male connectors positioned at lateral ends of both the first evaporation panel and the second evaporation panels. The first evaporation panel and the second evaporation panel can be orthogonally connectable via the male connectors of the first evaporation panel and the female-receiving openings of the second evaporation panel. 1. An evaporation panel system , comprising a plurality of evaporation panels , wherein a first evaporation panel and a second evaporation panel of the plurality of evaporation panels each include:a plurality of evaporation shelves that are laterally elongated, vertically stacked, spaced apart from one another, and horizontally oriented;a plurality of vertical support columns positioned laterally along the plurality of evaporation shelves to provide support and separation to the plurality of evaporation shelves;a plurality of female-receiving openings which are individually bordered by two evaporation shelves and two support columns; anda plurality of male connectors positioned at lateral ends of both the first evaporation panel and the second evaporation panels,wherein the first evaporation panel and the second evaporation panel are orthogonally connectable via the male connectors of the first evaporation panel and the female-receiving openings of the second evaporation panel.2. The evaporation panel system of claim ...

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15-12-2016 дата публикации

CONTAINERIZED SYSTEM AND METHOD FOR SPRAY EVAPORATION OF WATER

Номер: US20160362307A1
Принадлежит: Energy Water Solutions, LLC

A system for spray evaporating water comprising: a wastewater inlet; a pump, where an outlet of the wastewater inlet is fluidly connected to an inlet of the pump and wherein an outlet of the pump is fluidly connected to an inlet of a manifold; a spray nozzle, wherein an outlet of the manifold is fluidly connected to an inlet of the spray nozzle; a container, wherein an upper portion of the container is enclosed with a demister element and wherein the outlet of the spray nozzle discharges into the container; and a discharge outlet, wherein a bottom of the container is fluidly connected to the discharge outlet. A method of spray evaporating water is also disclosed. 1. A system for spray evaporating water comprising:a. a wastewater inlet;b. a pump, where an outlet of the wastewater inlet is fluidly connected to an inlet of the pump and wherein an outlet of the pump is fluidly connected to an inlet of a manifold;c. a spray nozzle, wherein an outlet of the manifold is fluidly connected to an inlet of the spray nozzle;d. a container, wherein an upper portion of the container is enclosed with a demister element and wherein the outlet of the spray nozzle discharges into the container; ande. a discharge outlet, wherein a bottom of the container is fluidly connected to the discharge outlet.2. The system of claim 1 , wherein the pump produces a water flow rate into the system from about 15 GPM to about 100 GPM.3. The system of claim 1 , wherein the spray nozzle is selected from the group consisting of plain-orifice nozzles claim 1 , shaped-orifice nozzles claim 1 , surface impingement spray nozzles claim 1 , spiral spray nozzles claim 1 , and pressure swirl spray nozzles.4. The system of claim 3 , wherein the spray nozzle is a surface impingement spray nozzle claim 3 , wherein the spray nozzle is capable of from about 3 GPM to about 8 GPM.5. The system of claim 3 , wherein the spray nozzle produces water droplet sizes from about 50 μm to about 1 claim 3 ,000 μm.6. The system ...

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06-12-2018 дата публикации

EVAPORATION PANEL SECURING SYSTEMS

Номер: US20180347910A1
Автор: Patey Michael J.
Принадлежит: ECOVAP, INC.

Evaporation panel securing system can include first and second evaporation panels, and a security fastener to secure a male connector (first evaporation panel) within a female-receiving opening (second evaporation panel) in an orthogonally joined orientation, for example. The evaporation panels can include a plurality of evaporation shelves that are laterally elongated, vertically stacked, spaced apart from one another, and horizontally oriented; a plurality of vertical support columns positioned laterally along the plurality of evaporation shelves to provide support and separation to the plurality of evaporation shelves; a plurality of female-receiving openings individually bordered by two evaporation shelves and two support columns; and a plurality of male connectors positioned laterally at ends of the plurality of evaporation panels, wherein the male connectors of the first evaporation panel are releasably joinable with female-receiving openings of the second evaporation panel. 1. An evaporation panel securing system , comprising: a plurality of evaporation shelves that are laterally elongated, vertically stacked, spaced apart from one another, and horizontally oriented;', 'a plurality of vertical support columns positioned laterally along the plurality of evaporation shelves to provide support and separation to the plurality of evaporation shelves;', 'a plurality of female-receiving openings individually bordered by two evaporation shelves and two support columns; and', 'a plurality of male connectors positioned laterally at ends of the plurality of evaporation panels, wherein the male connectors of the first evaporation panel are releasably joinable with female-receiving openings of the second evaporation panel; and, 'a plurality of evaporation panels, wherein a first evaporation panel and a second evaporation panel of the plurality of evaporation panels individually includea security fastener to secure a male connector of the first evaporation panel within a ...

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22-12-2016 дата публикации

WATER TREATMENT SYSTEM AND METHOD

Номер: US20160367936A1
Принадлежит: MITSUBISHI HEAVY INDUSTRIES, LTD.

The water treatment system includes: a wet desulfurization device that removes sulfur oxide present in boiler flue gas; a dewatering device that separates gypsum from desulfurization waste water containing gypsum slurry; a reaction tank to which separated water from the dewatering device is introduced, and which immobilizes heavy metals present in the separated water by inputting a chelating agent; a solid-liquid separation unit that performs solid-liquid separation with respect to heavy metal sludge present in the separated water; a mixing unit that mixes the separated water obtained with effluent generated in a plant facility; a desalination device that removes salt content from the mixed water mixed by the mixing unit; and a spray drying device that includes a spray unit, which sprays concentrated water in which the salt content has been concentrated by the desalination device, and that performs spray drying using a part of the boiler flue gas. 1. A water treatment system comprising:a wet desulfurization device that removes sulfur oxide from boiler flue gas;a dewatering device that separates gypsum from desulfurization waste water which contains gypsum slurry and which is obtained from the wet desulfurization device;a mercury removing unit to which is introduced separated water that is obtained from the dewatering device, and which immobilizes heavy metals present in the separated water by inputting a chelating agent;a solid-liquid separation unit that performs solid-liquid separation with respect to solid content present in separated water obtained from the mercury removing unit;a mixing unit that mixes separated water obtained from the solid-liquid separation unit with effluent generated in a plant facility;a desalination device that removes salt content from mixed water obtained by the mixing unit; anda spray drying device that includes a spraying unit, which sprays concentrated water in which salt content has been concentrated by the desalination device, and ...

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22-12-2016 дата публикации

High Efficiency, Large Scale Desalination System

Номер: US20160368784A1
Автор: HAYNES Joel
Принадлежит:

An apparatus and method for the distillation of ocean and brackish water that includes a means for using the ambient temperatures of seawater and air to continually transfer the heat energy, from the outer perimeters of the system, back into the, centrally located, evaporation chamber and insulation for preventing heat from escaping to the atmosphere. The insulation comprises a first and second wall surrounding the basic assemblies of a desalination system in which the space between the first and second wall is under low partial vacuum and is partially filled with an insulation material for structural support. The system provides a feed through means that prevent heat transfer through the structural connections between the first and second walls. The system provides an evaporation system for flash evaporation by atomizing the input contaminated water, preheated by the heat of condensation into very small liquid droplets, which are then sprayed into a stream of hot dry air. The liquid rapidly evaporates leaving behind hot dry solids that is recaptured and used to preheat the input contaminated water. 1. A desalination system for substantially increasing the efficiency of the distillation of seawater , comprising:a double-wall assembly, comprising a first wall exposed to an environment and a second wall internal to and coextensive with the first wall to create a space in between the first wall and the second wall, wherein the space is a low partial vacuum and filled with a structural insulation, wherein the second wall defines an internal cavity, wherein the double-wall assembly defines a single opening into the internal cavity located at a first end of the desalination system;a feed-through assembly mounted within the opening of the double-wall assembly, the feed-through assembly comprising an intake port to take in the seawater, an exit port in fluid connection with the intake port to deliver the seawater into the internal cavity, a receiver port to receive ...

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31-12-2015 дата публикации

Air pollution control system and air pollution control method

Номер: US20150375166A1
Принадлежит: Mitsubishi Hitachi Power Systems Ltd

Provided is an air pollution control system including: a denitration apparatus; an air heater; a precipitator; a desulfurization apparatus; a dehydrator; a spray drying apparatus provided with a spray unit that is configured to spray dehydrated filtrate supplied from the dehydrator; a flue gas introduction line through which a branch gas branched from the flue gas is introduced to the spray drying apparatus; a flue gas supply line through which a flue gas from the spray drying apparatus returns to a main flue gas duct; a solid content separator that performs a solid-gas separation on solid contents contained in the flue gas; and a kneader that performs kneading and immobilizing treatment on the separated solid contents together with an immobilization aid.

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21-11-2019 дата публикации

Method and Device for Cooling a Fluid Stream of an Electrolysis Unit and for Obtaining Water

Номер: US20190352887A1
Принадлежит: SIEMENS AKTIENGESELLSCHAFT

A method for cooling a fluid from an electrolysis unit and extracting water from ambient air comprising: conducting moist air having a first molar amount of water and raw water into an evaporator unit in a counterflow at a temperature at or below the boiling temperature of the water; evaporating pure water from the raw water into the moist air and cooling the raw water; conducting the cooled raw water into a heat exchanger thereby cooling the fluid stream of the electrolysis unit; conducting the moist air and the pure water into a water extraction unit; separating a second molar amount of the pure water off from the moist air in the water extraction unit, wherein a third molar amount of water remaining in the air is less than the first; conducting the preheated raw water back to the evaporator; and conducting the cooled fluid back into the electrolysis unit. 1. A method for cooling a fluid stream of an electrolysis unit and extracting water from the ambient air , the method comprising:conducting moist air having a first molar amount of water into an evaporator unit;conducting raw water into the evaporator unit in a counterflow to a flow of the moist air at a temperature at or below the boiling temperature of the water;evaporating pure water from the raw water into the moist air and thereby cooling the raw water;conducting the cooled raw water into a heat exchanger;conducting the fluid stream of the electrolysis unit into the heat exchanger, wherein heat is transferred from the fluid stream to the raw water;conducting the moist air and the pure water into a water extraction unit;separating a second molar amount of the pure water off from the moist air with water in the water extraction unit, wherein a third molar amount of water remaining in the air after the separation of the second molar amount is less than the first molar amount;conducting the preheated raw water back into the evaporator unit; andconducting the cooled fluid stream back into the electrolysis unit.2 ...

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17-11-2022 дата публикации

STEAM GENERATION APPARATUS

Номер: US20220364721A1
Принадлежит:

Steam generation apparatus and method in which liquid is regulated in thermal catalytic reaction below a specific temperature and accelerated in thermal catalytic reaction above that temperature, including a vaporizer housing, axial ends of the housing being opened, and collars formed at axial ends of a cylindrical part of the housing; upper and lower flanges joined to housing collars; a vaporizer with a spiral channel in between; an exothermic member disposed such that the vaporizer inside is heated to a predetermined temperature; an injection nozzle at a center of the upper flange with an intake for liquid to be treated; a steam socket attached to the lower flange for guiding steam to the spiral channel, the steam socket including an inlet port connected to an inside of the vaporizer, outlet port connected to the spiral channel, and a steam channel connecting the inlet port and the outlet port.

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29-12-2022 дата публикации

WATER DISTILLATION SYSTEM

Номер: US20220411289A1
Принадлежит: GTI ENERGY

A method and apparatus for recovering distilled water from wastewater. The method and apparatus evaporates water vapor from a wastewater stream into a moving airflow, collects collecting distilled water from the water vapor, and powers the moving airflow and the collecting distilled water with a thermoelectric generator. The apparatus includes a self-regenerative distillation unit, with an evaporating channel, a condensing channel, and a distilled water outlet. The thermoelectric generator includes a hot shoe side in combination with the wastewater stream, and a cold shoe side in combination with the distilled water outlet. The thermoelectric generator powers a fan or blower connected to the evaporating channel and/or a water pump connected to the distilled water outlet. 1. A method for recovering distilled water from wastewater , the method comprising the steps of:evaporating water vapor from a wastewater stream into a moving airflow;collecting distilled water from the water vapor; andpowering the moving airflow and the collecting distilled water with a thermoelectric generator.2. The method of claim 1 , wherein the thermoelectric generator powers a fan or blower for the moving airflow and a pump for the collecting distilled water.3. The method of claim 1 , wherein the evaporating and the collecting are performed by a self-regenerative distillation unit including an evaporating channel and a condensing channel.4. The method of claim 3 , further comprising reducing a temperature of the moving airflow upstream of the evaporating channel.5. The method of claim 3 , further comprising reducing a pressure of the airflow in the evaporating channel.6. The method of claim 5 , further comprising increasing a pressure of the airflow in a condensing channel downstream of the evaporating channel.7. The method of claim 5 , further comprising maintaining a sub-atmospheric pressure of the airflow in the evaporating channel to reduce a dew point of the airflow.8. The method of ...

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17-10-2007 дата публикации

식수를 제조하기 위한 방법 및 장치

Номер: KR20070101849A
Принадлежит: 문터스 코포레이션

비-식수로부터 식수를 제조하는 방법 및 장치에 있어서, 공기의 공급물을 가열 유닛을 통해 통과시켜 그 온도를 증가시키고, 이후 비-식수가 가열된 공기와 액체 가스 접촉으로 통과하는 증발성 냉각 매체를 통해 통과시키는 방법 및 장치. 증발성 매체를 떠나는 공기의 온도는 물과의 접촉의 결과로서 감소되고, 그 수분함량은 증가된다. 더욱 차가운 축축한 공기를 이후 냉각 코일을 통해 통과시켜 공기 중의 수분이 액체수로서 응축되도록 유발시키고, 이 액체수를 집수하고, 음용수로서의 사용에 적합하도록 만든다. 식수

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12-02-2020 дата публикации

VOC refining equipment

Номер: JP6643637B2
Автор: 大助 田端, 晃 磯見

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03-10-2017 дата публикации

脱硫废水喷雾干燥的方法

Номер: CN107226573A

本发明涉及锅炉领域,公开了脱硫废水喷雾干燥的方法,包括:先将脱硫废水与树脂组合物进行第一接触,然后将接触后所得溶液与碱性物质进行第二接触,接着将第二接触后所得混合物与压缩空气一起通过喷嘴引入至锅炉的烟道中,其中,所述树脂组合物为体积比为(2~20):1的钠型阳离子交换树脂和氢型阳离子交换树脂。本发明的方法可直接将脱硫系统浓缩液或多效蒸发、MVR非饱和溶液进行喷雾干燥,并充分利用烟道内高温进行盐与水的物化分离,以及能够避免脱硫废水在喷嘴内短周期内大量结垢。

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22-03-2022 дата публикации

Water desalination method and device for implementation thereof

Номер: RU2767966C1

FIELD: chemistry. SUBSTANCE: invention can be used for desalination of sea water in mobile conditions - on ships or in stationary conditions - near coasts of seas, oceans, as well as on sea platforms. Air is saturated with water vapour inside dome-shaped housing 4 by bubbling sea water heated to temperature above 100 °C by atmospheric air, which is supplied under pressure through fine-meshed screen 1 with size of cells, providing air passage through it, but excluding air outlet through lower part of housing. Dome-shaped housing 4 is placed so that mesh 1 is under a layer of sea water. For this purpose, it is lowered on cable 5 and immersed below waterline 3. At the same time under the dome there is formed a space not filled with water for supply of air saturated with steam. Salt water desalination device also includes a condenser-cooler, a storage tank for collecting desalinated water, a hot air generator, a supply air duct 7, connected to a fan for injecting air into bubbling zone 2, as well as air duct 6 communicated with the fan for pumping out the moisture-saturated air from the dome space. EFFECT: invention makes it possible to simplify method and device due to exclusion of sea water pumping and its heating to boiling point, as well as significantly reduce energy consumption for the steam generation process and increase efficiency, since it depends only on the volume of hot air passed through. 2 cl, 1 dwg РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 767 966 C1 (51) МПК C02F 1/12 (2006.01) C02F 103/08 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (52) СПК C02F 1/12 (2021.08); C02F 2103/08 (2021.08) (21)(22) Заявка: 2021108722, 30.03.2021 (24) Дата начала отсчета срока действия патента: (73) Патентообладатель(и): Черников Андрей Михайлович (RU) Дата регистрации: 22.03.2022 (45) Опубликовано: 22.03.2022 Бюл. № 9 2 7 6 7 9 6 6 R U (54) СПОСОБ ОПРЕСНЕНИЯ ВОДЫ И УСТРОЙСТВО ДЛЯ ЕГО ОСУЩЕСТВЛЕНИЯ (57) Реферат: ...

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23-11-2016 дата публикации

一种用烟气余热处理脱硫废水的系统及方法

Номер: CN106145230A
Автор: 朱文瑜, 李筱璋, 郑伟, 髙燎

本发明公开了一种用烟气余热处理脱硫废水的系统及方法,包括浓缩塔和浓浆箱,所述浓缩塔中设置有喷淋层,浓浆箱同时与浓缩塔内部以及喷淋层连通,浓缩塔上开设有通入烟气的通孔,并且通孔设置在喷淋层上方,在浓缩塔外部设置有循环泵,循环泵同时与浓缩塔内部和喷淋层连通,且循环泵与浓缩塔内部的连通处位于喷淋层下方。该系统及方法利用锅炉烟气余热的热量蒸发从脱硫石膏旋流器出来的脱硫废水,达到以废治废及脱硫废水零排放的目的,蒸发过程温和,操作弹性高,需要的烟气量较小,不需要消耗其他热源,耗能少,占地小,易于实施,而且具有除投资省、运行费用低、不需添加任何化学药品等优势。

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15-04-2000 дата публикации

Management apparatus dirty water livestock raising

Номер: KR200179902Y1
Автор: 천상석
Принадлежит: 천상석

본 고안은 축산분뇨중의 오수를 처리하는 축산 오수 처리장치에 관한 것으로, 축산분뇨중의 오수를 안개처럼 대기중에 분무시켜 증발처리하도록 하는 것이다. The present invention relates to a livestock sewage treatment apparatus for treating sewage in livestock manure, and to evaporate the sewage in livestock manure by spraying it into the atmosphere as a fog. 이러한 본 고안은 분무통 중앙에 입설되고 모터의 회전동력을 받아 회전하는 회전축에 다단으로 설치된 회전판과, 상기 회전판의 상부에 펌핑된 오수를 분사 시키는 분사노즐과, 상기 회전판의 외측으로 이격되어 설치되고 다수의 분무홈과 분무돌기가 형성된 분무판과, 회전축 하부에 설치된 송풍팬과, 상기 분무통 하부에 설치되어 오수를 모으는 집수통과, 상기 분무통 측면에 설치되고 송풍구가 분무통 중앙 상부에 설치되는 송풍기를 구비시킴으로써 이루어 진다. The present invention has a rotary plate installed in the center of the spray tank and installed in multiple stages on the rotating shaft rotated by the rotational power of the motor, the spray nozzle for spraying the sewage pumped on the upper portion of the rotating plate, and is spaced apart from the outer side of the rotating plate A spray plate having a plurality of spray grooves and spray projections, a blower fan disposed below the rotating shaft, a collecting tank installed at the lower part of the spray bottle to collect sewage, and a side of the spray bottle installed at the upper side of the spray bottle. It is made by providing a blower.

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22-05-2019 дата публикации

Method of desalination of water and device for its implementation

Номер: RU2688764C1

FIELD: water and air purification technology.SUBSTANCE: invention relates to a method and a device for desalinating water. Method of desalination of salty water, in which desalinated salt water, supplied in form of jet or shroud, is periodically exposed to impact of strong shock wave and high-speed flow of hot gaseous detonation products, leading to fine aerodynamic fragmentation of jet or shroud of desalinated salt water. Formed two-phase torch is supplied tangentially to vortex zone, where in conditions of strongly swirled high-temperature flow there is fast evaporation of microdroplets of desalinated salt water with formation of finely dispersed crystalline sea salt, separated from gaseous detonation products and steam due to the field of centrifugal forces. Gaseous detonation products and water vapor are discharged from the vortex zone into the condensation zone of water vapor and its separation from gaseous detonation products. Salt residue is continuously removed from the vortex zone in the form of finely dispersed crystalline sea salt. Method is realized in a device in which systems for fragmentation and evaporation of desalinated salt water are made in form of pulse generator of strong shock wave and high-speed flow of hot gaseous detonation products, connected to vortex reactor for evaporation of microdroplets of desalinated salt water with formation of finely dispersed crystalline sea salt, connected to condenser water vapor. Water vapor condenser is equipped with system for removal of gaseous detonation products and system for discharge of desalinated water to consumer.EFFECT: invention provides desalination of salty water by means of thermomechanical action on jet or shroud of salt water with strong shock wave and high-speed flow of hot gaseous detonation products obtained in cyclic working process with pulse-detonation burning of one or another fuel.2 cl, 1 dwg, 1 ex РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 688 764 C1 (51) МПК C02F 1/12 (2006.01) ...

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09-12-2010 дата публикации

Apparatus and method for reclamation of treatable water

Номер: US20100307987A1
Принадлежит: H2O Cleaning Technology

The present invention relates to an apparatus and method to reclaim water. The water that may be reclaimed begins as untreated treatable water, which is water having solids, particulates, or minerals not originally in the water. Untreated treatable water is also natural water having solids, particulates, or minerals that are undesired. The invention provides for removal of the totally dissolved solids from the water by micronizing the water in a chamber having a first temperature, and condensing the water in a second chamber having an interior surface that is cooled to the ambient wet-bulb temperature of the surrounding environment. Reclaimed treatable water from this invention becomes usable water.

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15-11-2000 дата публикации

Management apparatus dirty water livestock raising

Номер: KR200203203Y1
Автор: 천상석
Принадлежит: 천상석

본 고안은 축산분뇨중의 오수를 처리하는 축산 오수 처리장치에 관한 것으로써, 오수를 안개처럼 미세한 입자로 대기중에 분무시켜 자연 증발처리하는 축산 오수 처리장치에 관한 것이다. The present invention relates to a livestock sewage treatment apparatus for treating sewage in livestock manure, and relates to a livestock sewage treatment apparatus for spraying sewage into the atmosphere with fine particles as fog to spontaneously evaporate. 본 고안은 수개의 지지프레임(9)에 의해 원통형의 분무통(1)이 지면위에 놓이고, 분무통(1)의 안쪽에서 모터(3)가 수직상으로 설치되며, 송풍팬(7)이 장착된 회전축(6)이 커플링(5)에 의해 모터축과 결합되고, 분무통(1)의 상측부에서 회전축(6)에 장착된 회전판(10)의 외주연으로 분무판(20)이 설치되고, 이 분무판(20)의 아래에 집수통(30)이 고정 부착되며, 회전판(10)위에 분사노즐(40)이 설치되어 구성된다. According to the present invention, a cylindrical spray bottle 1 is placed on the ground by several supporting frames 9, and a motor 3 is installed vertically inside the spray bottle 1, and a blower fan 7 is provided. The mounted rotating shaft 6 is coupled to the motor shaft by the coupling 5, and the spray plate 20 is formed by the outer circumference of the rotating plate 10 mounted on the rotating shaft 6 at the upper side of the spray bottle 1. The collection container 30 is fixedly attached to the bottom of the spray plate 20, and the injection nozzle 40 is installed on the rotating plate 10.

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