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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 2527. Отображено 199.
10-01-2014 дата публикации

СПОСОБ И УСТРОЙСТВО ДЛЯ ОЧИСТКИ ОБОГАЩЕННОГО ДИОКСИДОМ УГЛЕРОДА ТОПОЧНОГО ГАЗА

Номер: RU2012127761A
Принадлежит:

... 1. Способ очистки обогащенного диоксидом углерода топочного газа, содержащего диоксид серы, который образуется в бойлере, сжигающем топливо в присутствии газа, содержащего газообразный кислород, где способ включает:отделение, по меньшей мере, 80% содержания диоксида серы топочного газа, который образуется в бойлере, в первом устройстве газоочистки для получения частично очищенного обогащенного диоксидом углерода топочного газа,направление, по меньшей мере, части частично очищенного обогащенного диоксидом углерода топочного газа во второе устройство газоочистки, которое отделено от первого устройства газоочистки,охлаждение в указанном втором устройстве газоочистки частично очищенного обогащенного диоксидом углерода топочного газа для конденсации, содержащейся в нем воды, в результате чего образуется очищенный обогащенный диоксидом углерода топочный газ, имеющий меньшую концентрацию водяного пара, чем частично очищенный обогащенный диоксидом углерода топочный газ.2. Способ по п.1, в котором ...

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10-05-2011 дата публикации

СПОСОБ ДИСТИЛЛЯЦИИ ИСХОДНОГО МАТЕРИАЛА И УСТАНОВКА ДЛЯ ОСУЩЕСТВЛЕНИЯ ТАКОГО СПОСОБА

Номер: RU2009140746A
Принадлежит:

... 1. Способ дистилляции исходного материала (4), содержащего подлежащую дистилляции жидкость Fd, с использованием газонепроницаемой, прочной к избыточному давлению и/или разрежению системы (1) резервуаров, которая содержит испаритель (2) с исходным материалом (4), температуру которого можно регулировать, конденсатор (3) для конденсации превратившейся в пар темперируемой жидкости Fd в конденсат (5), а также соединяющее испаритель (2) и конденсатор (3) паровое пространство (6), причем паровое пространство (6) снабжено датчиком (7) давления для измерения устанавливающегося в нем давления pm смеси, датчиком (8) температуры для измерения устанавливающейся в нем температуры (Tm) смеси, а также регулятором (9) давления, отличающийся тем, что содержит следующие стадии способа: ! а) создание в испарителе (2) с исходным материалом (4) первой температуры (Т1), а в конденсаторе (3) второй, более низкой температуры (Т2); ! b) измерение давления pm смеси и температуры Tm смеси; ! с) определение по измеренной ...

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29-01-1976 дата публикации

Condensn of vapours by direct contact with liq - flowing in thin film over perforated plate

Номер: DE0002433641A1
Принадлежит:

In an appts. for condensn. of vapours by direct contact with a cold liq., e.g. water vapour and ater, the liq. flows as a thin film over an approx. horizontal perforated plate and the vapour is blown from the underside of the plate through the perforations of the liq. film. The appts. may be used in single stage for condensn. of steam from turbines and steam jet vacuum pumps, and in multistage as heat exchangers, esp. for vacuum cooling of process liqs. A high efficiency is achieved with a comparatively small column height; the equipment is simple to construct.

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30-03-1971 дата публикации

Apparatus of condensation multi-stage.

Номер: OA0000003596A
Автор:
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15-09-2007 дата публикации

GAS WASH PROCEDURE AND - DEVICE

Номер: AT0000369900T
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15-08-2008 дата публикации

PLANT FOR THE PRODUCTION OF ALCOHOL

Номер: AT0000401412T
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15-08-2017 дата публикации

APPARATUS FOR WATER RECUPERATION

Номер: AT0000518169B1
Принадлежит:

Die Erfindung betrifft ein Verfahren und eine Vorrichtung (100; 200; 300) zur Wasserrückgewinnung aus einem Abgasmassenstrom (112; 204; 304) der eine Abgaskammer (101) durchströmt und in ein Rohrsystem (124; 202; 302), durch ein molekulares Sieb Wassermoleküle abgibt. Aufgabe der vorliegenden Erfindung ist es, ein Verfahren und eine Vorrichtung (100; 200; 300) anzugeben, die es auf einfache Weise schaffen einen möglichst hohen Anteil des Wassers aus dem Abgasmassenstrom (112; 204; 304) zurück zu gewinnen. Gelöst wird das dadurch, dass der Abgasmassenstrom (112; 204; 304) zuerst am molekularen Sieb vorbeiströmt und Wassermoleküle in verdampftem Zustand erhält und der Dampfstrom der Wassermoleküle in einem Kondensator (70) kondensiert wird, und dass der Abgasmassenstrom (112; 204; 304) durch ein Ventil (122; 212; 312) am Ende der Abgaskammer (101) gesteuert wird.

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15-08-1989 дата публикации

VERFAHREN ZUR KONTINUIERLICHEN RUECKGEWINNUNG VON LOESUNGSMITTELN

Номер: ATA140388A
Автор:
Принадлежит:

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10-11-1972 дата публикации

Condenser plant with several, condensation chambers elevatorshifted

Номер: AT0000302914B
Автор:
Принадлежит:

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12-06-2014 дата публикации

Bubble-column vapor mixture condenser

Номер: AU2012312643B2
Принадлежит:

In a bubble-column vapor mixture condenser, a fluid source supplies a carrier-gas stream including a condensable fluid in vapor phase. The condensable fluid in liquid form is contained as a bath in a chamber in each stage of the condenser, and the carrier gas is bubbled through the bath to condense the fluid into the bath. Energy from condensation is recovered to a coolant in a conduit that passes through the liquid in the stages of the condenser. The bubble-column vapor mixture condenser can be used, e.g., in a humidification-dehumidification system for purifying a liquid, such as water.

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06-08-2020 дата публикации

ODH complex with on-line mixer unit and feed line cleaning

Номер: AU2019208519A1
Принадлежит: Griffith Hack

Oxidative dehydrogenation is an alternative to the energy extensive steam cracking process presently used for the production of olefins from paraffins. Various embodiments of an oxidative dehydrogenation chemical complex designed to allow removal of sulfur containing contaminants that collect in the gas mixer unit and in the feed lines leading to the ODH reactor are disclosed herein.

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06-05-2004 дата публикации

APPARATUS FOR THE PRODUCTION OF ALCOHOL

Номер: CA0002503067A1
Принадлежит:

The aim of the invention is to produce alcohol from plant-based raw materials while reducing energy consumption. Said aim is achieved by separating the husk portion of cereals during grinding and feed said husk portion to a dryer (21) which dries distiller's wash as a carrier medium for distiller's wash. The lost heat of said dryer (21) is supplied to the distillation station (15) as process heat. The lost heat of a molecular sieve (45) that drains the raw alcohol is also redirected to the distillation station (15) as process heat.

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13-02-2018 дата публикации

BUBBLE-COLUMN VAPOR MIXTURE CONDENSER

Номер: CA0002848412C

In a bubble-column vapor mixture condenser, a fluid source supplies a carrier-gas stream including a condensable fluid in vapor phase. The condensable fluid in liquid form is contained as a bath in a chamber in each stage of the condenser, and the carrier gas is bubbled through the bath to condense the fluid into the bath. Energy from condensation is recovered to a coolant in a conduit that passes through the liquid in the stages of the condenser. The bubble-column vapor mixture condenser can be used, e.g., in a humidification-dehumidification system for purifying a liquid, such as water.

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15-10-2009 дата публикации

Device to the synthesis of urea and kit for re-tooling existing such device.

Номер: CH0000698707B1
Автор: YASUHIKO KOJIMA

Es ist das Ziel, eine Vorrichtung zur Synthese von Harnstoff und ein Kit zum Nachrüsten einer bestehenden solchen Vorrichtung zu ermöglichen, um einen schweren Kondensator an einer relativ niedrigen Position anzuordnen und die Probleme, die mit der Strömungsführung eines Prozessfluids innerhalb eines Rohrs in dem Kondensator verbunden sind, zu umgehen. Die vorliegende Erfindung schafft eine Vorrichtung zur Synthese von Harnstoff, welche umfasst: einen Synthesereaktor (A) zum Umsetzen von NH3 mit CO2 um eine Harnstoff, nicht umgesetztes NH3 und CO2 sowie Wasser enthaltende Harnstoffsyntheselösung zu erhalten; einen Stripper (C) zum Austreiben der Harnstoffsyntheselösung unter Verwendung von zumindest einem Teil des Ausgangsmaterials CO2, um ein Gas, welches das nicht umgesetzte NH3 und CO2 enthält, abzutrennen; einen vertikalen Tauchkondensator (B) mit einem Mantel-Rohrbündel-Aufbau zum Kondensieren des Gases in einem Absorptionsmedium auf der Mantelseite, während das Gas mit einem Kühlmedium ...

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30-06-2009 дата публикации

Device to the synthesis of urea.

Номер: CH0000698261B1
Автор: YASUHIKO KOJIMA ON

Es ist das Ziel, in einer Vorrichtung zur Synthese von Harnstoff durch Umgehung des abwärtsgerichteten Stroms einer Harnstoffsyntheselösung, welche ein zweiphasiger Gas-Flüssigkeits-Strom ist, und durch Stabilisierung des Stroms der Harnstoffsyntheselösung, welche noch immer der zweiphasige Gas-Flüssigkeits-Strom bleibt, einen gleichmässigeren Betrieb zu ermöglichen und den Energieverlust durch einen geringeren Strömungswiderstand zu verringern. Die vorliegende Erfindung schafft eine Vorrichtung zur Synthese von Harnstoff, welche umfasst: einen Synthesereaktor (A) zum Umsetzen von NH3 mit CO2, um eine Harnstoff, nicht umgesetztes NH3, nicht umgesetztes CO2 und Wasser enthaltende Harnstoffsyntheselösung zu erhalten; einen Stripper (C) zum Austreiben der Harnstoffsyntheselösung unter Verwendung von zumindest einem Teil des Ausgangsmaterials CO2, um ein Gasgemisch, welches das nicht umgesetzte NH3 und das nicht umgesetzte CO2 enthält, abzutrennen; einen vertikalen Tauchkondensator (B) mit ...

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29-03-2018 дата публикации

Disposal vehicle for receiving waste water and method for disposal.

Номер: CH0000709546B1
Принадлежит: KAISER AG

Die Erfindung betrifft ein Entsorgungsfahrzeug und ein Verfahren zur Aufnahme von Schmutzwasser (22) aus einem Sammelbehälter (2), Eindickung des Schmutzwassers (22) unter Absonderung von sauberem Wasser (23) und Rückgabe des sauberen Wassers (23) in die Umwelt. Das Entsorgungsfahrzeug umfasst einen Schmutzwassertank (4), einen Wassertank (5) sowie eine Anlage zur Verdickung des Schmutzwassers, wobei die Anlage eine Destillationsanlage (8) ist, welche im Arbeitsbereich zwischen 70 und 105 °C sauberes Wasser (23) aus dem Schmutzwasser (22) destilliert. Zum Leeren des Sammelbehälters (2) wird das Schmutzwasser (22) mittels einer Vakuumpumpe (18) aus dem Sammelbehälter (2) in den Schmutzwassertank (4) gepumpt und weiter in die Anlage (8) zur Destillierung geleitet. Die Anlage (8) scheidet sauberes Wasser (23) aus, das in den Wassertank (5) und schliesslich zurück in die Umwelt abgegeben wird. Eingedicktes Schmutzwasser (22) wird aus der Anlage zurück in den Schmutzwassertank (4) geleitet.

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30-10-2015 дата публикации

Disposal vehicle for receiving of dirty water and a method of disposal.

Номер: CH0000709546A1
Автор: HÄUSLE VIKTOR
Принадлежит:

Die Erfindung betrifft ein Entsorgungsfahrzeug und ein Verfahren zur Aufnahme von Schmutzwasser (22) aus einem Sammelbehälter (2), Eindickung des Schmutzwassers (22) unter Absonderung von sauberem Wasser (23) und Rückgabe des sauberen Wassers (23) in die Umwelt. Das Entsorgungsfahrzeug umfasst einen Schmutzwassertank (4), einen Wassertank (5) sowie eine Anlage zur Verdickung des Schmutzwassers, wobei die Anlage eine Destillationsanlage (8) ist, welche im Arbeitsbereich zwischen 70 und 105 °C sauberes Wasser (23) aus dem Schmutzwasser (22) destilliert. Zum Leeren des Sammelbehälters (2) wird das Schmutzwasser (22) mittels einer Vakuumpumpe (18) aus dem Sammelbehälter (2) in den Schmutzwassertank (4) gepumpt und weiter in die Anlage (8) zur Destillierung geleitet. Die Anlage (8) scheidet sauberes Wasser (23) aus, das in den Wassertank (5) und schliesslich zurück in die Umwelt abgegeben wird. Eingedicktes Schmutzwasser (22) wird aus der Anlage zurück in den Schmutzwassertank (4) geleitet.

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31-12-1996 дата публикации

Process and apparatus for the purification of a gaseous stream containing acrolein

Номер: EA0199600035A2
Принадлежит:

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31-12-1996 дата публикации

Process and apparatus for the purification of a gaseous stream containing acrolein

Номер: EA0000960035A2
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30-07-2012 дата публикации

ОХЛАЖДЕНИЕ НИЗКОЭНЕРГЕТИЧЕСКОГО ОТХОДЯЩЕГО ГАЗА С ИСПОЛЬЗОВАНИЕМ СМЕШИВАЮЩЕГО КОНДЕНСАТОРА

Номер: EA201270240A1
Принадлежит:

Тепло отводят из технологической жидкости смешивающего конденсатора путем охлаждения отходящего газа с использованием двух раздельных и отличающихся охлаждающих устройств, которые подают охлажденную технологическую жидкость по меньшей мере в две раздельные секции в смешивающем конденсаторе. Наиболее предпочтительно, что секции жидкостно изолированы и подают нагретые технологические жидкости на соответствующие охлаждающие устройства. Однако в других вариантах осуществления секции жидкостно соединены друг с другом, так чтобы обеспечить передачу технологической жидкости из одной секции в другую секцию. В одном из двух охлаждающих устройств использован хладагент, менее дорогой или более доступный по сравнению со вторым хладагентом. В целом предпочтительно, чтобы одно из охлаждающих устройств представляло собой воздушный охладитель и чтобы в другом охлаждающем устройстве была применена охлаждающая среда, отличная от воздуха.

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18-01-1954 дата публикации

Process and apparatus of condensation of gases

Номер: FR0001051538A
Автор:
Принадлежит:

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26-07-1996 дата публикации

Method and device for removing by selective adsorption a volatile hydrocarbon compound from a gaseous mixture, and applications.

Номер: FR0002719500B1
Автор:
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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10-11-1995 дата публикации

Process and device to extract by selective adsorption a volatile hydrocarbon compound from gas unmélange, and applications

Номер: FR0002719500A1
Принадлежит:

L'invention concerne l'extraction d'un composé hydrocarboné volatil d'un mélange gazeux en vue de réduire la concentration de ce composé. On utilise l'énergie de condensation du composé hydrocarboné et / ou l'énergie produite par un déplacement (2) de ce composé depuis un adsorbant (6) jusqu'à un condenseur (3) pour fournir la chaleur nécessaire à la désorption du composé hydrocarboné. La figure 1 est un schéma de principe de mise en oeuvre de l'invention. L'invention s'applique notamment à la purification d'un gaz contenant des vapeurs d'hydrocarbures.

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23-06-1960 дата публикации

Process and device to separate, of crude gases, the condensable components

Номер: FR0001224442A
Автор:
Принадлежит:

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09-11-2006 дата публикации

APPARATUS FOR UREA SYNTHESIS AND METHOD OF IMPROVING THE SAME

Номер: WO2006118071A1
Автор: KOJIMA, Yasuhiko
Принадлежит:

In an apparatus for synthesizing urea and a method of improving the same, it becomes possible to provide a heavy condenser at a relatively low position and, further, it becomes possible to overcome the problems caused by passing a process fluid from the condenser in a tube. Namely, an apparatus for synthesizing urea which comprises: a synthesis tube wherein NH3 is reacted with CO2 to give a synthesis solution containing urea, the unreacted NH3, the unreacted CO2 and water; a stripper whereby the synthesis solution is stripped by using at least a portion of the starting CO2 to thereby separate a gas containing the unreacted NH3 and CO2; a vertical submerge condenser which has a shell-and-tube structure and by which the above-described gas is condensed into an absorption medium in the shell side under cooling with a cooling medium passing through the tube side; and a circulation means for circulating the liquid obtained from the condenser into the synthesis tube; wherein the condenser is ...

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01-11-1990 дата публикации

A PROCESS AND DEVICE FOR VAPOUR CONDENSATION AND HEAT CONVERSION

Номер: WO1990012631A1
Автор: CURTIUS, Fritz
Принадлежит:

A washing condenser as a backflow reactor for heat and material exchange is filled with two substances which have the ideal mixing ratio but different boiling points. One is fed in as a vapour (10) and condensed in backflow with the condensate (11) of the other as a washing fluid. The heat of condensation may be drawn off with the vapours (6) of the washing fluid at its boiling point.

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14-06-2019 дата публикации

ПРОМЫВКА ВЫХОДЯЩЕГО ИЗ РЕАКТОРА ПОТОКА ДЛЯ УДАЛЕНИЯ АРОМАТИЧЕСКИХ СОЕДИНЕНИЙ

Номер: RU2691453C1
Принадлежит: ЮОП ЛЛК (US)

Изобретение относится к способу удаления ароматических соединений из технологического потока, включающему направление технологического потока, содержащего парафины, олефины и ароматические соединения, в первый контактный охладитель, использующий первый охлаждающий агент, для образования первого потока; направление первого потока в компрессор для образования второго потока; и направление второго потока во второй контактный охладитель, использующий второй охлаждающий агент, для образования третьего потока, содержащего олефины и парафины, причем содержание ароматических соединений во втором охлаждающем агенте меньше, чем содержание ароматических соединений в первом охлаждающем агенте. Поток углеводородов образуется с помощью процесса дегидрирования, который приводит к образованию ароматических соединений. Способ включает систему из двух контактных охладителей, причем первый и второй контактные охладители используют различные охлаждающие агенты. Второй охлаждающий агент является неароматическим ...

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06-12-2019 дата публикации

Номер: RU2018106541A3
Автор:
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14-12-1989 дата публикации

Process for continuous solvent recovery

Номер: DE0003917389A1
Принадлежит:

A process is proposed for continuous recovery of solvents, such as hydrocarbons or halogenated hydrocarbons, from a process gas stream in which the solvents are adsorbed to solids from the process gas stream in a first stage, desorbed in a second stage by means of a preferably hot regeneration gas and, in a third stage, are condensed from the laden regeneration gas, if necessary after drying, and separated off. This is achieved by using liquid droplets, in particular solvent droplets distributed in the laden regeneration gas at least essentially as a heat removal medium for condensation of the solvent treatment. In addition, an apparatus for carrying out this process is proposed having an adsorber which is advantageously designed as a segmented drum adsorber, the segments of which are designed for radial or axial flow, a regeneration gas circuit, if appropriate an adsorption drier for drying the laden regeneration gas and a solvent condenser, the solvent condenser being equipped with a ...

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07-01-2009 дата публикации

Desalination method

Номер: GB0000821884D0
Автор:
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12-03-1990 дата публикации

VERFAHREN ZUR KONTINUIERLICHEN RUECKGEWINNUNG VON LOESUNGSMITTELN

Номер: AT0000390016B
Автор:
Принадлежит:

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11-09-1989 дата публикации

PROCEDURE AND DEVICE FOR RUECKGEWINNUNG OF LOESUNGSMITTELN FROM GASES

Номер: AT0000388881B
Принадлежит:

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15-08-2017 дата публикации

APPARATUS FOR WATER RECUPERATION

Номер: AT0000518169A4
Принадлежит:

Die Erfindung betrifft eine Vorrichtung (100; 200; 300) zur Wasserrückgewinnung aus einem Abgasmassenstrom (112; 204; 304) mit einer Abgaskammer (101), die eine stromaufwärts angeordnete Abgasöffnung (110), einen stromabwärts angeordneten Abgasauslass (118; 220; 320) und ein Rohrsystem (124; 202; 302) aufweist, wobei das Rohrsystem (124; 202; 302) die Abgaskammer (101) in ein unbehandeltes Volumen (116) und ein behandeltes Volumen (114) teilt, das Rohrsystem (124, 202; 302) mit einem Kondensator (70) strömungsverbunden ist und das unbehandelte Volumen (116) mit der Abgasöffnung (110) strömungsverbunden ist und das behandelte Volumen (114) stromabwärts des Rohrsystems (124; 202; 302) angeordnet ist und die Vorrichtung (100; 200; 300) ein Ventil (122; 212; 312) aufweist. Aufgabe der vorliegenden Erfindung ist es, eine Vorrichtung (100; 200; 300) anzugeben, die es auf einfache Weise schafft einen möglichst hohen Anteil des Wassers aus dem Abgasmassenstrom (112; 204; 304) zurück zu gewinnen ...

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26-11-1997 дата публикации

Method and device for producing water by condensing atmospheric moisture

Номер: AU0002628597A
Принадлежит:

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31-07-1973 дата публикации

GASOLINE VAPOR RECOVERY

Номер: CA931066A
Автор:
Принадлежит:

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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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31-03-1997 дата публикации

СПОСОБ И УСТАНОВКА ОЧИСТКИ ГАЗОВОГО ПОТОКА, СОДЕРЖАЩЕГО АКРОЛЕИН

Номер: EA0199600035A3
Принадлежит:

Изобретение относится к способу и устройству очистки газового потока, содержащего акролеин. Сущность изобретения заключается в том, что на первом этапе питающий газовый поток, содержащий акролеин, воду, кислоты и инертные газы, получаемый, в частности, при окислении пропилена в акролеин в газовой фазе, разделяют на газовый эфлюент и жидкий поток в охладительной колонне, в которой обеспечивают температуру жидкого потока в основании колонны более низкой или равной точке росы газового потока, при поддержании температурного перепада, не превышающего 20°С, и на втором этапе газовый эфлюент конденсируют при температуре ниже 20°С с получением жидкой фракции и очищенной газовой фракции. Установка для осуществления способа включает в себя охлаждающую колонну и блок конденсации, подключенный к ее верхней части.

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12-04-1940 дата публикации

Process and installation for the fractionation of mixtures of hydrocarbons or others liquid

Номер: FR0000050378E
Автор:
Принадлежит:

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13-10-1938 дата публикации

Process and device of condensation in particular in the recovery of the vapors by the solid adsorbents

Номер: FR0000833196A
Автор:
Принадлежит:

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22-03-2011 дата публикации

GASOLINE VAPOR RECOVERY APPARATUS

Номер: KR1020110029144A
Автор:
Принадлежит:

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26-04-2016 дата публикации

Humidification-dehumidification system with a bubble-column vapor mixture condenser and intermediate gas extraction

Номер: US0009320984B2

A humidification-dehumidification system comprises a source of liquid; a humidifier including carrier-gas and liquid inlets and outlets and a chamber in which the liquid can contact a carrier gas containing a condensable fluid in vapor phase that is introduced from the carrier-gas inlet in a counterflow arrangement and in which a portion of the liquid can vaporize into the carrier gas; a bubble-column vapor mixture condenser including at least first and second stages, each stage including a carrier-gas inlet and outlet and a chamber configured to contain a liquid bath in fluid communication with the carrier-gas inlet and the carrier-gas outlet; a conduit passing from the source of the liquid through the chamber of each stage of the bubble-column condenser; and an intermediate exchange conduit coupled with (a) the bubble-column vapor mixture condenser and (b) the humidifier chamber at intermediate stages of each for transfer of the carrier gas therebetween.

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18-10-2018 дата публикации

Method for Preventing Fouling of a Demister

Номер: US20180299194A1
Принадлежит:

A method for preventing fouling of a demister is disclosed. A process fluid is provided into a vessel. A gas is provided to a gas inlet of the vessel. The gas comprises a component that desublimates, crystallizes, solidifies, reacts, or a combination thereof, in the process fluid, forming a first solid. The gas is passed through the process fluid, the component of the gas forming the first solid, resulting in a component-depleted gas. The component-depleted gas is passed out of the process fluid, causing splashing or spurting of the process fluid and the first solid. The diverter section is provided between the demister and the gas inlet, the diverter section comprising a physical obstruction preventing the process fluid and the first solid from splashing or spurting onto the demister. In this manner, fouling of the demister is prevented.

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10-09-2014 дата публикации

A method and a device for cleaning a carbon dioxide rich flue gas

Номер: EP2335804B1
Принадлежит: Alstom Technology Ltd

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07-01-1965 дата публикации

Vorrichtung zur Verteilung von Fluessigkeiten fuer den Direktaustausch in Gasen

Номер: DE0001184736B
Автор: SCHOLZ ERICH

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15-02-1989 дата публикации

PROCEDURE AND DEVICE FOR THE RECUPERATION OF LOESUNGSMITTELN FROM GASES

Номер: AT0000140288A
Автор: JIRENEC KARL ING.
Принадлежит:

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15-08-1989 дата публикации

PROCEDURE FOR THE CONTINUOUS RECUPERATION OF LOESUNGSMITTELN

Номер: AT0000140388A
Автор:
Принадлежит:

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15-01-2020 дата публикации

Verfahren und Vorrichtung zur Gewinnung von Wasser aus Luft

Номер: AT0000521380A4
Принадлежит:

Die Erfindung betrifft ein Verfahren zur Gewinnung von Wasser aus Luft (2, 2‘) mit folgenden nacheinander und parallel zueinander ablaufenden Schritten: a) Gaswäsche der Luft (2, 2‘) in einem Gaswäscher (1) mit einer gekühlten wässrigen Kaliumcarbonatlösung, welche derart gekühlt ist, dass die Luft (2, 2‘) im Gaswäscher (1) unter ihren Taupunkt abgekühlt wird, b) Ableiten der Kaliumcarbonatlösung aus dem Gaswäscher (1), c) Erwärmen der abgeleiteten Kaliumcarbonatlösung über zumindest eine Wärmpumpe (3a, 3b), d) Verdampfen von Wasser aus der erwärmten Kaliumcarbonatlösung und Kondensieren des gebildeten Wasserdampfes sowie Sammeln des Wassers, e) Kühlen von zumindest einem Teilstrom (TS1) der nach Schritt d) zurückbleibenden Kaliumcarbonatlösung über die zumindest eine Wärmpumpe (3a, 3b) gemäß Schritt c), − wobei die in Schritt e) erhaltene, gekühlte Kaliumcarbonatlösung in Schritt a) verwendet wird.

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02-11-2010 дата публикации

APPARATUS FOR THE PRODUCTION OF ALCOHOL

Номер: CA0002503067C
Принадлежит: GEA WIEGAND GMBH

The aim of the invention is to produce alcohol from plant-based raw materials while reducing energy consumption. Said aim is achieved by separating the husk portion of cereals during grinding and feed said husk portion to a dryer (21) which dries distiller's wash as a carrier medium for distiller's wash. The lost heat of said dryer (21) is supplied to the distillation station (15) as process heat. The lost heat of a molecular sieve (45) that drains the raw alcohol is also redirected to the distillation station (15) as process heat.

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31-07-1973 дата публикации

GASOLINE VAPOR RECOVERY

Номер: CA0000931066A1
Автор: KEVORKIAN V, SCHONEWALD R
Принадлежит:

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15-09-2020 дата публикации

METHOD FOR CONTROLLING THE WATER CONTENT IN PYROLYSIS LIQUIDS

Номер: CA0002873347C
Принадлежит: BTG BIOLIQUIDS B V, BTG BIOLIQUIDS B.V.

The present invention relates to a method for controlling the water content in a pyrolysis liquid comprising: a) producing a pyrolysis vapour comprising condensable compounds and non-condensable gases at a temperature equal to, or below 70° C and at a pressure equal to or below 1.5 bar; b) introducing the vapour phase in a condenser, condensing the condensable compounds of the pyrolysis vapour to obtain a condensate at a temperature equal to, or below, 70° C and at a pressure equal to or below 1.5 bar, and separating the non-condensable gases from the condensate; c) introducing at least part of the condensate into concentrator and concentrating said condensate by removing a certain amount of water at a temperature equal 1 to, or below 80° C thereby obtaining a concentrate; d)introducing the concentrate obtained after step c) into condenser and mixing it with the condensate present in condenser thereby obtaining a pyrolysis liquid with controlled water content.

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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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20-03-2013 дата публикации

Method for distilling raw materials and installation for carrying out said method

Номер: CN101663075B
Принадлежит:

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14-03-1972 дата публикации

GASOLINE VAPOR RECOVERY

Номер: US0003648436A1
Автор:
Принадлежит: INGERSOLL-RAND COMPANY

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05-06-2007 дата публикации

Diffusion driven water purification apparatus and process

Номер: US0007225620B2

An apparatus for purifying water, such as for desalinization, includes a source of a heated air stream, the heated air stream having a temperature above an ambient temperature. A diffusion tower having high surface area material therein receives a water stream including at least one impurity and creates at least one region having thin films of water therein from the water stream. The heated air stream is directed over the thin films of water to create a humidified air stream that is at least substantially saturated. At least one direct contact condenser is in fluid communication with the humidified air stream for condensing the humidified air stream, thus producing purified water. A power plant can include the apparatus for purifying water, where energy to heat the air stream is provided by low pressure condensing steam.

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29-08-1967 дата публикации

Номер: US0003338029A1
Автор:
Принадлежит:

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27-05-2009 дата публикации

УСТРОЙСТВО ДЛЯ ПРОИЗВОДСТВА ЛЕГКОПОЛИМЕРИЗУЕМОГО СОЕДИНЕНИЯ И УСТАНОВКА ДЛЯ ПОЛУЧЕНИЯ ЛЕГКОПОЛИМЕРИЗУЕМОГО СОЕДИНЕНИЯ

Номер: RU2356875C2

Изобретение может быть использовано в ректификационных и испарительных колоннах. Конденсатор 20 включает: трубчатую панель 33, разделяющую камеру 31, в которую сверху подается газ, содержащий акриловую кислоту, и камеру 32, в которую подается охлаждающая среда. Охлаждающие трубы 34 проходят через камеру 32 вертикально. Первая труба для подачи ингибитора полимеризации 28 входит в камеру 31 снаружи от конденсатора 20, а разбрызгиватель 35 соединен с концом первой трубы для подачи ингибитора полимеризации 28. Первая труба для подачи ингибитора полимеризации 28 поддерживается держателем 36 снаружи конденсатора 20. Изобретение позволяет проводить стабильный непрерывный процесс в конденсаторе в течение длительного времени за счет предотвращения полимеризации легко полимеризуемого соединения в конденсаторе с простой конструкцией, в который поступают пары легко полимеризуемого соединения. 3 н. и 4 з.п. ф-лы, 6 ил.

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27-06-2008 дата публикации

УСТРОЙСТВО ДЛЯ ПРОИЗВОДСТВА ЛЕГКО ПОЛИМЕРИЗУЕМОГОСОЕДИНЕНИЯ И УСТАНОВКА ДЛЯ ПОЛУЧЕНИЯ ЛЕГКО ПОЛИМЕРИЗУЕМОГО СОЕДИНЕНИЯ

Номер: RU2006144831A
Принадлежит:

... 1. Устройство для производства легко полимеризуемого соединения, в которое подаются пары легко полимеризуемого соединения, содержащее область конденсации, в которой легко полимеризуемое соединение конденсируется внутри устройства, распределитель для области конденсации для распределения ингибитора полимеризации по области конденсации, трубу для подачи ингибитора полимеризации для подачи ингибитора полимеризации в распределитель в области конденсации, и поддерживающее средство для поддерживания распределителя в области конденсации в заранее заданном положении внутри устройства, причем поддерживающим средством является средство для поддерживания трубы для подачи ингибитора полимеризации снаружи устройства. 2. Устройство для производства легко полимеризуемого соединения, в которое подаются пары легко полимеризуемого соединения, содержащее область конденсации, в которой легко полимеризуемое соединение конденсируется внутри устройства, распределитель для области конденсации для распределения ...

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10-03-2015 дата публикации

УВЛАЖНИТЕЛЬНО-ОСУШИТЕЛЬНАЯ СИСТЕМА, СОДЕРЖАЩАЯ ПАРОВОЙ КОНДЕНСАТОР СМЕШИВАНИЯ С ПУЗЫРЬКОВОЙ КОЛОННОЙ

Номер: RU2543873C1

Изобретение предназначено для обработки воды. Увлажнительно-осушительная система содержит источник жидкости, содержащий испаряемый компонент; увлажнитель, содержащий отверстия для газа-носителя и жидкости; камеру, в которой жидкость, вводимая из входного отверстия для жидкости, контактирует с газом-носителем, содержащим конденсируемую текучую среду в паровой фазе, вводимым из входного отверстия для газа-носителя в направлении противотока, и в которой часть жидкости испаряется в газ-носитель; паровой конденсатор смешивания с пузырьковой колонной, содержащий по меньшей мере первую ступень и вторую ступень. Входное отверстие для газа-носителя первой ступени находится в гидравлическом соединении с выходным отверстием для газа-носителя увлажнителя. Выходное отверстие для газа-носителя первой ступени находится в гидравлическом соединении с входным отверстием для газа-носителя второй ступени. Выходное отверстие для газа-носителя второй ступени находится в гидравлическом соединении с входным отверстием ...

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27-09-2007 дата публикации

Gaswaschverfahren und -vorrichtung

Номер: DE602004008275D1

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28-10-1953 дата публикации

Improvements in or relating to cooling, condensing or absorption apparatus for liquids, gases or vapours having a strong corrosive or etching action

Номер: GB0000698966A
Автор:
Принадлежит:

... 698,966. Plate heat-exchangers ; surface condensers ; film heat-exchangers for cooling liquid. CHLOBERAG CHLOR BETRIEB RHEINFELDEN AKT.-GES. May 4, 1951 [Dec. 23, 1948], No. 10563/51. Class 64 (iii) [Also in Group XII] In an arrangement in which liquids, gases or vapours having a corrosive or etching action, e.g. hydrogen chloride or chlorinated organic solvents, are cooled or condensed or such a gas is absorbed (see Group XII), hollow elements of graphite (or pressed thermosetting or thermoplastic synthetic material containing graphite) are assembled to form a column. Lenticular hollow elements 11 are interconnected by nipples 12, also of graphite &c., each axially bored but closed at one end adjacent lateral outlets 13 through which fluid flows from the bore radially into the next element. As shown in Fig. 1 liquid or gas to be cooled flows upwards through the column which is located in a vessel 14 containing cooling liquid such as water. A medium to be cooled, such as a liquid, may flow ...

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24-02-1954 дата публикации

Improvements in or relating to condensing gases by direct contact with immiscible cooling liquids

Номер: GB0000704580A
Автор:
Принадлежит:

... In order to effect substantially total condensation of vapours which contain both readily condensable fractions and less readily condensable fractions, the vapours are introduced into the base of a direct contact condenser which is supplied at the top with a cooling liquid that is immiscible with the vapours; both the cooling liquid and the condensate of the readily condensable fractions of the vapours are withdrawn from the base of the condenser, the condensate of the readily condensable fractions is introduced into the top of the condenser wherein it acts as a condensing and absorbing liquid for the less readily condensable fraction, and the total condensate required as product is accumulated in, and withdrawn from, an intermediate section of the condenser. Water may be used as cooling liquid for the condensation of the vapours, containing gasoline together with C4 and lighter hydrocarbons, obtained as overhead in the fractionation of the products of the catalytic ...

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15-09-2002 дата публикации

PROCEDURE FOR THE CLEANING OF A ACROLEIN OF CONTAINING GAS FLOW

Номер: AT0000223885T
Принадлежит:

Подробнее
15-02-1989 дата публикации

VERFAHREN UND VORRICHTUNG ZUR RUECKGEWINNUNG VON LOESUNGSMITTELN AUS GASEN

Номер: ATA140288A
Автор:
Принадлежит:

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15-01-2020 дата публикации

Verfahren und Vorrichtung zur Gewinnung von Wasser aus Luft

Номер: AT0000521380B1
Принадлежит:

Die Erfindung betrifft ein Verfahren zur Gewinnung von Wasser aus Luft (2, 2‘) mit folgenden nacheinander und parallel zueinander ablaufenden Schritten: a) Gaswäsche der Luft (2, 2‘) in einem Gaswäscher (1) mit einer gekühlten wässrigen Kaliumcarbonatlösung, welche derart gekühlt ist, dass die Luft (2, 2‘) im Gaswäscher (1) unter ihren Taupunkt abgekühlt wird, b) Ableiten der Kaliumcarbonatlösung aus dem Gaswäscher (1), c) Erwärmen der abgeleiteten Kaliumcarbonatlösung über zumindest eine Wärmpumpe (3a, 3b), d) Verdampfen von Wasser aus der erwärmten Kaliumcarbonatlösung und Kondensieren des gebildeten Wasserdampfes sowie Sammeln des Wassers, e) Kühlen von zumindest einem Teilstrom (TS1) der nach Schritt d) zurückbleibenden Kaliumcarbonatlösung über die zumindest eine Wärmpumpe (3a, 3b) gemäß Schritt c), − wobei die in Schritt e) erhaltene, gekühlte Kaliumcarbonatlösung in Schritt a) verwendet wird.

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11-09-2008 дата публикации

Apparatus for the production of alcohol

Номер: AU2003283281B2
Принадлежит:

Подробнее
13-03-2014 дата публикации

Bubble-column vapor mixture condenser

Номер: AU2012312643A1
Принадлежит:

In a bubble-column vapor mixture condenser, a fluid source supplies a carrier-gas stream including a condensable fluid in vapor phase. The condensable fluid in liquid form is contained as a bath in a chamber in each stage of the condenser, and the carrier gas is bubbled through the bath to condense the fluid into the bath. Energy from condensation is recovered to a coolant in a conduit that passes through the liquid in the stages of the condenser. The bubble-column vapor mixture condenser can be used, e.g., in a humidification-dehumidification system for purifying a liquid, such as water.

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21-01-1993 дата публикации

HEAT AND MASS TRANSFER

Номер: AU0000633074B2
Принадлежит:

Подробнее
19-03-2015 дата публикации

SYSTEMS INCLUDING A CONDENSING APPARATUS SUCH AS A BUBBLE COLUMN CONDENSER

Номер: CA0002924121A1
Принадлежит:

Condensing apparatuses and their use in various heat and mass exchange systems are generally described. The condensing apparatuses, such as bubble column condensers, may employ a heat exchanger positioned external to the condensing vessel to remove heat from a bubble column condenser outlet stream to produce a heat exchanger outlet stream. In certain cases, the condensing apparatus may also include a cooling device positioned external to the vessel configured and positioned to remove heat from the heat exchanger outlet stream to produce a cooling device outlet stream. The condensing apparatus may be configured to include various internal features, such as a vapor distribution region and/or a plurality of liquid flow control weirs and/or chambers within the apparatus having an aspect ratio of at least 1.5. A condensing apparatus may be coupled with a humidifier to form part of a desalination system, in certain cases.

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29-11-2012 дата публикации

METHOD, APPARATUS AND SYSTEM FOR CONCENTRATING SOLUTIONS USING EVAPORATION

Номер: CA0002816746A1
Принадлежит:

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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25-08-1905 дата публикации

Cooling system or of heating of the liquids by mixture with others liquid nonmiscible with them

Номер: FR0000004246E
Принадлежит:

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29-03-1935 дата публикации

A method for withdrawing solvents of organic matter solutions

Номер: FR0000779074A
Автор:
Принадлежит:

Подробнее
14-04-1961 дата публикации

Final condenser to absorb the naphthalene of the coke oven gas

Номер: FR0001258250A
Автор:
Принадлежит:

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04-09-1929 дата публикации

Improvements with the purifiers associated with the boiling-in apparatuses

Номер: FR0000664517A
Автор:
Принадлежит:

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17-03-2017 дата публикации

COOLING TOWER WITHOUT ENTRAINMENT VESICULAR

Номер: FR0003041087A1
Автор: MANON ALEXANDRE
Принадлежит: JACIR

La tour de refroidissement comprend un corps d'échange thermique 14, un système de distribution 16 d'un liquide sur le corps d'échange thermique, un moyen de génération 26 d'un flux de gaz en direction du corps d'échange thermique, et un séparateur 18 de gouttes disposé en aval du corps d'échange thermique 14 et apte à séparer des gouttelettes de liquide distribué qui sont entrainées par le flux de gaz. La tour comprend en outre un moyen de filtrage 20 par absorption disposé en aval du séparateur de gouttes, perméable aux gaz et apte à absorber des gouttelettes de liquide distribué entrainées par le flux de gaz.

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28-12-2000 дата публикации

SYSTEM AND APPARATUS FOR CONDENSING BOIL-OFF VAPOR FROM A LIQUIFIED NATURAL GAS CONTAINER

Номер: WO0000079179A1
Автор: ENGDAHL, Gerald, E.
Принадлежит:

L'invention concerne un système et un appareil de condensation de vapeur évaporée provenant d'un conteneur de gaz naturel liquéfié (LNG). Ledit système de condensation de vapeur consiste à créer une zone de contact (56) à l'intérieur d'un réservoir (10) de condenseur, acheminer la vapeur (28) vers ledit réservoir (10), à produire un fluide de condensation (66) et un fluide moteur (72), acheminer le fluide de condensation ¿(66) vers le réservoir (10) de condenseur, faire varier le flux de fluide de condensation (66) pour réguler la pression dans le réservoir (10), mettre en contact la vapeur (28) avec le fluide de condensation (66) de manière à créer un condensat, et mélanger le condensat et le fluide moteur (72). L'appareil de condensation de vapeur comporte un réservoir (10), une entrée (64) de gaz liquéfié dans le réservoir, un dispositif de commande (114, 128) de l'entrée de gaz liquéfié (64) conçu pour faire varier un premier flux de gaz liquéfié (66) de manière à réguler la pression ...

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24-12-2019 дата публикации

Control system and method for multiple parallel desalination systems

Номер: US0010513445B2
Принадлежит: Gradiant Corporation, GRADIANT CORP

Embodiments described herein generally relate to humidification-dehumidification desalination systems, including apparatuses that include a vessel comprising a humidification region (e.g., a bubble column humidification region) and a dehumidification region (e.g., a bubble column dehumidification region), mobile humidification-dehumidification (HDH) desalination systems (e.g., systems having a relatively low height and/or a relatively small footprint), and associated systems and methods. Certain embodiments generally relate to methods of operating, controlling, and/or cleaning desalination systems comprising a plurality of desalination units (e.g., HDH desalination units).

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08-11-1995 дата публикации

Process to separate gaseous substances from air, containing a high proportion of substances having a low boil point

Номер: EP0000681154A1
Автор: Förster, Hans, Dr.
Принадлежит:

Abatement of volatile organic cpds. The volatile organic compounds or VOCs, are abstracted in a cold scrubber (2) at very low temperatures, where the lighter components are present as fluid condensate. The condensate is removed, pressurised, and passed to heat exchange (10). The extraction stream is heated to ambient temperature, and freed of water in the receiver (21). Dry organic fluid condensate (9), is produced from the plant. The equilibrium between the produced fluid product (9) and the organic vapour quantity contained in the air (1), is compensated, after the adjustment of fluid levels.

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03-03-2020 дата публикации

СПОСОБ ОКИСЛЕНИЯ ТИОЛЬНЫХ СОЕДИНЕНИЙ В ОДНОМ СОСУДЕ

Номер: RU2715705C1
Принадлежит: ЮОП ЛЛК (US)

Изобретение относится к способу окисления одного или более тиольных соединений из потока щелочи и отделения побочного продукта масла и избыточного воздуха от потока окисленной щелочи в одном сосуде, включающему: A) подачу смешанного потока, содержащего поток щелочи, в сосуд, имеющий секцию окисления, разделительную стенку, соединенную с нижней частью сосуда, секцию разделения и удлиненную горловину, содержащую секцию отходящего газа, причем все секции содержат один или более насадочных элементов, а последние две секции также содержат элемент отмывки, который включает в себя распределительное устройство и сетку; B) подачу потока окисленной щелочи через разделительную стенку в секцию разделения, содержащую первую камеру и вторую камеру, причем первая камера содержит сетку с покрытием, и C) подачу потока отходящего газа, также известного как отработанный воздух, через горловину, где отходящий газ отмывается с помощью промывочного масла, а затем направляется в резервуар с воздушником. Изобретение ...

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27-10-2005 дата публикации

УСТАНОВКА ДЛЯ ПОЛУЧЕНИЯ СПИРТА

Номер: RU2005115462A
Принадлежит:

... 1. Установка для получения спирта из растительных видов сырья, содержащая позицию (13) ферментации для сбраживания разжиженного сырья в мезгу, позицию (15) перегонки для отделения спирта от мезги, позицию (21, 31) сушки образующейся на позиции перегонки (15) барды, отличающаяся тем, что для получения спирта из зерновых выполнены позиция помола (1) для размалывания в муку содержащих крахмал и/или сахар ядер зерновых с отделением, по меньшей мере, части окружающих ядра оболочек и позиция разжижения (9) для приведения муки в удобное для переработки состояние, при этом отделенные оболочки выполнены с возможностью подачи на позицию сушки (21, 31) в качестве среды-носителя для сушки барды. 2. Установка по п.1, отличающаяся тем, что на позиции (1) помола предусмотрена возможность отделения оболочек в весовом соотношении между оболочками и мукой от 1:9 до 2:8. 3. Установка по п.1 или 2, отличающаяся тем, что на позиции (1) помола зерновые размалываются в муку с получением среднего класса крупности ...

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30-08-1990 дата публикации

Номер: DE0003916073C1

A washing condenser as a backflow reactor for heat and material exchange is filled with two substances which have the ideal mixing ratio but different boiling points. One is fed in as a vapour (10) and condensed in backflow with the condensate (11) of the other as a washing fluid. The heat of condensation may be drawn off with the vapours (6) of the washing fluid at its boiling point.

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03-08-1995 дата публикации

Optimiertes Verfahren zur Aufarbeitung von wasserdampfbasierten Brüdenströmen

Номер: DE0004402883A1
Принадлежит:

The objet of the invention is an optimised process for regenerating a steam-heating stream charged with water-vapour-volatile organic components by condensing the vapour phase with the recovery of the heat of condensation and the at least proportional separation of the water-vapour-volatil organic components of aqueous condensate. The process operates with a first energy exchange step in which the continuously supplied vapour stream is conveyed together with a cooled liquid stream of condensed vapours fed through a circuit. Heat is indirectly extracted from the stream of liquid thus heated in a subsequent second energy transfer step. A partial flow is taken from the liquid circuit of the condensed vapours and subsjected in a diaphragm process to material separation, while the remainder of the liquid stream is returned to the first operative stage. The invention describes the use of this operation principle to major engineering applications, especially the separation of mixtures of organic ...

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18-03-1992 дата публикации

RECOVERY OF DESORBATE

Номер: GB0002211753B

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02-06-1983 дата публикации

Improved method of drying and apparatus for drying

Номер: GB0002109256A
Принадлежит:

The invention relates to a method of drying moisture containing material by subjecting the material to a pressure below atmospheric pressure e.g. by a steam ejector 18. Because of the reduced pressure, moisture is given up by the material to be dried in the form of water vapour along line 14. This vapour is passed into a condenser 24, which is vented to allow air to escape, but the vapour travelling towards the vent 48 is caused to counter flow with an incoming relatively cold fluid from a supply 44 so that the temperature of the vapour/ air mixture is reduced in order to reduce the quantity of water vapour carried away by the vented air. Consequently, there is a saving in heat energy, which manifests itself in the condensate. ...

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28-05-1981 дата публикации

FLEXIBLE MULTICOLUMNAR CELLULAR HEAT EXCHANGER

Номер: AU0000516342B2
Автор: CARRICO A J, A.J. CARRICO
Принадлежит:

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19-07-2018 дата публикации

METHOD AND DEVICE FOR COOLING A FLUID STREAM OF AN ELECTROLYSIS UNIT AND FOR OBTAINING WATER

Номер: CA0003049927A1
Принадлежит: SMART & BIGGAR

The invention relates to a device and to a method for cooling a fluid stream of an electrolysis unit and for obtaining water from ambient air by means of a plurality of steps. A humid air stream having a first molar quantity of water is led into an evaporating unit. Then, raw water is led into the evaporating unit countercurrently to the humid air, wherein in the evaporating unit there is a temperature of at most the boiling temperature of the water. In the evaporating unit, pure water is evaporated from the raw water into the humid air flow, the raw water thus being cooled. The cooled raw water is led into a heat exchanger and the fluid stream of the electrolysis unit is led into the heat exchanger, wherein heat is transferred from the fluid stream to the raw water. The pre-heated raw water is led back into the evaporating unit. The humid air with the pure water is led into a water-obtaining unit and a second molar quantity of the pure water is separated from the humid air with water ( ...

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01-03-2012 дата публикации

System for collecting condensed dew water and a method of using the same

Номер: US20120048117A1
Принадлежит: Individual

A system for condensing water from atmospheric air is disclosed. The aforesaid device comprises (a) a structure comprising at least one cooled member connectable to a cooling device, the surface has a temperature lower than a dew point of an ambient atmosphere and adapted to condense water from ambient atmosphere; (b) at least one water collecting channel adapted to collect said water condensed on the cooled member and, (c) a water storage subsystem fluidly connected to at least one water collecting channel; The member is configured in a form of a hollow shell. The cooled member has an outer downward surface.

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26-07-2012 дата публикации

Fresh water recovery system

Номер: US20120186970A1
Автор: Dwight L. Jaeger
Принадлежит: Individual

A fresh water recovery system includes a solar heated evaporator and a heat exchanger operating in a waste heat recovery mode for recovering fresh water from a salt water supply.

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16-08-2012 дата публикации

Controlled-gradient, accelerated-vapor-recompression apparatus and method

Номер: US20120205232A1
Принадлежит: Purestream Technology LLC

An accelerated vapor recompression apparatus 10 converts incoming flow 35 a to a concentrate 35 c by developing a concentration profile 146 within a tank 30 holding a liquid 23 containing dissolved solids. The resulting curve 160 of saturation temperature of the stratified liquid 23 (such as a brine 23 or other material 23 ) moves away from the curve 162 corresponding to fully mixed conditions. The shift 174, 180 in saturation temperature results in increased boiling without increased energy from a heater 70 or compressor 50. A method 90, 200 of control of the system provides interventions 203, 204, 205, 206 at different levels 92, 94, 96, 98 of control, ranging from mass flows 35 to work of a compressor 50, heat from a heater 70, and a predictive processing 215 of feedback 217 for controlling commands 216 algorithmically.

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17-01-2013 дата публикации

Method and apparatus for processing vegetable oils

Номер: US20130018197A1
Автор: Marco Kruidenberg
Принадлежит: Cargill Inc

The present invention provides certain improvements in methods for processing vegetable oils and apparatus for carrying out such methods. One embodiment provides a method for processing a partially processed oil including glycerides and a volatilizable impurity fraction. The partially processed oil may processed by driving off a first volatiles stream comprising a portion of the glycerides and at least a portion of the volatilizable impurity fraction, leaving a deodorized oil. The first volatiles stream may be introduced into a first condensing chamber and a glyceride-rich, impurity-poor first condensate may be condensed from the first volatiles stream, leaving a glyceride-poor, impurity-rich second volatiles stream. The second volatiles stream may be passed into a second condensing chamber and a glyceride-poor, impurity-rich second condensate may be condensed from the second volatiles stream.

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28-03-2013 дата публикации

Bubble-Column Vapor Mixture Condenser

Номер: US20130075940A1

In a bubble-column vapor mixture condenser, a fluid source supplies a carrier-gas stream including a condensable fluid in vapor phase. The condensable fluid in liquid form is contained as a bath in a chamber in each stage of the condenser, and the carrier gas is bubbled through the bath to condense the fluid into the bath. Energy from condensation is recovered to a liquid composition in a conduit that passes through the liquid in the stages of the condenser. The bubble-column vapor mixture condenser can be used, e.g., in a humidification-dehumidification system for purifying a liquid, such as water.

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18-04-2013 дата публикации

Contaminant cold trap for a vapor-compression refrigeration apparatus

Номер: US20130091871A1
Принадлежит: International Business Machines Corp

Apparatuses and methods are provided for facilitating cooling of an electronic component. The apparatus includes a vapor-compression refrigeration system. The vapor-compression refrigeration system includes an expansion component, an evaporator and a compressor coupled in fluid communication via a refrigerant flow path. The evaporator is coupled to and cools the electronic component. The apparatus further includes a contaminant cold trap coupled in fluid communication with the refrigerant flow path. The cold trap includes a refrigerant cold filter and a coolant-cooled structure. At least a portion of refrigerant passing through the refrigerant flow path passes through the refrigerant cold filter, and the coolant-cooled structure provides cooling to the refrigerant cold filter to cool refrigerant passing through the filter. By cooling refrigerant passing through the filter, contaminants solidify from the refrigerant, and are deposited in the refrigerant cold filter.

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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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10-04-2014 дата публикации

Vapor Compression Steam Stripping

Номер: US20140097076A1
Принадлежит: ALGENOL BIOFUELS INC.

The invention provides systems and methods for the pre-concentration of a target molecule from feed solution comprising a low concentration of the target molecule. 1. An apparatus for concentrating a dilute feed of ethanol in water , comprising:a) a counter-current vapor-liquid contactor having an inlet at the top of the counter-current vapor-liquid contactor for the dilute feed, an outlet at the bottom of the counter-current vapor-liquid contactor for a depleted feed solution, an inlet at the bottom of the counter-current vapor-liquid contactor for a vapor phase input, and an outlet at the top of the counter-current vapor-liquid contactor for a vapor phase output;b) an evaporator that evaporates a liquid feed to produce the vapor phase input to the counter-current vapor-liquid contactor, the evaporator having an inlet for the liquid feed and an outlet for the vapor phase input to the counter-current vapor-liquid contactor;c) a condenser that condenses the vapor phase output of the counter-current vapor-liquid contactor to produce a condensed liquid product and that transfers latent heat released by condensation to the evaporator, the condenser having an inlet for the vapor phase output of the counter-current vapor-liquid contactor and an outlet for the condensed liquid product;d) a compressor that compresses the vapor phase output of the counter-current vapor-liquid contactor or the vapor phase input to the counter-current vapor-liquid contactor, the compressor having an inlet and an outlet for the vapor phase output of the counter-current vapor-liquid contactor or the vapor phase input to the counter-current vapor-liquid contactor;e) a first heat exchanger having inlets and outlets for the dilute feed entering the counter-current vapor-liquid contactor, the depleted feed solution leaving the counter-current vapor-liquid contactor, the condensed liquid product leaving the condenser, or the liquid feed entering the evaporator;f) fluid connections among the inlets ...

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02-01-2020 дата публикации

Production of purified dialkyl-furan-2,5-dicarboxylate (dafd) in a retrofitted dmt plant

Номер: US20200002301A1
Принадлежит: Eastman Chemical Co

Disclosed is a process to produce a purified vapor comprising dialkyl-furan-2,5-dicarboxylate (DAFD). Furan-2,5-dicarboxylic acid (FDCA) and an alcohol in an esterification zone to generate a crude diester stream containing dialkyl furan dicarboxylate (DAFD), unreacted alcohol, 5-(alkoxycarbonyl)furan-2-carboxylic acid (ACFC), and alkyl furan-2-carboxylate (AFC). The esterification zone comprises at least one reactor that has been previously used in an DMT process.

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09-01-2020 дата публикации

Autonomous apparatus for extracting water from the air

Номер: US20200009497A1
Принадлежит: Czech Technical University In Prague

An apparatus for extracting water from ambient air is disclosed comprising an air duct for the process air, an air duct for the regeneration air and a sorption exchanger moving at least partially between the two air ducts. Additionally, in the air duct for the regeneration air, on the side facing the sorption exchanger outlet, a cooler is installed, and on the side facing its inlet, a heater is installed. The apparatus also comprises a closed refrigerant circuit. The cooler for cooling the regeneration air is a refrigerant evaporator and this cooler is, by the refrigerant piping via a compressor for the evaporated refrigerant suction and compression, connected to the regeneration air heater, where this heater for heating the regeneration air is a condenser for condensing the refrigerant vapor. The apparatus also comprises a subcooler for additional heat removal from the refrigerant.

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25-01-2018 дата публикации

MULTI-STAGE DISTILLATION SYSTEM, METHOD FOR THE OPERATION THEREOF

Номер: US20180021691A1
Автор: LEHMANN MARKUS
Принадлежит:

A multi-stage distillation system includes multiple stages, and each stage Si includes an evaporator Ei and a condenser Ci. Each condenser includes a steam chamber in pressure-connection with a steam chamber of each evaporator of the same stage. Each evaporator has a steam chamber outlet connected to a spray inlet of the next evaporator Ei+1, and the outlet of the last evaporator En connects to the spray inlet of the first evaporator E with a respective fluid line to form an evaporator circuit. Each outlet of each condenser Ci connects to the one spray inlet of the previous condenser Ci−1, and the outlet of the first condenser C connects to the spray inlet of the last condenser Cn with a fluid line to form a condenser circuit. A steam line connects between condensers Ci+1 and Ci or between the evaporators En and E 120-. (canceled).21. A multistage distillation system , comprising:a plurality of stages Si, where i=1, . . . n, wherein each stage Si works in a higher pressure and temperature range (Δ Pi, Δ Ti) than its ensuing stage Si+1 during operation, wherein each stage Si includes a pressure-tight vessel Vi that contains an evaporator Ei and a condenser Ci, wherein each evaporator Ei includes a spray inlet for introducing and spraying added liquid into the evaporator Ei and a lower outlet for letting out liquid from the evaporator Ei and defines a steam space between the spray inlet and the lower outlet, wherein each condenser Ci includes a spray inlet for introducing and spraying added liquid into condenser Ci and a lower outlet for letting out liquid from the condenser Ci and defines a steam space between the spray inlet and the lower outlet;a pressure-tight steam pipe disposed within each vessel Vi and connecting the steam space of each evaporator Ei with the steam space of each condenser Ci, the pressure-tight steam pipe being configured with a cross section large enough that the pressure Pi in the steam space between the evaporator Ei and the condenser Ci of ...

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25-01-2018 дата публикации

PROCESS FOR REMOVING IMPURITIES FROM ACETIC ACID

Номер: US20180021692A1
Принадлежит:

A process of purifying acetic acid is provided. The process includes feeding a stream of acetic acid into a distillation column and distilling acetic acid in the presence of an oxidizing agent in the distillation column, to oxidize oxidizable impurities in the acetic acid, wherein the oxidizing agent is an oxidant capable of cleaving C═C bonds. The process further includes removing a distilled acetic acid stream from the distillation column. Further processes for purifying acetic acid and systems for purifying acetic acid are also provided. 1. A process for purifying acetic acid , comprising:feeding a stream of acetic acid into a distillation column;distilling acetic acid in the presence of an oxidizing agent in the distillation column, to oxidize oxidizable impurities in the acetic acid, wherein the oxidizing agent is capable of cleaving C═C bonds; andremoving a distilled acetic acid stream from the distillation column.2. The process of claim 1 , wherein the oxidizable impurities comprise one or more α claim 1 ,β-unsaturated carbonyl compounds.3. The process of claim 2 , wherein the one or more α claim 2 ,β-unsaturated carbonyl compounds comprise one or more α claim 2 ,β-unsaturated carboxylic acids.4. The process of claim 2 , wherein the one or more α claim 2 ,β-unsaturated carboxylic acids comprise acrylic acid.5. The process of claim 1 , wherein the distillation column comprises a top and a bottom and wherein the oxidizing agent is positioned at or near the bottom of the distillation column.6. The process of claim 5 , wherein the distillation column comprises a sump at the bottom of the distillation column and the oxidizing agent is positioned in the sump.7. A process for purifying acetic acid claim 5 , comprising: [ a top and a bottom; and', 'a sump at the bottom of the distillation column; and, 'the distillation column comprises, 'wherein the stream of acetic acid is fed into the distillation column at or near the bottom of the distillation column; and, ' ...

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25-01-2018 дата публикации

Discontinuously operating desublimator for the separation of products out of gas mixtures

Номер: US20180021693A1
Принадлежит: KELVION GMBH

A discontinuously operating desublimator for the recovery of products from gas mixtures is disclosed having a housing including an inner cooling line and a housing wall, inwardly directed lamellae arranged on an inside of the housing wall which can be cooled for the desublimation of the product by a cooling medium conducted through ducts on the housing wall. The housing is cylindrical and enables the product to be melted down by a change of pressure.

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24-01-2019 дата публикации

Production of purified dialkyl-furan-2,5-dicarboxylate (dafd) in a retrofitted dmt plant

Номер: US20190023677A1
Принадлежит: Eastman Chemical Co

Disclosed is a process to produce a purified vapor comprising dialkyl-furan-2,5-dicarboxylate (DAFD). Furan-2,5-dicarboxylic acid (FDCA) and an alcohol in an esterification zone to generate a crude diester stream containing dialkyl furan dicarboxylate (DAFD), unreacted alcohol, 5-(alkoxycarbonyl)furan-2-carboxylic acid (ACFC), and alkyl furan-2-carboxylate (AFC). The esterification zone comprises at least one reactor that has been previously used in an DMT process.

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31-01-2019 дата публикации

Temperature-Matched Influent Injection in Humidifier Systems and Associated Methods

Номер: US20190031531A1
Принадлежит: Gradiant Corporation

Temperature-matching of an injected influent stream with a location along a humidifier feed stream flow path is generally described. According to embodiments, an influent stream can be injected into and combined with a feed stream of a humidifier at a location on the humidifier feed stream flow path at which the temperature of the feed stream most closely matches the temperature of hot influent stream. 1. A humidification method , comprising:flowing a first liquid stream comprising water and a dissolved salt, the first liquid stream having a first temperature, through a first heating device, wherein the first liquid stream is heated to a second temperature within the first heating device to form a heated liquid stream;combining the heated liquid stream with a second liquid stream comprising water and a dissolved salt, the second liquid stream having a third temperature, to form a combined liquid stream;directly contacting the combined liquid stream with an influent gas stream to transfer to heat and mass from the combined liquid stream to the influent gas stream within a humidifier, wherein the heat and mass transfer produces a humidified gas stream enriched in water vapor with respect to the influent gas stream;wherein, the difference between the first temperature and the third temperature is greater in magnitude than the difference between the second temperature and the third temperature.2. The method according to claim 1 , further comprising flowing the combined liquid stream through a second heating device prior to directly contacting the combined liquid stream with the influent gas stream claim 1 , and heating the combined liquid stream to a fourth temperature within the second heating device claim 1 , wherein the difference between the third temperature and the fourth temperature is greater in magnitude than the difference between the second temperature and the third temperature.3. The method according to claim 1 , further comprising flowing the first liquid ...

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08-02-2018 дата публикации

Process Scheme To Improve Divalent Metal Salts Removal From Mono Ethylene Glycol (MEG)

Номер: US20180037527A1
Принадлежит: Cameron International Corp

A MEG reclamation process includes the step of increasing above 2,000 ppm the divalent metal salts concentration of a rich (wet) MEG feed stream flowing into a precipitator. The increasing step includes routing a salts-saturated MEG slipstream from the flash separator it to the precipitator. The slipstream may be mixed with a fresh water feed stream, a portion of the rich MEG feed stream, or some combination of the two. The rich MEG feed stream also may be split into two streams, with a portion of the stream being heated and routed to the flash separator and the other portion being combined as above with the removed slipstream. The process can be performed on the slipstream after dilution and prior to entering the precipitator or after being loaded into the precipitator. Removal of the insoluble salts may be done in either a batch or continuous mode.

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15-02-2018 дата публикации

Fresh-Water Generating Apparatus

Номер: US20180043277A1
Автор: Ito Tomoaki
Принадлежит:

To provide a fresh water-generating apparatus that does not require large amounts of heating energy as in the past, also does not require maintenance such as replacement of reverse osmosis membranes, and is simpler and inexpensive. 1. A fresh-water generating apparatus , characterized by comprising:a first storage tank in which seawater, sludge water, oily water, industrial waste water, or another stored liquid is accommodated;a first water-absorbing base material of which a lower end is impregnated with the stored liquid of the first storage tank;a blowing means for blowing air at an upper-end side of the first water-absorbing base material;a second water-absorbing base material for causing water vapor vaporized and blown out from the upper-end side of the first water-absorbing base material by the air blown by the blowing means to adsorb and condense on the upper-end side, the second water-absorbing base material being designed so that the condensed water droplets drip down from a lower-end side;a second storage tank in which the condensed water dripping down from the lower-end side of the second water-absorbing base material is stored;a lid for closing an upper space of the first and second storage tanks; anda guide pipe of which one end communicates with the upper space of the second storage tank of the lid to exhaust the air blown from the blowing means, and the other end communicates with the upper space of the first storage tank and with an intake side of the blowing means to form a circulation path for the blown air.2. The fresh-water generating apparatus according to claim 1 , wherein the first and second water-absorbing base materials comprise synthetic zeolite of which each hole diameter of a porous structure is formed to the size of a water molecule.3. The fresh-water generating apparatus according to claim 1 , wherein the first and second water-absorbing base materials comprise nanocarbon of which each hole diameter of a porous structure is formed to ...

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15-02-2018 дата публикации

REACTOR EFFLUENT WASH TO REMOVE AROMATICS

Номер: US20180043280A1
Принадлежит:

A process is presented for the removal or aromatics from a hydrocarbon stream. The hydrocarbon stream is generated by a dehydrogenation process that generates aromatics. The process includes a two contact cooler system with the first and second contact coolers using different coolants. The second coolant is a non-aromatic hydrocarbon coolant that will absorb aromatics. 1. A process for removing aromatics from a process stream , comprising:passing the process stream comprising paraffins, olefins and trace aromatics to a first contact cooler using a first coolant to generate a first stream;passing the first stream to a compressor to generate a second stream; andpassing the compressed stream to a second contact cooler using a second coolant to generate a third stream comprising olefins and paraffins.2. The process of further comprising:passing a hydrocarbon stream comprising paraffins to a dehydrogenation reactor to generate the process stream comprising olefins and paraffins.3. The process of further comprising passing the third stream to a cryogenic separation unit to generate an olefin and paraffin product stream.4. The process of wherein the first coolant comprises an aromatic solvent as a coolant.5. The process of wherein the second coolant comprises a paraffinic solvent or an alkylate solvent.6. The process of wherein the first stream is cooled to a temperature between 10° C. and 45° C.7. The process of wherein the first stream is compressed to a pressure between 250 kPa and 600 kPa.8. The process of wherein the first stream has a reduced aromatics content.9. The process of wherein the first stream has an aromatics content below 1500 ppmw.10. The process of wherein the third stream has an aromatics content below 100 ppmw.11. The process of wherein the third stream is cooled to a temperature between 10° C. and 45° C.12. A process for the production of olefins from paraffins claim 1 , comprising:passing a hydrocarbon stream comprising paraffins to a dehydrogenation ...

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03-03-2022 дата публикации

Condensate recovery unit

Номер: US20220062811A1
Принадлежит: ConocoPhillips Co

Production equipment and methods which reduce “gray” or off-specification production and improve central processing facility (CPF) efficiency. The process is a combination of unit operations (heat exchange, pumping, and separation) to produce an on-spec gas product, an on-spec condensate product, and/or on-spec oil product. It does so by placing the feed under pressure and heating it to the point that it can be vaporized and separated. The blended components are modulated dependent upon the composition of the produced fluids, produced gas, and off-specification fluid to efficiently produce on-specification products.

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13-02-2020 дата публикации

PROCESSES FOR SEPARATING AN MTO EFFLUENT

Номер: US20200047079A1
Принадлежит:

A process is presented for removing the fouling problems associated with the product recovery in a methanol to olefins conversion process. The process includes passing the quenched MTO process stream to a product separator, wherein an intermediate stream is generated and includes water and heavier hydrocarbons. The intermediate stream is processed to remove the buildup of heavier hydrocarbons. 1. A process for separating heavy hydrocarbons from an MTO reactor effluent , the process comprising:separating an effluent from an MTO reaction zone in a product separation zone into a vapor stream comprising olefinic hydrocarbons, oxygenates, and steam, and a first liquid stream comprising two phases, a first phase comprising water and a second phase comprising heavy hydrocarbons;compressing the vapor stream in a compression zone having a plurality of stages of compression and being configured to provide at least one compressed liquid stream and a compressed vapor stream, each compressed liquid stream comprising two phases, a first phase comprising water and a second phase comprising heavy hydrocarbons; and,separating the first liquid stream from the product separation zone and the at least one compressed liquid stream from the compression zone in a separation vessel into a hydrocarbon liquid stream and a lean hydrocarbon water stream.2. The process of wherein the separation vessel comprises a settling vessel.3. The process of further comprising:stripping DME from the vapor stream in a DME stripping zone, wherein the DME stripping zone includes a charge drum and a stripping column, and wherein the compressed vapor stream is provided by the charge drum.4. The process of claim 3 , wherein the charge drum provides the at least one compressed liquid stream claim 3 , and further comprising:separating the at least one compressed liquid stream from the charge drum in the separation vessel into the hydrocarbon liquid stream and the lean hydrocarbon water stream.5. The process of ...

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23-02-2017 дата публикации

Gravity power and desalination technology system

Номер: US20170051717A1
Автор: Dongho Kim
Принадлежит: Individual

A gravity power and desalination technology system is provided, including a heat storage apparatus, an inner tube portion, a hot-air and vapor generator, and venting holes, a corrugated tube portion, an outer tube portion, an updraft wind power generator, and an artificial hydro power generator. The heat storage apparatus is provided in a lower portion and configured. The inner tube portion has an inner vent portion inside and disposed vertically over the heat storage apparatus. The hot-air and vapor generator is disposed between the heat storage apparatus and the inner tube portion. The venting holes are bored through the inner tube portion obliquely outwards. The corrugated tube portion is provided on a top portion of the outer tube portion. The updraft wind power generator and the artificial hydro power generator are installed in the lower portions of the inner vent portion and the outer vent portion, respectively.

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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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10-03-2022 дата публикации

SYSTEM AND METHOD FOR SUSTAINABLE GENERATION OF ENERGY

Номер: US20220074373A1
Принадлежит:

A system for sustainable generation of energy, comprising at least one device for converting natural power into useful energy, and at least one internal combustion engine or heat engine. The internal combustion engine or heat engine may be connected to a gas cleaning device for fuel or heat supply. A method for sustainable generation of energy, comprising the steps of generating a first amount of useful energy by converting natural power; and generating a second amount of energy by operating at least one internal combustion engine or heat engine, wherein the internal combustion engine or heat engine is driven by fuel or heat derived from cleaning a waste gas. 1. A system for sustainable generation of energy , comprising:at least one internal combustion engine and at least one heat engine, the internal combustion engine and heat engine being connected to a gas cleaning device for fuel supply and heat supply, respectively,wherein at least one device for converting natural power into useful energy comprises a wave power generator which is configured for generating electrical energy and which is connected to a grid,wherein the wave power generator is further connected to a cold buffer, which in turn is connected to the heat engine, the wave power generator being configured to drive a pump that is configured to pump cold water to the heat engine,wherein the heat engine is further connected to a heat buffer which is configured to receive heat from the at least one internal combustion engine and/or industrial waste heat, andwherein the heat engine is configured to generate electrical energy utilizing a temperature differential between the cold buffer and the heat buffer and to supply the electrical energy to the grid or to an end user.2. The system according to claim 1 , wherein the gas cleaning device comprises a multi-stage condenser arrangement.3. The system according to claim 1 , wherein a further natural power conversion device is selected from the group consisting of ...

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02-03-2017 дата публикации

Water distilling and purifying unit and variants thereof

Номер: US20170057834A1
Принадлежит: Individual

A water purification unit includes an evaporator, a heat exchanger, a pump and a liquid-driven condensing ejector. A liquid inlet of the ejector is in fluid communication with an outlet of the pump. A gas inlet of the ejector is in fluid communication with a vapor outlet of the evaporator. An outlet of the ejector is in fluid communication with a fluid inlet of the heat exchanger. A fluid outlet of the heat exchanger is in fluid communication with an intake of the pump. The heat exchanger is in thermal communication with a fluid inlet to the evaporator.

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28-02-2019 дата публикации

Methods and Apparatuses for Water Purification

Номер: US20190060778A1
Принадлежит: Individual

An apparatus for generating purified liquid from an input liquid, comprises, an evaporation chamber flooded with the input liquid and wherein the evaporation chamber generates saturated gases and comprises a shared wall with the condensation chamber and wherein the evaporation chamber is configured to generate evaporation cavities and condensation cavities on respective sides of the shared wall for a 2-phase counter flow of a liquid phase component and a gaseous phase component in composite flows for a 2-phase to 2-phase direct latent heat exchange. A condensation chamber has channels disposed in the input liquid, wherein liquid-saturated gases are generated therefrom in the evaporation chamber. The apparatus is operated as a four-port counter-flow heat exchanger where two different fluids are exchanging heat based on the inlet ports of both fluids being on opposite sides and the outlet ports of both fluids are also on opposite sides of the evaporator and condenser.

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10-03-2016 дата публикации

Pressurized Vapor Cycle Liquid Distillation

Номер: US20160067629A1
Принадлежит:

Embodiments of the invention are directed toward a novel pressurized vapor cycle for distilling liquids. In some embodiments of the invention, a liquid purification system is revealed, including the elements of an input for receiving untreated liquid, a vaporizer coupled to the input for transforming the liquid to vapor, a head chamber for collecting the vapor, a vapor pump with an internal drive shaft and an eccentric rotor with a rotatable housing for compressing vapor, and a condenser in communication with the vapor pump for transforming the compressed vapor into a distilled product. Other embodiments of the invention are directed toward heat management, and other process enhancements for making the system especially efficient. 1. A liquid vapor distillation apparatus comprising:an evaporative condenser for transforming the liquid to a compressed vapor and for transforming the compressed vapor into a product liquid;a first heat exchanger;a second heat exchanger; and a first heat source input connected to a first heat source fluid line, the first heat source input connecting the first heat exchanger and the third heat exchanger, wherein the first heat source input is fluidly connected to a blowdown fluid line in the liquid vapor distillation apparatus; and', 'a second heat source input connected to a second heat source fluid line, wherein the second heat source input is fluidly connected to a product liquid fluid line in the liquid vapor distillation apparatus, whereby multiple heat source inputs are exchanged with the intake liquid., 'a third heat exchanger, the first heat exchanger comprising2. The apparatus of claim 1 , wherein at least one of the first and second heat exchangers further comprises a third heat source input fluidly connected to a steam pump drive motor.3. The apparatus of claim 1 , wherein at least one of the first and second heat exchangers further comprises a third heat source input fluidly connected to a Stirling engine generator powering the ...

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15-03-2018 дата публикации

CLOSED-LOOP THERMAL SERVICING OF SOLVENT-REFINING COLUMNS

Номер: US20180071799A1
Автор: MELSERT Ryan
Принадлежит: Tesla, Inc.

A method of thermally servicing a solvent-refining column comprises: running a closed-loop water-steam system past a top and bottom of a first column, the first column containing at least a solvent and impurities; boiling pressurized water in the closed-loop water-steam system to steam using first heat from the top of the first column; compressing the steam in the closed-loop water-steam system to a higher temperature; and providing second heat to the first column by condensing the steam at the bottom of the first column after compression. 1. A method of thermally servicing a solvent-refining column , the method comprising:running a closed-loop water-steam system past a top and a bottom of a first column, the first column containing at least a solvent and impurities;boiling pressurized water in the closed-loop water-steam system to steam using first heat from the top of the first column;compressing the steam in the closed-loop water-steam system to a higher temperature; andproviding second heat to the first column by condensing the steam at the bottom of the first column after compression.2. The method of claim 1 , wherein water is separated from the solvent and the impurities in a second column claim 1 , the method further comprising providing third heat to the second column by condensing the steam at a bottom of the second column after compression.3. The method of claim 2 , further comprising selectively bypassing claim 2 , at least partially claim 2 , the bottom of the first or second column with the closed-loop water-steam system.4. The method of claim 3 , further comprising applying a heater to the steam after the compression and before the bottom of the second column.5. The method of claim 1 , further comprising selectively bypassing claim 1 , at least partially claim 1 , the bottom of the first column with the closed-loop water-steam system.6. The method of claim 1 , further comprising applying a heater to the steam after compression and before the bottom of ...

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16-03-2017 дата публикации

A METHOD AND APPARATUS FOR MULTI-EFFECT ADSORPTION DISTILLATION

Номер: US20170072336A1
Автор: LI Ang, Ng Su Hui Joseph
Принадлежит:

An apparatus for multi-effect adsorption distillation, the apparatus including a plurality of consecutive effects configured for evaporation of feed water therein; and a plurality of adsorber beds configured to adsorb vapor evaporated from feed water in a last effect of the plurality of consecutive effects and to release desorbed vapor during regeneration of the plurality of adsorber beds; wherein heat in the desorbed vapor is used to evaporate feed water fed into a first effect of the plurality of consecutive effects. 1. An apparatus for multi-effect adsorption distillation , the apparatus including:a plurality of consecutive effects configured for evaporation of feed water therein;a plurality of adsorber beds configured to adsorb vapor evaporated from feed water in a last effect of the plurality of consecutive effects and to release desorbed vapor during regeneration of the plurality of adsorber beds;wherein heat in the desorbed vapor is used to evaporate feed water fed into a first effect of the plurality of consecutive effects.2. The apparatus according to claim 1 , wherein the apparatus is configured to channel the desorbed vapor into a heat exchange tube of the first effect.3. The apparatus according to claim 1 , further comprising a condenser in fluid connection with the plurality of adsorber beds claim 1 , the condenser comprising a condenser tube in fluid communication with a heat exchange tube of the first effect claim 1 , the condenser tube configured to allow heat in the desorbed vapor to be taken up by water in the condenser tube and circulated into the heat exchange tube of the first effect.4. A method of multi-effect adsorption distillation claim 1 , the method comprising:placing a last effect of a plurality of consecutive effects in a state of low pressure;adsorbing vapor evaporated from feed water in the last effect using an adsorbent;regenerating the adsorbent to release desorbed vapor;using heat in the desorbed vapor to evaporate feed water in a ...

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22-03-2018 дата публикации

METHOD AND APPARATUS FOR TREATING WATER

Номер: US20180079657A1
Автор: Ellis, JR. John C.
Принадлежит:

A method and apparatus for treating water that results in water having a hydrogen bond angle of greater than 110°, preferably in a range of about 113° to about 114°. The method includes: channeling the water into a receptacle; devolatilizing and deaerating the water in the receptacle by using a condensing channel immersed in the water contained in the receptacle; channeling a portion of the water from the receptacle to a boiler via a feeder channel; heating the water in the boiler to generate steam; providing ozone to the steam in the boiler; and channeling the steam into the condensing channel. The apparatus includes a closed receptacle, a condensing channel housed in the receptacle, and a boiler in fluid communication with the receptacle. The boiler includes a boiler housing, an ozone generator and at least one heater having a total power of about 1500 watts. 1. A method for treating water comprising:channeling the water into a receptacle;devolatilizing and deaerating the water in the receptacle by using a condensing channel immersed in the water contained in the receptacle;channeling a portion of the water from the receptacle to a boiler via a feeder channel, wherein the boiler comprises a boiler housing and one or two heaters housed in the boiler housing, wherein the boiler housing has an outer diameter of about 6.25 inches and two substantially flat and parallel surfaces that are about 2.375 inches apart;heating the water in the boiler to generate steam;providing ozone to the steam in the boiler;channeling the steam into the condensing channel immersed in the water contained in the receptacle; andflowing the water out of the condensing channel.2. The method according to claim 1 , wherein a predetermined level of the water contained in the receptacle is maintained such that a temperature of the water in the receptacle is in a range of about 180° F. to about 190° F.3. The method according to claim 1 , wherein the feeder channel is a feeder tube having a diameter ...

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12-03-2020 дата публикации

HEAT INTEGRATION IN A PROCESS FOR THE PREPARATION OF ETHYLENE CARBONATE AND ETHYLENE GLYCOL

Номер: US20200079712A1
Принадлежит:

Processes and associated reaction systems for the preparation of ethylene carbonate and ethylene glycol from ethylene oxide are provided, particularly processes and associated reaction systems directed to heat integration in the treatment of recycle gas streams. 1. A process comprising{'b': 14', '15', '20, 'supplying an ethylene oxide absorber overhead stream () to a condenser () to produce a cooled recycle gas stream () and one or more aqueous streams,'}{'b': 20', '30, 'heating at least a portion of said cooled recycle gas stream () to provide a heated recycle gas stream (),'}{'b': 30', '31', '2', '36, 'contacting said heated recycle gas stream () with one or more guard bed materials in one or more guard bed systems () positioned upstream of an ethylene oxide reactor () to provide a treated recycle gas stream (),'}{'b': 1', '36', '2', '4, 'contacting an epoxidation feed gas () comprising ethylene, oxygen and at least a portion of said treated recycle gas stream () with an epoxidation catalyst in ethylene oxide reactor () to yield an epoxidation reaction product stream (),'}{'b': 4', '9', '10', '13', '14, 'contacting the epoxidation reaction product stream () in an ethylene oxide absorber () with a lean absorbent stream () in the presence of a carboxylation and hydrolysis catalyst to yield a fat absorbent stream () comprising ethylene carbonate and/or ethylene glycol and an ethylene oxide absorber overhead stream (),'}{'b': '20', 'wherein cooled recycle gas stream () is heated by heat exchange with a hot process stream selected from'}{'b': 14', '15, '(i) the ethylene oxide absorber overhead stream (), in a condenser ();'}{'b': 24', '15, '(ii) steam () produced in an ethylene glycol purification column overhead condenser, in a first heat exchanger located downstream of condenser ();'}{'b': 25', '15, '(iii) steam () produced by flashing one or more condensate streams collected in the process, in a second heat exchanger located downstream of condenser (), or a ...

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31-03-2022 дата публикации

Cooling Systems Having An Integrated Ionic Liquid Salt Dehumidification System

Номер: US20220099314A1
Принадлежит:

A cooling system utilizes an organic ionic salt composition for dehumidification of an airflow. The organic ionic salt composition absorbs moisture from an inlet airflow to produce an outlet airflow with a reduce moisture from that of the inlet airflow. The organic ionic salt composition may be regenerated, wherein the absorbed moisture is expelled by heating with a heating device. The heating device may be an electrochemical heating device, such as a fuel cell, an electrochemical metal hydride heating device, an electrochemical heat pump or compressor, or a condenser of a refrigerant cycle, which may utilize an electrochemical pump or compressor. The efficiency of the cooling system may be increased by utilization of the waste heat the cooling system. The organic ionic salt composition may circulate back and forth or in a loop between a conditioner, where it absorbs moisture, to a regenerator, where moisture is desorbed by heating. 1. A cooling system comprising an ionic liquid dehumidification system comprising:{'claim-text': ['i) an ionic liquid desiccant;', 'ii) water;'], '#text': 'a) an ionic liquid desiccant composition comprising:'}{'claim-text': [{'claim-text': ['an ionic liquid desiccant inlet;', 'an ionic liquid desiccant outlet;'], '#text': 'i) a conditioner ionic liquid desiccant conduit having:'}, 'wherein the ionic liquid desiccant composition flows through the conditioner ionic liquid desiccant conduit;', {'claim-text': ['a conditioner fluid inlet;', 'a conditioner fluid outlet;'], '#text': 'ii) a conditioner fluid conduit having:'}, 'wherein a conditioner fluid flows through the conditioner fluid conduit; and', 'iii) an impermeable exchange membrane configured between the conditioner ionic liquid desiccant conduit and the conditioner fluid conduit;', 'wherein the conditioner fluid comprises moisture that is transferred through the conditioner impermeable exchange membrane to the ionic liquid desiccant flowing through the conditioner ionic liquid ...

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21-03-2019 дата публикации

FLUE GAS CONDENSATION WATER EXTRACTION SYSTEM

Номер: US20190083900A1
Принадлежит:

A flue gas condensation water extraction system includes a flue gas condensation-end system and a flue gas refrigeration source-end system. The flue gas condensation-end system includes a desulfurization absorption tower, a flue gas purification and condensation tower, and a condensed water storage tank. The flue gas purification and condensation tower is arranged above the desulfurization absorption tower. A flue gas outlet, a water inlet, and a water outlet are provided on the flue gas purification and condensation tower. The flue gas refrigeration source-end system includes a cooling tower. The water outlet is connected to the condensed water storage tank via a condensed water downcomer. The water inlet is connected to the cooling tower via a circulating water supply pipe. A condensation circulation water pump is provided on the circulating water supply pipe. The cooling tower is connected to the condensed water storage tank via a circulating water return pipe. 1. A flue gas condensation water extraction system , comprising:a flue gas condensation end system;a flue gas refrigeration source end system; and wherein the flue gas condensation end system comprises a desulfurization absorption tower, a flue gas purification condensation tower, and a condensate storage tank,', 'wherein the desulfurization absorption tower is provided with a flue gas inlet,', 'wherein the flue gas purification condensation tower is disposed above the desulfurization absorption tower,', 'wherein the flue gas purification condensation tower is provided with a flue gas outlet, a water inlet, and a drain,', 'wherein the flue gas refrigeration source end system comprises a cooling tower,', 'wherein the drain is connected to the condensate storage tank via a descending condensate water pipe,', 'wherein the water inlet is connected to the cooling tower via a circulating water supply pipe,', 'wherein a circulating water pump is arranged on the circulating water supply pipe,', 'wherein the ...

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31-03-2016 дата публикации

Moisture- harvesting device

Номер: US20160089616A1
Автор: Eiichi Maruyama
Принадлежит: All Round Corp

A moisture-harvesting device capable of harvesting moisture, which can be also used as drinking water or the like, from atmospheric air. The moisture-harvesting device includes: an atmospheric-air introduction unit; an atmospheric moisture converter that is provided with a mechanism for reducing a pressure of atmospheric air introduced by the atmospheric-air introduction unit and is equipped with a cooling section for cooling the introduced atmospheric air and extracting a moisture content; a water intake cock, that extracts water obtained by the atmospheric moisture converter; and a filter unit that has first to fifth fitters and is provided at an upstream side from the water intake cock, and removes foreign matter from the water obtained by the atmospheric moisture converter, whereby it is possible to harvest the moisture, which can be also used as the drinking water or the like, from the atmospheric air.

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05-05-2022 дата публикации

Method and Apparatus for Sharing Co-Generated Energy When Processing Essential Elements from Plant Matter

Номер: US20220134250A1
Принадлежит:

Methods and apparatus consistent with the present disclosure may provide electrical energy and thermal to extraction or separation equipment. Methods and apparatus consistent with the present disclosure may extract and concentrate essential elements plant matter. An amount of wasted heat energy collected from a engine that powers an electrical generator may be provided to an evaporation or separation process when electrical power is provided to extraction or separation processing equipment. Computers or electronics that control equipment consistent with the present disclosure may be remotely controlled via a mobile electronic device, when desired. Such computers or electronics may receive sensor data related to the operation of plat matter extractors, related separation equipment, or other equipment may be used to manage a production line. As such, methods and apparatus consistent with the present disclosure may extract essential elements from cannabis plant matter and process those essential elements into cannabis extracts or isolates.

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05-05-2022 дата публикации

MULTIMODE SYSTEM FOR COOLING AND DESALINATION

Номер: US20220135439A1

A multimode system for cooling and desalination includes a humidification-dehumidification (HDH) system, an ejector cooling cycle (ECC) system and valves. The HDH system includes a heater, a humidifier and a dehumidifier. The ECC system includes a generator, an evaporator, an ejector and a condenser. The valves are configured to connect to inlets and outlets of the heater, the generator and a heat source so that by selectively opening and closing the valves, the heat source is connected to the heater while disconnected from the generator, or connected to the generator while disconnected from the heater, or connected to both the heater and the generator, or disconnected from both the heater and the generator. The ECC system and the HDH system are connected at the condenser for heat exchange.

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01-04-2021 дата публикации

SYSTEM AND METHOD FOR MULTI-FUNCTIONAL SLURRY PROCESSING

Номер: US20210094842A1
Принадлежит: Sedron Technologies, LLC

A multi-functional slurry processing system (“VARCOR”) and associated methods is disclosed. The present examples provide a multi-functional slurry processing system incorporating systems and methods for separating liquid and solid components in slurries. In particular the systems and methods described herein produce clean water, dried solids, and potential concentration of desirable constituents with a boiling point lower than water. At least one example of the multi-functional slurry processing system provides a self-contained processing facility configured to efficiently convert high water-content slurries into its constituent solid and liquid fractions and subsequently generating and collecting clean water and concentrating desirable constituents with a boiling point lower than water. The multi-functional slurry processing system advantageously applies thermodynamic principles in a system which may include various combinations of a preheater, a degassing unit, a dryer, a steam filter, a compressor, a concentrating tower, and a condensation unit. 1a pre-heater comprised of at least a cold side configured to receive wet slurry on the cold side, and a hot side, wherein heat from the hot side can pass to the cold side;a degassing sub-assembly configured to receive wet slurry from the pre-heater; 'one or more drying discs that are substantially cylindrical with a shaft running through a center thereof, wherein each of the one or more drying discs is at least partially hollow and contains one or more disc condensate tubes and one or more disc condensate scoops configured to output the dryer condensates; and', 'a dryer comprised of at least a cold side configured to receive slurry from the degassing sub-assembly and output slurry vapor and dried solids, and a hot side configured to receive pressurized slurry vapor and output concentrated slurry vapor and dryer condensates, the hot side includinga compressor configured to receive slurry vapor and output pressurized ...

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01-04-2021 дата публикации

Process and plant for separation of a hydrocarbon mixture

Номер: US20210094895A1
Принадлежит:

The invention relates to a process for separating a component mixture (K) comprising hydrogen, methane, hydrocarbons having two carbon atoms and hydrocarbons having three or more carbon atoms, wherein in a deethanization at least a portion of the component mixture (K) is subjected to a first partial condensation by cooling from a first temperature level to a second temperature level at a first pressure level to obtain a first gas fraction (G) and a first liquid fraction (C), at least a portion of the first gas fraction (G) is subjected to a second partial condensation by cooling from the second temperature level to a third temperature level at the first pressure level to obtain a second gas fraction (G) and a second liquid fraction (C), and at least a portion of the first liquid fraction (C) and at least a portion of the second liquid fraction (C) are subjected to a rectification to obtain a third gas fraction (G) and a third liquid fraction (C). The first liquid fraction (C) or its part subjected to the rectification and the second liquid fraction (C) or its part subjected to the rectification are expanded to a second pressure level and the rectification is carried out at the second pressure level, the first pressure level being 25 to 35 bar and the second pressure level being 14 to 17 bar. An overhead gas formed during the rectification is cooled to −25 to −35° C. and partially condensed, wherein a condensed portion of the overhead gas is used partially or completely as a reflux in the rectification and an uncondensed portion of the overhead gas is provided partially or completely as the third gas fraction (G). The present invention likewise provides a corresponding plant (). 1. Process for separating a component mixture (K) comprising hydrogen , methane , hydrocarbons having two carbon atoms and hydrocarbons having three or more carbon atoms , comprising a deethanization and a demethanization subsequent to the deethanization , wherein{'b': 1', '1, 'in the ...

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05-04-2018 дата публикации

Reactor Systems and Processes Related Thereto

Номер: US20180094083A1
Автор: Paul J. Clymans
Принадлежит: ExxonMobil Chemical Patents Inc

A process for separating components of a reactor off gas is provided. A related reactor system is also provided. The reactor system may include a high pressure tubular reactor and/or an autoclave reactor and may be used for the production polyolefin polymers.

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26-03-2020 дата публикации

METHOD AND APPARATUS FOR TREATING WATER

Номер: US20200095136A1
Автор: Ellis, JR. John C.
Принадлежит:

A method and apparatus for treating water that results in water having a hydrogen bond angle of greater than 110°, preferably in a range of about 113° to about 114°. The method includes: channeling the water into a receptacle; devolatilizing and deaerating the water in the receptacle by using a condensing channel immersed in the water contained in the receptacle; channeling a portion of the water from the receptacle to a boiler via a feeder channel; heating the water in the boiler to generate steam; providing ozone to the steam in the boiler; and channeling the steam into the condensing channel. The apparatus includes a closed receptacle, a condensing channel housed in the receptacle, and a boiler in fluid communication with the receptacle. The boiler includes a boiler housing, an ozone generator and at least one heater having a total power of about 1500 watts. 1. A method for treating water comprising:channeling the water into a receptacle;devolatilizing and deaerating the water in the receptacle by using a condensing channel immersed in the water contained in the receptacle;channeling a portion of the water from the receptacle to a boiler via a feeder channel, wherein the boiler comprises a boiler housing and one or two heaters housed in the boiler housing, wherein the boiler housing has an outer diameter of about 6.25 inches and two substantially flat and parallel surfaces that are about 2.375 inches apart;heating the water in the boiler to generate steam;providing ozone to the steam in the boiler;channeling the steam into the condensing channel immersed in the water contained in the receptacle; andflowing the water out of the condensing channel such that the water flowing out of the condensing channel has a hydrogen bond angle of greater than 110°.2. The method according to claim 1 , wherein a predetermined level of the water contained in the receptacle is maintained such that a temperature of the water in the receptacle is in a range of about 180° F. to about ...

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02-06-2022 дата публикации

ENERGY-SAVING PROCESS SYSTEM FOR PURIFYING AND RECYCLING OXYGEN FROM HIGH-TEMPERATURE OXYGEN-ENRICHED FLUE GAS AND PROCESS THEREOF

Номер: US20220168683A1
Принадлежит:

The disclosure discloses an energy-saving system for purifying and recycling oxygen from high-temperature oxygen-enriched flue gas, including a water washing mechanism for introducing high-temperature oxygen-enriched flue gas, a compressor set connected with the water washing system through a pipeline, a compressor outlet heat exchanger connected with the compressor set through a pipeline, a gas-liquid separation tank connected with the compressor outlet heat exchanger through a pipeline, a temperature swing adsorption isobaric drying mechanism and a pressure swing adsorption purification mechanism connected with the gas-liquid separation tank through pipelines, a dedusting and filtering mechanism for introducing gas treated by the temperature swing adsorption isobaric drying mechanism and the pressure swing adsorption purification mechanism, and a cooling mechanism for cooling the water washing mechanism and the compressor outlet heat exchanger. 112232454634454624546446. An energy-saving system for purifying and recycling oxygen from high-temperature oxygen-enriched flue gas , comprising a water washing mechanism for introducing the high-temperature oxygen-enriched flue gas , a compressor set () connected with the water washing system through a pipeline , a compressor outlet heat exchanger () connected with the compressor set () through a pipeline , a gas-liquid separation tank () connected with the compressor outlet heat exchanger () through a pipeline , a temperature swing adsorption isobaric drying mechanism () and a pressure swing adsorption purification mechanism () connected with the gas-liquid separation tank () through pipelines , a dedusting and filtering mechanism () for introducing gas treated by the temperature swing adsorption isobaric drying mechanism () and the pressure swing adsorption purification mechanism () , and a cooling mechanism for cooling the water washing mechanism and the compressor outlet heat exchanger () , wherein an output end of the ...

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02-04-2020 дата публикации

SUPERHYDROPHOBIC COATED MICRO-POROUS CARBON FOAM MEMBRANE AND METHOD FOR SOLAR-THERMAL DRIVEN DESALINATION

Номер: US20200101420A1
Принадлежит:

A solar membrane distillation apparatus includes a housing comprising a light transmitting wall. A solar distillation membrane is positioned in the housing to receive solar radiation transmitted through the light transmitting wall. The solar distillation membrane includes a porous graphitic foam and a coating of a hydrophobic composition on the surface and pores of the graphitic foam. A water chamber within the housing is provided for retaining water adjacent to the solar distillation membrane. A vapor chamber is provided for collecting water vapor distilling through the solar distillation membrane. A condenser is provided for condensing distilled water vapor from the vapor chamber into liquid water. A separation membrane and a method of solar distillation are also disclosed. 1. A solar membrane distillation apparatus , comprising:a housing comprising a light transmitting wall;a solar distillation membrane positioned in the housing to receive solar radiation transmitted through the light transmitting wall, the solar distillation membrane comprising a porous graphitic foam and a coating of a hydrophobic composition on the surface and pores of the graphitic foam;a water chamber within the housing for retaining water adjacent to the solar distillation membrane;a vapor chamber for collecting water vapor distilling through the solar distillation membrane;a condenser for condensing distilled water vapor from the vapor chamber into liquid water.2. The solar membrane distillation apparatus of claim 1 , wherein the membrane surface is superhydrophobic.3. The solar membrane distillation apparatus of claim 1 , wherein the solar distillation membrane is tubular and has an open interior claim 1 , the open interior of the tubular distillation membrane forming the water chamber.4. The solar membrane distillation apparatus of claim 3 , wherein the condenser comprises a feed water heat exchange conduit for receiving feed water and exchanging heat with the water vapor to condense the ...

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11-04-2019 дата публикации

Nested Bubbling Apparatus

Номер: US20190105616A1
Принадлежит: Individual

A device for bubbling a gas into a liquid is disclosed. The device comprises a first bubbling apparatus nested inside a second bubbling apparatus. The first bubbling apparatus comprises a gas inlet for receiving the gas and a plurality of first openings for releasing the gas. The second bubbling apparatus at least partially encloses the plurality of first openings of the first bubbling apparatus. The second bubbling apparatus receives the gas from the plurality of first openings. The second bubbling apparatus comprises a plurality of second openings for bubbling the gas into the liquid.

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25-08-2022 дата публикации

SEPARATING METHOD FOR ALTERNATIVE GAS MIXTURES FOR USE AS INSULATING MEDIA

Номер: US20220266190A1
Принадлежит: DILO ARMATUREN UND ANLAGEN GMBH

A method is disclosed for recovering a useful gas from a gas mixture including a useful gas and at least one secondary gas. The gas mixture is first compressed and transferred into a pressure vessel where cooling occurs. Then, from the pressure vessel, a secondary-gas containing gas phase is removed and condensed useful gas is transferred into a purification vessel. In the purification vessel, the condensed useful gas is then purified. A plant is disclosed for recovering a useful gas from a gas mixture. Finally, the use of a plant for carrying out a method for recovering a useful gas from a gas mixture is disclosed. 1. A method for recovering a usage gas from a gas mixture consisting of a usage gas and at least one secondary gas , comprising at least the steps:A) compression of the gas mixture in a compressor,B) transfer of the compressed gas mixture into a pressure vessel,C) cooling of the compressed gas mixture in the pressure vessel until the usage gas goes over into the liquid phase and a gas phase containing secondary gas remains, with the pressure in the pressure vessel being set so that it is at least twice as high as the vapor pressure of the usage gas at the prevailing temperature in the pressure vessel and the pressure in the pressure vessel is at least 5% lower than the vapor pressure of the secondary gas at the prevailing temperature in the pressure vessel,D) removal of the gas phase containing secondary gas from the pressure vessel,E) transfer of the liquefied usage gas from the pressure vessel into a purification vessel,F) heating of the liquefied usage gas in the purification vessel,G) extraction of the gas phase from the purification vessel until the internal pressure in the purification vessel corresponds to the vapor pressure of the usage gas at the prevailing temperature in the purification vessel.2. The method as claimed in claim 1 , wherein the transfer B) of the gas mixture into the pressure vessel is carried out periodically and a ...

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14-05-2015 дата публикации

SYSTEMS INCLUDING A CONDENSING APPARATUS SUCH AS A BUBBLE COLUMN CONDENSER

Номер: US20150129410A1
Принадлежит: Gradiant Corporation

Condensing apparatuses and their use in various heat and mass exchange systems are generally described. The condensing apparatuses, such as bubble column condensers, may employ a heat exchanger positioned external to the condensing vessel to remove heat from a bubble column condenser outlet stream to produce a heat exchanger outlet stream. In certain cases, the condensing apparatus may also include a cooling device positioned external to the vessel configured and positioned to remove heat from the heat exchanger outlet stream to produce a cooling device outlet stream. The condensing apparatus may be configured to include various internal features, such as a vapor distribution region and/or a plurality of liquid flow control weirs and/or chambers within the apparatus having an aspect ratio of at least 1.5. A condensing apparatus may be coupled with a humidifier to form part of a desalination system, in certain cases. 176-. (canceled)77. A condenser system , comprising:a bubble column condenser, comprising: a vessel comprising an inlet in fluid communication with a source of a gas comprising a condensable fluid in vapor phase, and an outlet; wherein the vessel contains a liquid layer comprising an amount of the condensable fluid and the bubble column condenser is configured to remove at least a portion of the condensable fluid from the gas to produce a bubble column condenser outlet stream comprising the condensable fluid in liquid phase; anda heat exchanger positioned external to the vessel and fluidically connected to the vessel to receive the bubble column condenser outlet stream and to remove heat from the bubble column condenser outlet stream to produce a heat exchanger outlet stream.78. The condenser system of claim 77 , wherein the bubble column condenser is a multi-stage bubble column condenser.79. The condenser system of claim 78 , wherein the bubble column condenser comprises a first stage comprising a first stage inlet and a first stage outlet claim 78 , ...

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25-04-2019 дата публикации

SOLVENT DECONTAMINATION SYSTEM AND METHOD

Номер: US20190119127A1
Принадлежит:

A system and method for decontaminating a fluid like a non-azeotrope solvent such as water, wherein a transport gas is maintained at a temperature between the freezing point and boiling point at atmospheric pressure of the solvent and continuously circulated between an evaporation chamber and a condensation chamber, a contaminated solvent is introduced into the transport gas in the evaporation chamber under process heat and contaminant precipitates out, and the cleaned solvent cools in the condensation chamber releasing heat to be used in the evaporation chamber. A heat pump is used to promote evaporation and condensation within the system. 120-. (canceled)21. A system for at least partial decontamination of a contaminated fluid to produce a purified fluid , the system comprising:a process fluid container that separately contains the contaminated fluid and the purified fluid;an evaporation chamber that at least partially evaporates the contaminated fluid to form an evaporated fluid;a condensation chamber that condenses the purified fluid;the evaporation chamber and the condensation chamber in fluid communication;the evaporation chamber and the condensation chamber retains a transport gas for transporting the evaporated fluid to the condensation chamber, the transport gas becoming at least partially saturated with the evaporated fluid in the evaporation chamber, the transport gas releasing the purified fluid in the condensation chamber;an inlet for introducing the contaminated fluid to the evaporation chamber;a purified fluid outlet for withdrawing the purified fluid from the condensation chamber;a pump that supplies, from the process fluid container, a process fluid in the form of either the contaminated fluid or the purified fluid to cool the transport gas to promote condensation in the condensation chamber; anda heat exchanger;wherein the process fluid passes through the heat exchanger to remove heat from the process fluid to form a cooled process fluid, and the ...

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25-04-2019 дата публикации

Method and System for Treating Wastewater

Номер: US20190119130A1
Принадлежит: Eureka Resources, LLC

Methods and systems for treating brine to produce distilled water and dried NaCl are disclosed. The brine enters a crystallization plant and is heated. Once heated, the brine is circulated to an evaporator. The evaporator increases the concentration of NaCl in the brine to a point about the super saturation level. Once above the super saturation level, NaCl crystals are formed. The larger crystals are circulated to a centrifuge for drying and the smaller crystals are recirculated through the evaporator for continued growth. The NaCl crystals are dried in the centrifuge. 1. A system for treating wastewater comprising:a wastewater input line for receiving wastewater comprising a concentration of total dissolved solids (“TDS”) that is greater than 150,000 mg/L:a pretreatment system configured to pretreat the wastewater from the wastewater input line to produce a pretreated wastewater suitable for crystallization/evaporation;{'sub': '2', 'an evaporation/crystallization unit configured to produce, from the pretreated wastewater, a distilled water, a concentrated brine comprising CaCl, and a salt slurry comprising NaCl;'}a purification system configured to receive a first portion of the distilled water from the evaporation/crystallization unit and remove contaminants therefrom to produce a purified water; anda post-treatment system comprising at least one of an ion exchange system and a reverse osmosis system, the post-treatment system configured to convert the purified water from the purification system into a de-wasted water.2. A system according to claim 1 , further comprising a centrifuge configured to:receive the salt slurry produced by the evaporation/crystallization unit; anddewater the salt slurry to produce a centrate/filtrate and a sodium chloride product comprising NaCl crystals.3. A system according to claim 2 , further comprising a circulation line connected to the centrifuge and the evaporation/crystallization unit claim 2 , the circulation line configured ...

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10-05-2018 дата публикации

A MODULAR APPARATUS FOR WATER PRODUCTION

Номер: US20180127955A1

A modular apparatus () for water production from atmospheric air comprises: a first parallelepiped module () provided with an inlet opening () for moist air, an outlet opening () of the dehumidified air, a ventilator (), configured such as to force an air flow to cross an internal volume of the first module () from the inlet opening () to the outlet opening (), a condensation unit (), located internally of the first module () so as to intercept the air flow, and a collecting tub () located inferiorly of the condensation unit () for collecting the condensation water that is separating from the air flow; and a second parallelepiped module () in which a refrigerating unit () is contained provided with at least a portion of a refrigerating circuit () in which a refrigerating fluid circulates and an evaporator in which the refrigerating liquid evaporates so as to cool the air flow internally of the condensation unit (); where the first module () and the second module () are fixed to one another at a respective interconnecting fact and where the second module () exhibits a side of the interconnecting face having a width (W) equal to twice a width (W/2) of a side of the interconnecting face of the first module (). 110. A modular apparatus () for water production from atmospheric air which comprises:{'b': 200', '21', '22', '23', '200', '21', '22', '20', '200', '291', '292', '293', '20, 'a first parallelepiped module () provided with an inlet opening () for moist air, an outlet opening () of the dehumidified air, a ventilator (), configured such as to force an air flow to cross an internal volume of the first module () from the inlet opening () to the outlet opening (), a condensation unit (), located internally of the first module () so as to intercept the air flow, and a collecting tub (, , ) located inferiorly of the condensation unit () for collecting condensation water that is separating from the air flow; and'}{'b': 300', '30', '31', '200', '20, 'a second ...

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23-04-2020 дата публикации

SEPARATION SYSTEM AND METHOD THEREOF

Номер: US20200122054A1
Автор: STANTCHEV GEORGE
Принадлежит:

A separation system for separating constituents from a solution by utilizing a carrier gas and a separation method thereof are disclosed. The separation system includes an evaporator, a solution distribution unit connected to the evaporator for distributing the solution into the evaporator, and a gas distribution unit connected to the evaporator for distributing the carrier gas into the evaporator. The solution is countercurrent to the carrier gas and upon contact, at least one constituent of the solution is vaporized and separated from the solution. 1. A separation system for separating constituents from a solution by utilizing a carrier gas , the separation system comprising:an evaporator;a solution distribution unit fluidly connected to the evaporator for distributing the solution into the evaporator; anda gas distribution unit fluidly connected to the evaporator for distributing the carrier gas into the evaporator;wherein a flow of the solution is in countercurrent to a flow of the carrier gas and upon contact, at least one constituent of the solution is vaporized and separated from the solution.2. The separation system of claim 1 , further comprising:a solution collection vessel fluidly connected to the evaporator for collecting the solution remaining in the evaporator; andat least one condensation unit connected in series to the evaporator for condensing the at least one vaporized constituent.3. The separation system of claim 2 , wherein each of the at least one condensation unit comprises:a condenser fluidly connected to the evaporator or a previous condensation unit, wherein the condenser receives the carrier gas containing the at least one vaporized constituent from the evaporator or the previous condensation unit and condenses at least one of the at least one vaporized constituent contained in the carrier gas; anda collection unit fluidly connected to the condenser, wherein the collection unit collects the at least one condensed constituent and discharges ...

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03-06-2021 дата публикации

METHODS FOR BIOLOGICAL PROCESSING OF HYDROCARBON-CONTAINING SUBSTANCES AND SYSTEM FOR REALIZATION THEREOF

Номер: US20210163825A1
Автор: Finney Jerry Wayne
Принадлежит:

The present disclosure is related to systems and methods for the biological processing of hydrocarbon-containing substances. In particular embodiments, the systems and methods herein relate to pre-digestion of hydrocarbon containing substances and further processing of the same to produce hydrocarbon fuels, fertilizer, and other products. 1. A method for transforming waste into hydrocarbon fuels comprising:{'i': 'Bacillus firmus', 'creating a predigested coal slurry by mixing coal fines, water, urea, a culture of bacteria and a dispersant agent in a pre-digestion tank;'}transferring the predigested coal slurry to a vacuum digester, including a first burner lance;heating the predigested coal slurry via the first burner lance, producing combustion gases and first naphtha vapors;condensing and storing the first naphtha vapors;heating the combustion gases via a second burner lance in an atmospheric digester, producing second naphtha vapors; andcondensing and storing the second naphtha vapors.2. The method of claim 1 , wherein:heating the predigested coal slurry further produces first creosote solids; andthe method further comprises transporting the first creosote solids to a chemical tote bin.3. The method of claim 2 , wherein the method further comprises creating a creosote mixture by mixing the first creosote with water claim 2 , bacteria claim 2 , and urea.4. The method of claim 3 , wherein the method further comprises stirring the creosote mixture at regular intervals for at least a week to produce fertilizer.5. The method of claim 4 , wherein:the combustion gases are first combustion gases; andheating the first combustion gases via the second burner lance produces second combustion gases; andthe method further comprises transporting the second combustion gases to at least one scrubber tank for scrubbing the second combustion gases.6. The method of claim 5 , wherein:the at least one scrubber tank produces scrubber water comprising electrolytes; andthe method further ...

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10-06-2021 дата публикации

Pressurized Vapor Cycle Liquid Distillation

Номер: US20210170299A1
Принадлежит: Deka Products LP

Embodiments of the invention are directed toward a novel pressurized vapor cycle for distilling liquids. In some embodiments of the invention, a liquid purification system is revealed, including the elements of an input for receiving untreated liquid, a vaporizer coupled to the input for transforming the liquid to vapor, a head chamber for collecting the vapor, a vapor pump with an internal drive shaft and an eccentric rotor with a rotatable housing for compressing vapor, and a condenser in communication with the vapor pump for transforming the compressed vapor into a distilled product. Other embodiments of the invention are directed toward heat management, and other process enhancements for making the system especially efficient.

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16-05-2019 дата публикации

MANUFACTURING SYSTEM OF ELECTRONIC-GRADE AMMONIA SOLUTION

Номер: US20190144292A1
Принадлежит:

A manufacturing system of an electronic-grade ammonia solution comprises: a mixing tank to mix an unsaturated ammonia aqueous solution and alkali to obtain a mixing solution; a stripping unit, disposes downstream the mixing tank and comprises a heat exchanger to heat the mixing solution, and a stripping column to mix a nitrogen gas and the heated mixing solution to obtain a mixing gas; a first absorption unit, disposes downstream the stripping unit and comprises a first condensation unit to cool down the mixing gas, and a first absorption column to mix a saturated ammonia aqueous solution and the cooled mixing gas to obtain a purge gas; and a second absorption unit, disposes downstream the first absorption unit and comprises a second condensation unit to cool down a DI water, and a second absorption column to mix the cooled DI water and the purge gas to obtain electronic-grade ammonia solution. 1. A manufacturing system of an electronic-grade ammonia solution , comprisinga mixing tank used to mix an ammonia solution and an alkali to form a mixing solution, wherein the ammonia solution is an unsaturated solution;a stripping unit disposed in a downstream of the mixing tank and including a heat exchanger and a stripping column, wherein the heat exchanger is used to heat the mixing solution, and wherein the stripping column is used to mix nitrogen and the heated mixing solution and undertake stripping to obtain a mixing gas;a first absorption unit disposed in a downstream of the stripping unit and including a first condensation unit and a first absorption column, wherein the first condensation unit is used to cool down the mixing gas, and wherein the first absorption column is used to mix saturated ammonia solution and the cooled mixing gas and undertake absorption to obtain a purge gas; anda second absorption unit disposed in a downstream of the first absorption unit and including a second condensation unit and a second absorption column, wherein the second ...

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16-05-2019 дата публикации

METHOD OF PREPARING BUTADIENE

Номер: US20190144361A1
Принадлежит: LG CHEM, LTD.

A method of preparing butadiene and a device for preparing the same. The method includes passing reaction raw materials containing butene, oxygen, steam, and a diluent gas through an oxidative dehydrogenation reactor, and oxidative dehydrogenation is performed therein to produce a reaction product separating water from the reaction product condensing hydrocarbons to produce a crude hydrocarbon mixture; and separating butadiene from the crude hydrocarbon mixture, where a gas containing n-butane remaining after the butadiene is separated is fed into the oxidative dehydrogenation reactor, and butane is used as a diluent gas. Because butane is used as a diluent gas, a C4 mixture and gas products may be easily separated through cooling and condensation processes. Thus, the method may increase productivity while reducing energy consumption and raw material costs, thereby improving economic efficiency. 1. A method of preparing butadiene , comprising:{'sub': '2', 'passing reaction raw materials containing butene, oxygen (O), steam, and a diluent gas through an oxidative dehydrogenation reactor, and oxidative dehydrogenation is performed therein to produce a reaction product comprising a butadiene-containing C4 mixture, gas products and water;'}separating the water from the butadiene-containing C4 mixture and gas products by passing the reaction product through a cooling separator;passing the butadiene-containing C4 mixture and the gas products, from which water has been separated, through a condenser to condense hydrocarbons to produce a crude hydrocarbon mixture comprising n-butane, butene, and butadiene; andseparating the butadiene from the crude hydrocarbon mixture by passing the crude hydrocarbon mixture through a purification apparatus,wherein a gas containing n-butane remaining after the butadiene is separated in the purification apparatus is fed into the oxidative dehydrogenation reactor, and the diluent gas is butane.2. The method according to claim 1 , wherein the ...

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08-06-2017 дата публикации

Humidification System with Pressure Condensate Return and Method Therefor

Номер: US20170157527A1
Автор: KOPEL Zev W., LANDRY ÉRIC
Принадлежит: National Environmental Products, Ltd.

Supplied humidification steam is dispersed through tubes and a header. Condensate is collected from the header into a tank. A controlled steam supply valve pumps condensate from the tank to a return line by application of sourced steam. A non-mechanical electronic level sensor (ELS, sensing temperature, resistance, capacitance, inductance, luminance or sonic condition of condensate) signals a controller using the ELS and/or a timed pumping/evacuation cycle to push condensate from the tank to the return. The method removes condensate by isolating the collection tank from the tubes and header and pumps condensate from the tank based upon a sensed conditions. 1. A steam dispersion apparatus supplied with steam from a steam source comprising:a plurality of steam dispersion tubes coupled to a header in communication with said steam source;a condensate collection tank in communication with said header configured to collect condensate therefrom;an electronic sensor sensing the level of condensate in said collection tank; anda controlled steam supply valve pumping condensate from said collection tank based upon the level of condensate detected by said sensor.2. A steam dispersion apparatus as claimed in wherein said electronic sensor is a non-mechanical electronic level sensor sensing the condensate level.3. A steam dispersion apparatus as claimed in wherein said electronic sensor senses one of a gas-liquid differential of temperature claim 1 , resistance claim 1 , capacitance claim 1 , inductance claim 1 , luminance or sonic condition of condensate in the collection tank.4. A steam dispersion apparatus as claimed in wherein said electronic sensor employs one of a temperature claim 1 , resistance claim 1 , capacitance claim 1 , inductance claim 1 , luminance or sonic condition of the condensate in the collection tank.5. A steam dispersion apparatus as claimed in wherein the steam dispersion apparatus is part of a steam dispersion system claim 4 , the steam dispersion ...

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30-05-2019 дата публикации

Systems and Methods for Aromatic Alkylation

Номер: US20190161420A1
Принадлежит:

Methods and related systems are disclosed for condensing a minor portion of an effluent stream from an alkylation reactor by contacting the effluent stream with a first liquid hydrocarbon quench stream and a second liquid hydrocarbon quench stream. The effluent stream includes catalyst fines from the reactor, and at least a portion of the catalyst fines are carried with the condensed minor portion of the effluent stream. 1. A process , comprising:(a) reacting an aromatic feedstock comprising benzene with methanol under alkylation conditions in a reactor in the presence of a fluidized bed of solid catalyst particles to produce a vapor phase effluent comprising toluene, xylenes, water, unreacted benzene and solid catalyst fines;(b) contacting the vapor phase effluent with a first liquid phase hydrocarbon quench stream to produce a mixture having a higher dew point than the vapor phase effluent;(c) contacting the mixture with a second liquid phase hydrocarbon quench stream after (b) under conditions to condense a minor portion of the mixture and produce a condensate which contains at least some of the catalyst fines and which is substantially free of an aqueous phase; and(d) separating at least a portion of the condensate containing said fines from the remainder of the mixture.2. The process of claim 1 , further comprising:(e) flowing the condensate to a separation unit;(f) separating the first liquid phase hydrocarbon quench stream from the condensate in the separation unit; and(g) recycling the first liquid phase hydrocarbon quench stream to the contacting in (b).3. The process of claim 2 , wherein the separation unit is a divided wall column including a divided wall claim 2 , and wherein the first liquid phase hydrocarbon phase quench stream is emitted from the separation divided wall column on an opposing side of the dividing wall from where the condensate flows into the divided wall column at (g).4. The process of claim 1 , wherein the contacting in (c) occurs ...

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29-09-2022 дата публикации

METHOD FOR PRODUCING MAGNESIUM-LITHIUM ALLOY BY GASEOUS CO-CONDENSATION METHOD

Номер: US20220307108A1
Принадлежит:

The present invention belongs to the technical field of preparation of light metal alloy materials, in particular to a method for producing a magnesium-lithium alloy by a gaseous co-condensation method. The method comprises the steps of: 1) mixing and briquetting a lithium salt, a refractory agent and a catalyst under pressure, and then thermally decomposing to form an unsaturated composite oxide; 2) respectively crushing and ball-milling, and then briquetting the unsaturated composite oxide, magnesium oxide, a reducing agent and a fluxing agent; 3) reducing briquettes in vacuum; 4) making a gas pass through a first condensing chamber of a temperature control device, and then purifying; 5) The purified metal gas is condensed into the condensing phase of the alloy through the second condensing chamber of a quenching device; 6) obtaining the magnesium-lithium alloy with a purity being 99.5% or above by virtue of smelting and flux-refining, and then purifying by distillation. The magnesium-lithium alloy obtained in the present application is not segregated, so that a stable β-phase solid solution or a compound having an increasing purity being 99.95% is formed. 1. A method for producing a magnesium-lithium alloy by a gaseous co-condensation method , comprising the following steps:1) The lithium salt, the refractory agent and catalyst are mixed in proportion and briqueted under pressure, wherein a briquetted mixture is charged into an industrial tube furnace for thermal decomposition, an unsaturated composite oxide is generated by lithium oxide and the refractory agent, and the sublimated and condensed catalyst is recycled;2) respectively crushing and ball-milling the unsaturated composite oxide generated in step 1), magnesium oxide, the reducing agent and a fluxing agent, and then briquetting;3) charging briquettes in step 2) into an industrial heat-resistant tube furnace for vacuum reduction, at this time, the reduction product is in the gaseous state and carries ...

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21-05-2020 дата публикации

Wind-driven Air-Compressed Energy-Saving Collecting and Filtering Device for Field Fresh water

Номер: US20200157783A1
Автор: YAU Chun Ho
Принадлежит:

The invention relates to a wind-driven air-compressed energy-saving collecting and filtering device for field fresh water which includes a water collecting tank, a cooling pipe, a compression pipe and a wind wheel. The water collecting tank is provided with a pressure relief pipe, an outlet pipe and a plug. The outer side of the cooling pipe is provided with an ultraviolet sterilizer. The inner cavity of the cooling pipe is provided with a fin condenser. The upper end of the compression pipe is connected to an end cover, a second annular housing, a power generating coil disposed in the inner cavity of the second annular housing. The end cover is provided with a commutator. The inner cavity of the compression pipe is provided with a first rotating shaft, magnetic compression blades, and a limiting mesh plate. The wind wheel includes a bracket and Y-shaped blades. The wind-driven air-compressed energy-saving collecting and filtering device for field fresh water of the present invention has reasonable and simple structure, convenient to use, low cost, convenient to install, energy saving and environment friendly which effectively solve the problem of lack of fresh water in specific areas such as deserts and islands. 112451245111112111511. A wind-driven air-compressed energy-saving collecting and filtering device for field fresh water , comprising: a water collecting tank , a cooling pipe , a compression pipe and a wind wheel , wherein the water collecting tank and the cooling pipe are arranged under the ground surface , and the compression pipe and the wind wheel are arranged on the ground surface; the water collecting tank is provided with a pressure relief pipe communicated with the ground surface and the inner cavity of the water collecting tank ; an outlet pipe is provided in the inner cavity of the pressure relief pipe , and a plug is arranged on the port at one end of the pressure relief pipe located at the ground surface ,{'b': 2', '1', '2', '1', '2', '1', '2', ...

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21-06-2018 дата публикации

PORTABLE DEVICE FOR PRODUCING DRINKING WATER FROM ATMOSPHERIC MOISTURE

Номер: US20180171603A1
Принадлежит:

The present invention relates to a portable device for generating drinking water from atmospheric moisture and in particular relates to a portable device powered by means of renewable energy sources. 1. Device for the production of drinking water from the moisture contained in an atmospheric air flow , comprising:—an evaporator;—a refrigeration unit for the production of a refrigerant liquid which is circulated in said evaporator;—blowing means for forcedly conveying an atmospheric air flow towards said evaporator;—a tank for collecting the water obtained by the condensation of the moisture contained in said air for effect of the heat exchange between said air flow and said refrigerant liquid realized in said evaporator;—electric power supply means;—control means adapted at least to measure the external atmospheric temperature; said device further comprising deviation means for deviating selectively the refrigerated air exiting from said evaporator towards said refrigeration unit or towards said tank according to the value of the external atmospheric temperature measured by said control means , so that when the atmospheric temperature is lower than a given threshold value said air is directed towards said tank , whereas if said atmospheric temperature is higher than said threshold value said air is directed towards said refrigeration unit.2. The device according to claim 1 , wherein said evaporator is housed in a first compartment of said device claim 1 , said refrigeration unit and said tank being housed respectively in a second compartment and third compartment of said device claim 1 , said first compartment communicating with said second and third compartments by means of a branched duct claim 1 , said deviation means being operatively housed inside said duct.3. The device according to claim 2 , wherein said deviation means comprise a mobile partition moved to close or open one or other branch of said duct so as to convey said air flow towards the second ...

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28-05-2020 дата публикации

SYSTEM AND METHOD FOR SUSTAINABLE GENERATION OF ENERGY

Номер: US20200166010A1
Принадлежит:

A system for sustainable generation of energy, comprising at least one device for converting natural power into useful energy, and at least one internal combustion engine or heat engine. The internal combustion engine or heat engine may be connected to a gas cleaning device for fuel or heat supply. A method for sustainable generation of energy, comprising the steps of generating a first amount of useful energy by converting natural power; and generating a second amount of energy by operating at least one internal combustion engine or heat engine, wherein the internal combustion engine or heat engine is driven by fuel or heat derived from cleaning a waste gas. 1. A system for sustainable generation of energy , comprising:at least one device for converting natural power into useful energy, andat least one internal combustion engine or heat engine,wherein the internal combustion engine or heat engine is connected to a gas cleaning device for fuel or heat supply.2. The system according to claim 1 , wherein the gas cleaning device comprises a multi-stage condenser arrangement.3. The system according to claim 1 , wherein the at least one natural power conversion device is selected from the list consisting of solar power converters claim 1 , wind turbines claim 1 , hydro-turbines claim 1 , wave power converters claim 1 , geothermal heat pumps and tidal energy converters.4. The system according to claim 1 , wherein the at least one device for converting natural power into useful energy converts waste heat from industry or households into useful energy.5. The system according to claim 1 , further comprising means for storing generated energy.6. The system according to claim 5 , wherein the energy storage means is selected from the list consisting of gravitational energy storage means claim 5 , pneumatic energy storage means claim 5 , kinetic energy storage means and chemical energy storage means.7. The system according to claim 5 , wherein the energy storage means comprises ...

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30-06-2016 дата публикации

Atomizing separation method and atomizing separation device

Номер: US20160184738A1
Автор: Kazuo Matsuura
Принадлежит: NANOMIST TECHNOLOGIES Co Ltd

A method for separating at least one of components with different vapor pressures from a solution that includes the components by atomizing the solution. The method includes an atomization step, and a separation step. A solution L is atomized into mist in air whereby producing mist-mixed air in the atomization step. Droplets of the mist included in the mist-mixed air are classified according to their particle diameter sizes, and exhaust air that contains air as carrier gas is exhausted in the separation step. In the atomizing separation method, the heat energy of both of the latent heat and sensible heat that are included in the exhaust air exhausted in the separation step are collected, and one or both of the solution L to be atomized in the atomization step and air to be blown toward the solution L are heated by the collected heat.

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08-07-2021 дата публикации

PRODUCTION OF PURIFIED DIALKYL-FURAN-2,5-DICARBOXYLATE (DAFD) IN A RETROFITTED DMT PLANT

Номер: US20210206738A1
Принадлежит: EASTMAN CHEMICAL COMPANY

Disclosed is a process to produce a purified vapor comprising dialkyl-furan-2,5-dicarboxylate (DAFD). Furan-2,5-dicarboxylic acid (FDCA) and an alcohol in an esterification zone to generate a crude diester stream containing dialkyl furan dicarboxylate (DAFD), unreacted alcohol, 5-(alkoxycarbonyl)furan-2-carboxylic acid (ACFC), and alkyl furan-2-carboxylate (AFC). The esterification zone comprises at least one reactor that has been previously used in an DMT process. 1. A process comprising feeding a composition comprising furan-2 ,5-dicarboxylic acid (“FDCA”) in an amount greater than 80 wt % to a process to polymerize said FDCA; wherein said process includes co-locating the two manufacturing facilities , one for oxidation to produce FDCA and one for polymerization of the FDCA to produce a polymer composition comprising a polymer , within 10 miles of each other.2. The process according to claim 1 , wherein said polymer composition comprises PEF (polyethylene furanoate).3. The process according to wherein the polymer composition comprises at least 10% by weight PEF.4. The process according to wherein the polymer composition comprises at least 20% by weight PEF.5. The process according wherein said polymer composition comprises PEF and is produced through polymerization wherein the polymerization occurs in at least one reactor previously used in a PET (polyethylene terephthalate) plant.6. The process according to wherein said co-locating the two manufacturing facilities claim 1 , one for oxidation to produce FDCA and one for polymerization of the FDCA to produce a polymer composition comprising a polymer claim 1 , is within 5 miles of each other.7. The process according to wherein said co-locating the two manufacturing facilities claim 5 , one for oxidation to produce FDCA and one for polymerization of the FDCA to produce a polymer composition comprising a polymer claim 5 , is within 1 mile of each other.8. The process according to wherein said co-locating the two ...

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28-06-2018 дата публикации

PLANT FOR DEALCOHOLISING ALCOHOLIC BEVERAGES

Номер: US20180179480A1
Автор: Kinner Frank, Stoessel Kai
Принадлежит:

A plant for dealcoholising alcoholic beverages includes a rectification column having at least one inlet for the alcoholic beverage, a sump and a top. The rectification column is operable such that dealcoholised beverage can be removed from the sump and exhaust vapour can be removed from the top. At least one evaporator is configured to supply the rectification column with vapour. A condenser arrangement condenses the exhaust vapour removed from the top of the rectification column, at least in part. The plant further includes a heat pump which can operate the evaporator as well as the condenser arrangement. A method for dealcoholising alcoholic beverages in a rectification column is also disclosed. 1. Plant for dealcoholising alcoholic beverages , comprising:a rectification column having at least one inlet for the alcoholic beverage, a sump and a top, the rectification column being operable such that dealcoholised beverage is removable from the sump and exhaust vapour is removable from the top;at least one evaporator which is configured to supply the rectification column with vapour; anda condenser arrangement for condensing the exhaust vapour removed from the top of the rectification column at least in part; and{'b': 27', '127', '30, 'a heat pump which can operate the evaporator (; ) and the condenser arrangement ().'}2. Plant according to claim 1 , further comprising a heating circuit containing a heating medium for heating the evaporator and a cooling circuit containing a cooling medium for cooling the condenser arrangement the heat pump being operable so as to transfer heat from the cooling medium leaving the condenser arrangement to the heating medium leaving the evaporator.3. Plant according to claim 2 , wherein associated with at least one of the heating circuit and the cooling circuit is at least one heat exchanger which can remove heat from the plant.4. Plant according to claim 1 , wherein the heat pump comprises a mechanical exhaust vapour compressor which ...

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13-06-2019 дата публикации

SYSTEM AND A METHOD FOR PRODUCING AQUEOUS SULPHURIC ACID

Номер: US20190177914A1
Принадлежит:

A system () for producing aqueous sulphuric acid. The system () comprises a first heat exchanger () configured to cool water and/or aqueous sulphuric for producing cooled water and/or cooled aqueous sulphuric acid; a pre-cooling unit () configured to pre-cool some gas containing sulphur trioxide, the pre-cooling unit () comprising an inlet or inlets () for receiving [i] the gas containing sulphur trioxide and [ii] the cooled water and/or the cooled aqueous sulphuric acid, an outlet () for letting out aqueous sulphuric acid and the gas containing sulphur trioxide, and a first nozzle () for spraying the cooled water and/or the cooled aqueous sulphuric acid onto the gas containing sulphur trioxide to cool the gas containing sulphur trioxide. The system further comprises a condensation tower () comprising a first inlet () for receiving the cooled gas containing sulphur trioxide and aqueous sulphuric acid from the pre-cooling unit () and means () for circulating the aqueous sulphuric acid within the 116-. (canceled)17100600100. A system () for producing aqueous sulphuric acid from a sulphur dioxide containing gas of a liquor circulation of a pulp mill () , the system () comprising:{'b': '600', 'the pulp mill (), configured to produce at least some gas containing sulphur dioxide;'}{'b': 602', '500', '500, 'claim-text': [{'b': '502', 'an inlet arrangement () for receiving some gas containing at least some sulphur dioxide and some oxygen or some gas containing at least some sulphur dioxide and some other gas comprising oxygen, and'}, {'b': '510', 'catalyst () for converting at least some of the sulphur dioxide and the oxygen to sulphur trioxide,'}], 'a pipeline () configured to convey at least some of the gas containing sulphur dioxide to a converter (), the converter () comprising{'b': 440', '500', '212', '200, 'a pipeline () configured to convey gas containing sulphur trioxide from the converter () to an inlet () of a pre-cooling unit (); and'}{'b': '410', 'a first heat ...

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07-07-2016 дата публикации

Method and System for High-Efficiency Heat Energy Recycling Applicable to Plateau Areas Using a High-Temperature Concentrated Solar Thermal Collector

Номер: US20160193545A1
Принадлежит:

The invention discloses a high efficiency thermal energy recovery method and system, and a high temperature concentrated solar thermal collector. A concentrated solar photo-thermal device is used to heat heat-transfer oil to a high temperature and the oil is used for rapid heat replenishment for decompressing evaporation. Multiple methods are also used to recover thermal energy so as to recover a large part of thermal energy in a production process, thereby enabling the continuous production in plateau areas, reducing the electricity consumption, lowering the capacity of photovoltaic power stations, and reducing the fixed investment. 1. A high-efficiency heat energy recycling method , comprising:(a) utilizing a concentrated solar photo-thermal device to heat heat-transfer oil to more than 120° C. for standby;(b) heating a liquid heat conducting medium in a water tank hot end and bittern in a preheating pool via the solar photo-thermal device, and guiding the preheated bittern into a temperature rising kettle;(c) absorbing heat from the water tank cold end via a high temperature heat pump, releasing heat to the temperature rising kettle via the hot end of the water tank, and heating the bittern in the temperature rising kettle to the temperature required;(d) guiding the bittern in the temperature rising kettle into a reaction kettle, vacuumizing for decompressing concentration, guiding the heated heat-transfer oil into a heat exchanger in the reaction kettle to rapidly and additionally heat the reaction kettle, guiding the vapor produced by decompressing concentration in the reaction kettle into the heat exchanger in the preheating pool for cooling, and collecting the distilled water obtained into a distillate tank;(e) guiding the high temperature supernatant after crystallization in the reaction kettle into a cold end crystallization kettle via a pipeline, performing heat exchange between the water tank cold end and the cold end crystallization kettle via the heat ...

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20-06-2019 дата публикации

Water distilling and purifying unit and variants thereof

Номер: US20190184305A1
Принадлежит: Individual

A method for distilling water includes moving raw water into an evaporator. Water is pumped into a liquid-driven condensing ejector. Water vapor is discharged from a vapor outlet of the evaporator into a gas inlet of the ejector. Fluid from an outlet of the ejector is conducted into a heat exchanger. Heat from fluid conducted from the ejector is transferred in the heat exchanger to the raw water entering the evaporator.

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05-07-2018 дата публикации

Cooling Systems Having An Integrated Ionic Liquid Salt Dehumidification System

Номер: US20180187906A1
Принадлежит: Xergy Inc

A cooling systems utilizes an organic ionic salt composition for dehumidification of an airflow. The organic ionic salt composition absorbs moisture from an inlet airflow to produce an outlet airflow with a reduce moisture from that of the inlet airflow. The organic ionic salt composition may be regenerated, wherein the absorbed moisture is expelled by heating with a heating device. The heating device may be an electrochemical heating device, such as a fuel cell, an electrochemical metal hydride heating device, an electrochemical heat pump or compressor, or a condenser of a refrigerant cycle, which may utilize an electrochemical pump or compressor. The efficiency of the cooling system may be increased by utilization of the waste heat the cooling system. The organic ionic salt composition may circulate back and forth or in a loop between a conditioner, where it absorbs moisture, to a regenerator, where moisture is desorbed by heating.

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29-07-2021 дата публикации

Multi-Stage Bubble-Column Vapor Mixture Condensation

Номер: US20210228998A1
Принадлежит:

A multi-stage bubble-column vapor mixture condenser includes at least a first stage and a second stage. Each stage includes a condenser chamber including a carrier-gas inlet and a carrier-gas outlet and contains a condensing bath. Carrier gas bubbles from the carrier-gas inlet up through the condensing bath, overcoming a hydrostatic head of the condensing bath, to a volume of carrier gas above the condensing bath. The carrier-gas outlet is positioned with an opening for carrier-gas extraction, and the first-stage carrier-gas outlet is in fluid communication with the second-stage carrier-gas inlet to facilitate flow of the carrier gas through the condensing bath in the first-stage condenser chamber, into the volume of carrier gas above the first-stage condensing bath, and then through the condensing bath in the second-stage condenser chamber. The first-stage condenser chamber further includes an intermediate-exchange inlet positioned and configured to inject additional carrier gas into the first-stage condenser. 1. A multi-stage bubble-column vapor mixture condenser , comprising: a condenser chamber including a carrier-gas inlet and a carrier-gas outlet;', 'a condensing bath in the condenser chamber, wherein the carrier-gas inlet is positioned and configured to bubble carrier gas from the carrier-gas inlet up through the condensing bath, overcoming a hydrostatic head of the condensing bath; and', 'a volume of carrier gas above the condensing bath in the condenser chamber, wherein the carrier-gas outlet is positioned with an opening for carrier-gas extraction from the volume of carrier gas above the condensing bath, wherein the first-stage carrier-gas outlet is in fluid communication with the carrier-gas inlet of the second stage to facilitate flow of the carrier gas through the condensing bath in the condenser chamber of the first stage, into the volume of carrier gas above the first-stage condensing bath, and then through the condensing bath in the condenser chamber ...

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20-07-2017 дата публикации

Low Energy Process for purifying water and reducing crop water consumption

Номер: US20170203232A1
Принадлежит: Individual

The low-energy water reclamation process consists of evaporation from water sources, followed by capturing, condensing and reusing the water released into the atmosphere from both the evaporation process and by plant transpiration. 95% to 99% of water from plant transpiration is lost by venting to the atmosphere. We capture that water, and reuse it, to grow food or provide potable water. Reclaiming and reusing the evaporated water reduces both the amount of new water required for plant growth or potable water production, and also reduces the total energy requirement for the process. Over a large growing area, we expect to reclaim a significant amount of transpired water, which will reduce the need for new water to grow food and/or provide pure unpolluted potable water, at lower total cost.

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29-07-2021 дата публикации

Atmospheric Water Generator Utilizing Centrifugal Hydraulic Air Compressor

Номер: US20210230846A1
Автор: Rawls Rocky Lee
Принадлежит:

An atmospheric water generator utilizing centrifugal hydraulic air compressor is for harvesting water from the atmosphere. The purpose of atmospheric water generator utilizing centrifugal hydraulic air compressor is to provide potable water. The atmospheric generator utilizing centrifugal hydraulic air compressor includes a housing having a reservoir, a plurality of centrifugal discs, drive components, water pump, heat exchangers, and air filters. The housing reservoir further includes an indication device to determine the water level in device. The centrifugal discs can utilize centripetal forces to hydraulically compress the air, with water, to harvest the water from the atmosphere. The drive components further comprise a hollow shaft to direct the water to the centrifugal discs. In addition, the shape of the centrifugal disc utilizes the compressed air and water exiting the discs to help rotate the discs. 1) An atmospheric water generator utilizing centrifugal hydraulic air compressor comprising:a hollow frame with panels, drive motor, water pump, liquid-air heat exchanger passage, metal fins, air filters, water nozzle, centrifugal discs, hydraulic chamber, air-water thrust nozzles, hollow shaft, water shroud, wherein the device is configured into a centrifugal hydraulic air compressor that utilizes water to compress air to extract water from the atmosphere.2) The atmospheric water generator utilizing centrifugal hydraulic air compressor of claim 1 , wherein: one or more air filters disposed on the surface to filter incoming air.3) The atmospheric water generator utilizing centrifugal hydraulic air compressor of claim 1 , wherein: one or more centrifugal discs attached to the hollow shaft to hydraulically compress the air.4) The atmospheric water generator utilizing centrifugal hydraulic air compressor of claim 1 , wherein: one or more liquid-air heat exchange devices to exchange heat to the surrounding atmosphere.5) The atmospheric water generator utilizing ...

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12-08-2021 дата публикации

Multistage membrane distillation apparatus

Номер: US20210245105A1
Принадлежит: Evcon GmbH

The invention relates to a multistage membrane distillation apparatus ( 5000 ), comprising a plurality of multistage membrane distillation modules ( 500, 600 ), the modules being configured to be flowed through in parallel by a liquid (F) to be concentrated. Each module comprises a plurality of serial condensation/evaporation stages ( 50, 60 ) configured to be flowed through in series by the liquid to be concentrated. Each condensation/evaporation stage comprises a plurality of parallel condensation/evaporation elements ( 101, 102 ) configured to be flowed through in parallel by the liquid to be concentrated. Each condensation/evaporation element comprises at least one condensation unit and at least one evaporation unit. The apparatus further comprises at least one of: a centralized heating stage configured to generate steam and to provide the steam to each of the modules in parallel, and a centralized condensation stage configured to receive steam from each of the modules in parallel and to condensate the steam.

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10-08-2017 дата публикации

LOW PRESSURE SEPARATOR HAVING AN INTERNAL DIVIDER AND USES THEREFOR

Номер: US20170225098A1
Принадлежит:

Improvements in biological conversion processes and associated apparatuses are disclosed for the generation of useful end products such as ethanol, through metabolic pathways of C1-fixing bacteria that utilize, as a nutrient, a C1-carbon source from a C1-containing substrate such as an industrial waste gas. Particular aspects of the disclosure relate to the downstream recovery of ethanol and/or isopropanol from bleed and permeate streams and more particularly to performing such recovery with improved efficiency that can advantageously reduce capital (e.g., equipment) and/or operating (e.g., utility) costs. Particular aspects related to the downstream recovery of ethanol and/or isopropanol using a low pressure separator having an internal divider. 1. A biological conversion process comprising:feeding a substrate to a bioreactor system comprising at least a first bioreactor including a culture medium and bacterium to metabolize a carbon source in the substrate and produce at least one fermentation product;withdrawing from the bioreactor system a bleed stream comprising bacterium withdrawing from the bioreactor system a permeate stream obtained from filtration of a liquid stream of the bioreactor system;feeding at least a portion of the bleed stream and at least a portion of the permeate stream to a low pressure separator comprising a divider, the divider being configured to isolate, in a lower section, a liquid fraction of the bleed stream from a liquid fraction of the permeate stream and also configured to combine, in an upper section, a gaseous fraction of the bleed stream with a gaseous fraction of the permeate stream.2. The process of further comprisingpartitioning the permeate stream into at least a first permeate portion and a second permeate portion;feeding the first permeate portion-to a high pressure separator and feeding the second permeate portion to the low pressure separator;withdrawing, from the high pressure separator, a high pressure separator overhead ...

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18-07-2019 дата публикации

ODH COMPLEX WITH ON-LINE MIXER UNIT AND FEED LINE CLEANING

Номер: US20190218161A1
Принадлежит: NOVA CHEMICALS (INTERNATIONAL) S.A.

Oxidative dehydrogenation is an alternative to the energy extensive steam cracking process presently used for the production of olefins from paraffins. Various embodiments of an oxidative dehydrogenation chemical complex designed to allow removal of sulfur containing contaminants that collect in the gas mixer unit and in the feed lines leading to the ODH reactor are disclosed herein. 1. A chemical complex for the oxidative dehydrogenation of lower alkanes , the chemical complex comprising in cooperative arrangement:i) at least two mixers for premixing an oxygen containing gas and a lower alkane containing gas to produce a mixed feedstock stream and additionally comprising a cleaning loop; andii) at least one oxidative dehydrogenation reactor;wherein the at least two mixers are connected in parallel to the at least one oxidative dehydrogenation reactor so that either a first gas mixing unit or a second gas mixing unit is connected to the at least one oxidative dehydrogenation reactor during normal operations; andwherein an oxidative dehydrogenation catalyst contained within the at least one oxidative dehydrogenation reactor reacts with the mixed feed stock stream to produce a product stream comprising the corresponding alkene.2. The chemical complex of claim 1 , wherein the cleaning loop comprises a pump claim 1 , a filter claim 1 , and a small heating vessel.3. The chemical complex of claim 1 , further comprising a knock-out vessel claim 1 , after the mixed feedstock stream outlet and in close proximity to the at least one oxidative dehydrogenation reactor claim 1 , wherein the knock-out vessel is configured to receive a condensed cleaning solvent.4. The chemical complex of claim 1 , further comprising a feedline connecting each of the at least two mixers to the at least one oxidative dehydrogenation reactor claim 1 , wherein the feedlines are fitted with sprayers to introduce a cleaning solvent to internal walls of the feedline.5. The chemical complex of claim 1 , ...

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16-07-2020 дата публикации

ACETIC ACID PRODUCT QUALITY IMPROVEMENT

Номер: US20200222827A1
Принадлежит:

A process of purifying acetic acid is provided. The process includes feeding a feed stream comprising acetic acid into a bottom half of a distillation column and distilling the acetic acid in the presence of a homogeneous oxidizing agent in the distillation column, to oxidize oxidizable impurities in the acetic acid, wherein the homogeneous oxidizing agent is capable of cleaving C═C bonds. The process further includes removing a distilled acetic acid stream from the distillation column. Further processes for purifying acetic acid and systems for purifying acetic acid are also provided. 1. A process for purifying acetic acid , comprising:feeding a feed stream comprising acetic acid into a bottom half of a distillation column;distilling the acetic acid in the presence of a homogeneous oxidizing agent in the distillation column to oxidize oxidizable impurities in the acetic acid, wherein the homogeneous oxidizing agent is capable of cleaving C═C bonds; andremoving a distilled acetic acid stream from the distillation column,wherein the homogeneous oxidizing agent is positioned in the feed stream.2. The process of claim 1 , wherein the oxidizable impurities comprise an α claim 1 ,β-unsaturated carbonyl compound.3. The process of claim 2 , wherein the α claim 2 ,β-unsaturated carbonyl compound comprises an α claim 2 ,β-unsaturated carboxylic acid.4. The process of claim 3 , wherein the α claim 3 ,β-unsaturated carboxylic acid comprises acrylic acid.5. The process of claim 1 , wherein the distillation column comprises a sump in the bottom half of the distillation column and the homogeneous oxidizing agent is positioned in the sump.6. A process for purifying acetic acid claim 1 , comprising:feeding a feed stream comprising acetic acid into a distillation column, anddistilling the acetic acid in the presence of a homogeneous oxidizing agent, a top half and a bottom half; and', 'a sump in the bottom half of the distillation column; and, 'the distillation column comprises, ' ...

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26-08-2021 дата публикации

Process and apparatus for quenching a reactor effluent stream

Номер: US20210260554A1
Принадлежит: UOP LLC

A process and apparatus cool and remove catalyst from a hot vaporous reactor effluent stream by feeding the hot vaporous reactor effluent stream comprising catalyst and a first quench liquid stream to a first quench chamber. The hot vaporous reactor effluent stream is directly contacted with the first quench liquid stream to cool the hot reactor effluent stream and wash catalyst therefrom into the first quench liquid stream. The first quench liquid stream and the vaporous reactor effluent stream are passed together through a bed while disengaging catalyst from the vaporous reactor effluent stream and transferring catalyst into the first quench liquid stream.

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16-07-2020 дата публикации

Process and plant for separatory processing of a starting mixture

Номер: US20200224968A1
Принадлежит:

The present invention relates to a process () for separatory processing of a starting mixture containing predominantly hydrogen, methane and hydrocarbons having two or two or more carbon atoms, wherein at least a portion of the starting mixture is cooled to form one or more condensates using one or more heat exchangers () and at least a portion of the condensate(s) is subjected to a rectification to form a gaseous methane-rich fraction. It is provided that the gaseous methane-rich fraction is used to form a first fluid stream which is at least partly compressed, in an unchanged composition with respect to the gaseous methane-rich fraction, to a liquefaction pressure level of 35 to 45 bar, and at least partly liquefied by cooling, and in that the first fluid stream, or a second fluid stream formed using the first fluid stream, is expanded to a delivery pressure and heated in the or at least one of the heat exchanger(s) (). A corresponding plant likewise forms part of the subject matter of the invention. 1100101103105107101103105107. Process () for separatory processing of a starting mixture containing predominantly hydrogen , methane and hydrocarbons having two or two or more carbon atoms , wherein at least a portion of the starting mixture is cooled to form one or more condensates using one or more heat exchangers ( , , , ) and at least a portion of the condensate(s) is subjected to a rectification to form a gaseous methane-rich fraction , characterized in that the methane-rich fraction is used to form a first fluid stream which is at least partly compressed , in an unchanged composition with respect to the gaseous methane-rich fraction , to a liquefaction pressure level of 35 to 45 bar , is at least partly liquefied by cooling , and is expanded to a delivery pressure level , and in that the first fluid stream , or a second fluid stream formed using the first fluid stream , is heated in the or at least one of the heat exchanger(s) ( , , , ).2100. Process () ...

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23-08-2018 дата публикации

PRODUCTION OF MULTIVALENT ION-RICH STREAMS USING HUMIDIFICATION-DEHUMIDIFICATION SYSTEMS

Номер: US20180236372A1
Принадлежит: Gradiant Corporation

Disclosed herein are systems and methods in which an aqueous stream comprising solubilized monovalent ions and solubilized multivalent ions is processed such that multivalent ions are selectively retained and monovalent ions are selectively removed. According to certain embodiments, an aqueous feed stream is transported through an ion-selective separator to produce a multivalent-ion-enriched stream and a monovalent-ion-enriched stream. The monovalent-ion-enriched stream may be transported through a desalination apparatus to produce a substantially pure water stream and a concentrated aqueous stream. In some embodiments, at least a portion of the multivalent-ion-enriched stream produced by the ion-selective separator is combined with at least a portion of the substantially pure water stream produced by the desalination apparatus to produce a combined product stream containing a relatively large percentage of the solubilized multivalent ions from the aqueous feed stream and a relatively small percentage of the solubilized monovalent ions from the aqueous feed stream. 1. A method , comprising:transporting an aqueous feed stream containing solubilized monovalent ions and solubilized multivalent ions into an ion-selective separator comprising an ion-selective membrane to produce a first permeate stream containing at least about 75% of the solubilized monovalent ions from the aqueous feed stream and a first retentate stream containing at least about 75% of the solubilized multivalent ions from the aqueous feed stream;transporting at least a portion of the first permeate stream to a desalination apparatus comprising a humidifier and a dehumidifier;allowing at least a portion of the first permeate stream to evaporate within a humidifier of the desalination apparatus to produce a humidified gas and a concentrated aqueous stream having a higher concentration of solubilized monovalent ions than the first permeate stream;condensing at least a portion of the water within the ...

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01-08-2019 дата публикации

CLOSED-LOOP THERMAL SERVICING OF SOLVENT-REFINING COLUMNS

Номер: US20190232344A1
Автор: MELSERT Ryan
Принадлежит: Tesla, Inc.

A system for thermally servicing a solvent-refining column includes: a first solvent-refining column, a closed-loop water-steam system; a first heat-exchanger thermally coupling the closed-loop water-steam system to the top of the first solvent-refining column, a second heat-exchanger thermally coupling the closed-loop water-steam system to a bottom of the first solvent-refining column, and a compressor positioned between the first heat-exchanger and the second heat-exchanger. The first heat-exchanger boils pressurized water to steam by transferring first heat from the top of the first solvent-refining column to the closed-loop water- steam system. The compressor compresses the steam in the closed-loop water-steam system to a higher temperature. The second heat-exchanger provides second heat to the first solvent-refining column by condensing the steam at the bottom of the first solvent-refining column after compression by the compressor. 1. A system comprising:a first solvent-refining column containing at least a solvent and impurities, the first solvent-refining column having a top and a bottom;a closed-loop water-steam system;a first heat-exchanger thermally coupling the closed-loop water-steam system to the top of the first solvent-refining column;a second heat-exchanger thermally coupling the closed-loop water-steam system to the bottom of the first solvent-refining column;a compressor positioned between the first heat-exchanger and the second heat-exchanger;the first heat-exchanger configured to boil pressurized water in the closed-loop water-steam system to steam by transferring first heat from the top of the first solvent-refining column to the closed-loop water- steam system;the compressor configured to compress the steam in the closed-loop water-steam system to a higher temperature; andthe second heat-exchanger configured to provide second heat to the first solvent-refining column by condensing the steam at the bottom of the first solvent-refining column ...

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23-07-2020 дата публикации

Dirty water distillation and salt harvesting system, method, and apparatus

Номер: US20200230516A1
Принадлежит: XDI Holdings LLC

Embodiments of the present disclosure include a system for harvesting salt, and other valued material, and generating distilled water from at least one of a produced water and salt water. The system can include a direct steam generator (DSG) configured to generate saturated steam and combustion exhaust constituents. The system can include a separation system operating after the DSG, configured to separate salt from the saturated steam and combustion exhaust constituents in at least one of brine form and solid form. The system can include an energy recovery system that includes an expansion turbine configured to recover energy from the steam and exhaust constituents.

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01-09-2016 дата публикации

SOLVENT DECONTAMINATION SYSTEM AND METHOD

Номер: US20160251235A1
Принадлежит:

A system and method for decontaminating a fluid like a non-azeotrope solvent such as water, wherein a transport gas is maintained at a temperature between the freezing point and boiling point at atmospheric pressure of the solvent and continuously circulated between an evaporation chamber and a condensation chamber, a contaminated solvent is introduced into the transport gas in the evaporation chamber under process heat and contaminant precipitates out, and the cleaned solvent cools in the condensation chamber releasing heat to be used in the evaporation chamber. A heat pump is used to promote evaporation and condensation within the system. 1. A system for at least partial decontamination of a contaminated fluid to produce a purified fluid , the system comprising:a process fluid container for containing the contaminated fluid and the purified fluid;an evaporation region for at least partially evaporating the contaminated fluid to form an evaporated fluid;a condensation region for condensing the purified fluid;the evaporation region and the condensation region in fluid communication;the evaporation region and the condensation region retaining a transport gas for transporting the evaporated fluid to the condensation region, the transport gas becoming at least partially saturated with the evaporated fluid in the evaporation region, the transport gas releasing the purified fluid in the condensation region;an inlet for introducing the contaminated fluid to the evaporation region;a purified fluid outlet for withdrawing the purified fluid from the condensation region;a process fluid supply for supplying from the process fluid container a process fluid in the form of either the contaminated fluid or the purified fluid to cool the transport gas to promote condensation in the condensation region; anda heat exchanger;wherein the process fluid passes through the heat exchanger to remove heat from the process fluid to form a cooled process fluid, and the cooled process fluid ...

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17-09-2015 дата публикации

Humidification-Dehumidification System with a Bubble-Column Vapor Mixture Condenser and Intermediate Gas Extraction

Номер: US20150260418A1
Принадлежит:

A humidification-dehumidification system comprises a source of liquid; a humidifier including carrier-gas and liquid inlets and outlets and a chamber in which the liquid can contact a carrier gas containing a condensable fluid in vapor phase that is introduced from the carrier-gas inlet in a counterflow arrangement and in which a portion of the liquid can vaporize into the carrier gas; a bubble-column vapor mixture condenser including at least first and second stages, each stage including a carrier-gas inlet and outlet and a chamber configured to contain a liquid bath in fluid communication with the carrier-gas inlet and the carrier-gas outlet; a conduit passing from the source of the liquid through the chamber of each stage of the bubble-column condenser; and an intermediate exchange conduit coupled with (a) the bubble-column vapor mixture condenser and (b) the humidifier chamber at intermediate stages of each for transfer of the carrier gas therebetween. 1. A multi-stage bubble-column vapor mixture condenser comprising:a fluid source supplying a carrier gas that includes a condensable fluid in vapor phase;at least a first stage and a second stage of the bubble-column condenser, wherein each stage includes an inlet, an outlet and a chamber in fluid communication with the inlet and the outlet, wherein the inlet of the first stage of the bubble-column condenser is coupled with the fluid source, and wherein the outlet of the first stage is in fluid communication with the inlet of the second stage to facilitate flow of the carrier gas from the fluid source through the chamber of the first stage and then through the chamber of the second stage, wherein the condensable fluid in liquid phase fills the chambers of the first stage and the second stage such that the carrier gas including the vapor-phase condensable fluid passes through and contacts the liquid-phase condensable fluid when passing from the inlet to the outlet of each stage; anda conduit that passes through the ...

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07-10-2021 дата публикации

Organic ammonium compositions and methods of their use and making

Номер: US20210309582A1
Принадлежит: California Safe Soil LLC

Methods and systems for converting ammonium waste streams into certifiably Organic ammonium salts having a variety of uses in greenhouse gas-reducing activities are herein described. The resulting ammonium salt compositions can be used to enhance crop yield.

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22-09-2016 дата публикации

Multi-Stage Bubble-Column Vapor Mixture Condenser and HDH System

Номер: US20160271518A1

A multi-stage bubble-column vapor mixture condenser comprises at least a first stage and a second stage. Each stage includes a carrier-gas inlet and a carrier-gas outlet, as well as a condenser chamber containing a condensing bath in fluid communication with the carrier-gas inlet and the carrier-gas outlet. The carrier-gas inlet is positioned to bubble carrier gas from the carrier-gas inlet up through the condensing bath, overcoming a hydrostatic head of the condensing bath. The carrier-gas outlet is positioned with an opening for carrier-gas extraction above the condensing bath, wherein the first-stage carrier-gas outlet is in fluid communication with the carrier-gas inlet of the second stage to facilitate flow of the carrier gas through the condensing bath in the condenser chamber of the first stage and then through the condensing bath in the condenser chamber of the second stage.

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22-09-2016 дата публикации

Vacuum Condenser

Номер: US20160271519A1
Принадлежит: Individual

A vacuum condenser adapted to reduce pressure in an enclosure containing a secondary liquid and thereby cause the accelerated production of vapor from the secondary liquid by the passage of a primary liquid through the vacuum condenser and whereby the vapor produced is absorbed by the primary liquid within the vacuum condenser by being entrained and condensed within the primary liquid wherein the vacuum condenser is configured to cause the operating temperature of the secondary liquid within the enclosure to maintain a stable minimum temperature for a predetermined substantial rate of production of vapor.

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22-09-2016 дата публикации

System and Method for Water Treatment

Номер: US20160272507A1
Автор: Dighe Shyam V.
Принадлежит:

System and method of treating waste water includes: receiving waste water at a first pressure and a first temperature, the waste water comprising dissolved solids and VOCs; pressurizing the waste water to a second pressure; preheating the pressurized waste water to a second temperature to produce distilled water and pressurized/preheated water; heating the pressurized/preheated to a third temperature to produce pressurized/heated water; removing dissolved solids from the pressurized/heated water, by an evaporator operated at a third pressure less than the second pressure, to produce steam and brine water; and crystallizing the brine water, by a crystallizer operated at a fourth pressure greater than the second pressure, to produce a solid mass waste product and steam. Steam produced by the crystallizer, at the fourth pressure and a fourth temperature, is a heat source for the preheater and/or heater, and steam produced by the evaporator is a heat source for the crystallizer. 158-. (canceled)59. A system for treating waste water comprising:a pump receiving waste water at a first pressure and a first temperature and pressurizing the received waste water to a second pressure greater than the first pressure, the waste water comprising dissolved solids and volatile organic compounds;first and second preheaters connected in series and operatively connected to the pump such that the first preheater receiving the pressurized waste water from the pump and preheating the pressurized waste water to a second temperature greater than the first temperature to produce a pressurized/preheated waste water, and the second preheater heating the pressurized/preheated waste water to a third temperature greater than the second temperature to produce a pressurized/further preheated waste water, each of the first and second preheaters producing a distilled water without boiling of the waste water across heat transfer surfaces;a condenser operatively connected to the first and second ...

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22-08-2019 дата публикации

LIQUID SEPARATOR AND CONCENTRATOR

Номер: US20190255460A1
Принадлежит: Colorado Extraction Systems, LLC

A liquid separator and concentrator is disclosed. An example liquid separator and concentrator includes a separator column. A spray chamber has a sprayer nozzle to spray an influent within the spray chamber and create a falling film in the separator column. A heating jacket surrounds the separator column, wherein the heating jacket heats the falling film to evaporate at least one portion of the falling film and leaves a concentrate. A concentrate collection vessel receives the concentrate from the separator column. 1. A liquid separating and concentrating method , comprising:spraying an influent by a sprayer nozzle within the spray chamber to create a falling film with a consistent laminar flow in a separator column;heating the falling film to evaporate at least one portion and leave a concentrate; andcollecting the concentrate from the separator column.2. The method of claim 1 , further comprising cooling the evaporated portion.3. The method of claim 1 , further comprising drawing the evaporated portion through at least one condenser.4. The method of claim 1 , further comprising providing at least one condenser with a multi-layer chilling line.5. The method of claim 4 , wherein the at least one condenser has an outer chilling line wrapping around an inner wall of the at least one condenser claim 4 , a nested chilling line wrapping around inside the outer chilling line claim 4 , and an inner chilling line wrapping around the inside of the nested chilling line. This application is a divisional of U.S. patent application Ser. No. 15/086,838, filed on Mar. 31, 2016 entitled “Liquid Separator and Concentrator”, which claims priority to U.S. Provisional Patent Application No. 62/141,819, filed Apr. 1, 2015 entitled “Improved Volatiles Separator And Non-Volatiles Concentrator System and Methods of Use,” the contents of both of which hereby incorporated by reference in their entirety.A portion of the disclosure of this patent document contains material which is subject to ...

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21-09-2017 дата публикации

GRAIN ALCOHOL DISTILLATION PLANTS

Номер: US20170266582A1
Принадлежит: Porta Hnos. S.A.

Improvements in grain alcohol distillation plants by incorporating a novel internal arrangement in the wort column and the rectifying column with distributors and accumulators inside thereof, achieving a stable and safe process in wide ranges of operation, guaranteeing the productivity of the plant and the quality of the products. The wort column features detachable perforated plates, easy to access and clean through manholes. By having easily detachable plates and, also, a manhole for each plate with “holder” type connections, the access to the interior of the column for cleaning and maintenance purposes is facilitated. The rectifying column is a special filling column with flow distributors, it has an intermediate alcohol accumulator and a condenser which is an integral part of the column that prevents the use of pumps. The arrangement of distributors and accumulators within the rectifying column favors the operational stability of the plant, allowing a low scale equipment to work similarly to an industrial scale column. The improvements include an integrated automation system with Internet communication for self-management of the plant with remote monitoring and autonomous operation.

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13-08-2020 дата публикации

Fully Regenerative Distillation System for Low-Cost Water Desalination

Номер: US20200255302A1
Принадлежит: Amantsy, Inc.

A desalination device includes a sealed desalination chamber with two compartments, an evaporator space that contains saline water, and a condenser space that contains fresh water, a saline water distribution mechanism that directs the saline water into the evaporator space, a vapor compressor that directs a stream of pressurized freshwater vapor into the condenser space, and an integrated regenerative boundary between the evaporator space and the condenser space that has two sides, an evaporation surface and a condensation surface, enabling the pressurized freshwater vapor to condense on the condensation surface to generate freshwater, and where the latent heat of the condensation process transfers across the integrated regenerative boundary into the evaporator space and evaporates a portion of the saline water to produce freshwater vapor. 1. A desalination device , comprising: an evaporator space that contains saline water; and', 'a condenser space that contains fresh water;, 'a sealed desalination chamber that comprises two compartmentsa saline water distribution mechanism within the chamber for receiving incoming saline water and directing it into the evaporator space;a vapor compressor within the chamber that receives freshwater vapor from the evaporator space and directs a stream of pressurized freshwater vapor into the condenser space; andan integrated regenerative boundary that divides the evaporator space and the condenser space, comprising an evaporation surface inside the evaporator space and a condensation surface inside the condenser space, wherein the pressurized freshwater vapor condenses on the condensation surface to generate freshwater, and wherein the latent heat of condensation transfers across the integrated regenerative boundary into the evaporation space, and wherein the transferred heat evaporates the saline water into the evaporator space to evaporate the saline water.2. The device of claim 1 , further comprising:an external saline water ...

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28-09-2017 дата публикации

RECOVERY OF TOBACCO CONSTITUENTS FROM PROCESSING

Номер: US20170273351A1
Автор: Besso Clement
Принадлежит:

A method includes volatilizing one or more compounds from tobacco, or reaction products thereof, into a gas stream and recovering at least one of the one or more volatilized compounds or reaction products from the gas stream. The method may be carried out in connection with a dry ice expanded tobacco (“DIET”) process where volatile tobacco compounds are recovered rather than incinerated as is typically done with current DIET processes. 1. A composition comprising nicotine and one or more tobacco-derived compounds , wherein the one or more tobacco-derived compounds are obtained by a process comprising condensing a gas stream employed in a tobacco expansion process comprising the tobacco-derived compounds to form a condensate , and fractionating the condensate to selectively recover or enrich the one or more tobacco-derived compounds.2. A composition according to claim 1 , wherein the one or more tobacco-derived compounds are obtained by condensing a gas stream that is employed in a dry ice tobacco expansion process.3. A composition according to claim 1 , wherein the one or more tobacco-derived compounds in the gas stream are generated from tobacco by volatilization at a temperature at between about 150° C. and about 400° C.4. A composition according to claim 1 , wherein the one or more tobacco-derived compounds in the gas stream are obtained by treating tobacco that is impregnated with non-gaseous carbon dioxide with a gas stream comprising steam claim 1 , at a temperature at between about 150° C. and about 400° C. claim 1 , thereby volatizing the one or more tobacco-derived compounds.5. A composition according to claim 1 , wherein the one or more tobacco-derived compounds are obtained by condensing the gas stream in more than one stage at different temperature ranges and forming more than one condensate.6. A composition according to claim 1 , wherein one or more of the tobacco-derived compounds is a terpene claim 1 , a tobacco alkaloid claim 1 , or an alkylpyrazine. ...

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27-09-2018 дата публикации

Production Water Desalinization Via a Reciprocal Heat Transfer and Recovery

Номер: US20180272246A1
Автор: Fred Polnisch
Принадлежит: Individual

A system for brine water desalinization includes a first heat exchanger having an inlet plenum and an outlet plenum for a first fluid comprising a concentrate in a liquid. The first heat exchanger includes a shell side fluid inlet and a shell side fluid outlet for a second fluid comprising a higher concentrated liquid than the first fluid. The system also comprises pipes configured to direct the first fluid from the outlet plenum to a shell side fluid inlet of a second heat exchanger and to direct the second fluid from the shell side fluid outlet to an inlet plenum of the second heat exchanger. The system further includes pipes configured to produce desalinized water by a serial distillation of multiple steams from an nth number of heat exchangers into respective distillates thereof and a parallel product of brine waste thereof from the heat exchangers.

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04-10-2018 дата публикации

Fresh water and salable energy without environmental harm1

Номер: US20180282181A1
Автор: Taylor William P.
Принадлежит:

Three embodiments of an invention are disclosed in which sea water undergoes a desalination process accompanied by production of salable energy of value greater than the cost of the fossil fuel required, and which discharges brine to the sea at a temperature and salinity harmless to sea life. 19-. (canceled)10. A process for producing fresh water and salable energy without environmental harm , using components of existing technology ,a. a technique for removing water from the sea, removing the salt from a small portion, and returning the remainder to the sea at a temperature and salinity only slightly altered;b. evaporation of a small portion of that removed using heat from a gas-fired burner;c. production of energy from a steam driven turbine;d. production of distilled water by condensing salt-free steam in a condenser cooled by the larger portion of that removed from the sea111. A simple means , described as basic embodiment , for performing claim bya. use of a low pressure boiler to evaporate salt-free steam at a temperature below that likely to deposit scale;b. heating the steam before expanding it in a low pressure turbine;c. exhausting the steam to the condenser where it is condensed to distilled water121. A superior means for performing claim , described as the preferred embodiment bya. water, treated to be free of minerals capable of depositing scale cycles in a conventional high pressure process to produce significantly more energy;b. exhaust steam is condensed inside a coil immersed in seawater in a chamber in an isothermal process; the condensed water is pumped to a high pressure to commence a new cycle;c. the latent heat released transfers to the cooler inner wall of the coil and transfers to the outer wall by conduction of the high conductivity copper material;d. heat transfer from the outer wall evaporates a portion of the surrounding sea water in an isothermal process due to its lower temperature;e. the salt-free steam enters the condenser where it ...

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22-10-2015 дата публикации

DEVICES AND METHODS FOR REMOVING NANO-PARTICULATES FROM GASES

Номер: US20150298042A1
Автор: Liang Bin, Lin Han, TU Juan
Принадлежит: NANJING UNIVERSITY

Systems and methods are disclosed for removing nano-particulates from a gas. The systems may include a chamber to contain the particulate-containing gas, a source of the gas, a source of water vapor, a source of a supersonic gas, and at least one ultrasonic transducer in contact with the chamber. The chamber may also include one or more receptacles to receive the particulates. The methods may include introducing the particulate-containing gas and the water vapor into the chamber. A gas may be introduced into the chamber at supersonic speeds thereby cooling the water vapor to form nucleating ice crystals. The ultrasonic transducers may then introduce ultrasonic power into the chamber thereby causing the particulates to contact the ice crystals. The nucleating crystals, with their attached particulates, may then fall under gravity to be captured in the receptacles. 1. A system for removing a plurality of particulates from a particulate-containing gas , the system comprising:a chamber;a source of a particulate-containing gas comprising an inlet valve in fluid communication with the chamber;a source of a supersonic gas in fluid communication with the chamber, wherein the supersonic gas is a non-flammable gas;a source of water vapor in fluid communication with the chamber; andat least one ultrasonic transducer in acoustic communication with the chamber.23.-. (canceled)4. The system of claim 1 , wherein the chamber has a rectangular cross section or a circular cross section.59.-. (canceled)10. The system of claim 1 , wherein the source of a supersonic gas comprises a gas accelerating inlet comprising a first side and a second side claim 1 , and a source of a cooling gas claim 1 , wherein the first side of the gas accelerating inlet is in fluid communication with the source of the cooling gas and the second side of the gas accelerating inlet is in fluid communication with the chamber.11. The system of claim 10 , wherein the gas accelerating inlet is a de Laval nozzle.12. ...

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19-09-2019 дата публикации

SYSTEMS INCLUDING A CONDENSING APPARATUS SUCH AS A BUBBLE COLUMN CONDENSER

Номер: US20190282921A1
Принадлежит: Gradiant Corporation

Condensing apparatuses and their use in various heat and mass exchange systems are generally described. The condensing apparatuses, such as bubble column condensers, may employ a heat exchanger positioned external to the condensing vessel to remove heat from a bubble column condenser outlet stream to produce a heat exchanger outlet stream. In certain cases, the condensing apparatus may also include a cooling device positioned external to the vessel configured and positioned to remove heat from the heat exchanger outlet stream to produce a cooling device outlet stream. The condensing apparatus may be configured to include various internal features, such as a vapor distribution region and/or a plurality of liquid flow control weirs and/or chambers within the apparatus having an aspect ratio of at least 1.5. A condensing apparatus may be coupled with a humidifier to form part of a desalination system, in certain cases. 1268-. (canceled)269. A bubble column condenser , comprising:a first stage comprising a first stage inlet in fluid communication with a source of a gas comprising a condensable fluid in a vapor phase, and a first stage outlet; the first stage contains a liquid layer comprising an amount of the condensable fluid, and', 'the ratio of the height of the liquid layer within the first stage to the length of the condenser is about 1.0 or lower during substantially continuous operation., 'wherein270. The bubble column condenser of claim 269 , further comprising a second stage comprising a second stage inlet in fluid communication with the first stage outlet; wherein the first stage and the second stage each contain a liquid layer comprising an amount of the condensable fluid; and wherein the ratio of the height of the liquid layer within each stage to the length of the condenser is about 1.0 or lower during substantially continuous operation.271. The bubble column condenser of claim 269 , wherein the ratio of the height of the liquid layer within at least one ...

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19-09-2019 дата публикации

Multi-Stage Bubble-Column Vapor Mixture Condensation

Номер: US20190282922A1

A multi-stage bubble-column vapor mixture condenser comprises at least a first stage and a second stage. Each stage includes a carrier-gas inlet and a carrier-gas outlet, as well as a condenser chamber containing a condensing bath in fluid communication with the carrier-gas inlet and the carrier-gas outlet. The carrier-gas inlet is positioned to bubble carrier gas from the carrier-gas inlet up through the condensing bath, overcoming a hydrostatic head of the condensing bath. The carrier-gas outlet is positioned with an opening for carrier-gas extraction above the condensing bath, wherein the first-stage carrier-gas outlet is in fluid communication with the carrier-gas inlet of the second stage to facilitate flow of the carrier gas through the condensing bath in the condenser chamber of the first stage and then through the condensing bath in the condenser chamber of the second stage.

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26-09-2019 дата публикации

OIL PRODUCTS DERIVED FROM DILUTED PYROLYSIS GAS BY CONTINUOUS MILD-TEMPERATURE PYROLYSIS COAL-TAR SEPARATION PROCESS

Номер: US20190292467A1
Автор: England Dennis Carl
Принадлежит: Convert Coal, Inc.

The present invention pertains to the recovery, separation and the unique product mixtures obtained by recovery and separation of coal-tar oils produced from low-rank-coal by a novel mild-temperature pyrolysis [MTP] process originating at the point where the vapor phase exits the pyrolysis reactor. Mild-temperature pyrolysis [MTP] takes place below 1200° F. in contrast to the high-temperature pyrolysis [HTP] that is operated at 1600-2000° F. for coke oven processing of metallurgical coke. The yield and composition of coal-tar-oil recovered from MTP are quite different from HTP coal-tar. In order to optimize the oil recovery process, the most appropriate recovery and separation processes therefore also will be different. The MTP process produces coal-tar containing a major fraction of strongly polar compounds mixed with non-polar compounds that separates into several liquid phases and overlap in their distillation ranges. This invention addresses the distinct product fractions obtained from MTP and the integrated multi step oil recovery and product separation process, which is designed with the objective to improve and facilitate the product separation, decrease the required amount of energy for separation and equipment cost for downstream processing. 129-. (canceled)30. A process for recovering oil from pyrolysis vapor phase produced during mild temperature pyrolysis of a low rank coal by simultaneous fractionation of coal-tar-oil liquids , the method comprising:extracting the coal-tar-oil in vapor phase as one of the end-product of mild temperature pyrolysis process of a low rank coal using a sweeping gas;optimizing the recovered coal-tar-oil from the vapor phase and reduced the amounts of non-condensing gas compounds by sequentially passing the high temperature vapor phase through a plurality of vapor condensing unit such that each vapor condensing unit operates at a defined temperature which is lower than the temperature in preceding vapor condensing unit to ...

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24-09-2020 дата публикации

METHOD AND SYSTEM FOR RECOVERING AND PURIFYING A GASEOUS STERILIZING AGENT

Номер: US20200298140A1
Автор: LIN Enchi, Wu Peng-Chieh
Принадлежит:

A system for recovering a sterilization agent may include a pressure reducing value for reducing a pressure of a waste gas from a sterilization chamber to a first predefined pressure. The waste gas may include a gaseous mixture of a sterilization agent, nitrogen gas, and water vapor. A first condenser may cool the gaseous mixture to below a boiling point temperature and above a freezing point temperature of the water vapor at the first predefined pressure. A first tank may store the condensed water vapor. A separation pump may raise the pressure of the gaseous mixture to a second predefined pressure. A second condenser may cool the gaseous mixture to below a boiling point temperature and above a freezing point temperature of the sterilization agent at the second predefined pressure causing the sterilization agent to condense into a liquid. A second tank may store the separated sterilization agent. 1. A system for recovering a sterilization agent from a waste gaseous mixture , the system comprising:a pressure reducing value for reducing a pressure of a waste gas from one or more sterilization chambers to a first predefined pressure, the waste gas comprising a gaseous mixture of a sterilization agent, nitrogen gas, and water vapor;a first condenser configured to receive the gaseous mixture via the pressure reducing valve, and to cool the gaseous mixture to a temperature below a boiling point temperature and above a freezing point temperature of the water vapor at the first predefined pressure;a first tank coupled to the first condenser, for storing the condensed water vapor separated from the gaseous mixture in the first condenser;a separation pump coupled to the first tank for raising the pressure of the gaseous mixture to a second predefined pressure;a second condenser, configured to receive the gaseous mixture from the separation pump, to cool the gaseous mixture to a temperature below a boiling point temperature and above a freezing point temperature of the ...

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25-10-2018 дата публикации

Water purification device

Номер: US20180305222A1
Принадлежит: Benz Research and Development Corp

The disclosure provides systems methods and apparatus for purifying water. A purification device includes a heating vessel adapted to receive impure water and output water or water vapor. The device further includes at least one heating element arranged outside and in thermal contact with the heating vessel, configured to provide heat to the impure water. The device also includes at least one heat exchanger to exchange heat between the impure water and the water vapor to raise the temperature of the impure water. In some example implementations, the at least one heating element can include a Peltier cell.

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03-10-2019 дата публикации

HUMIDIFICATION-DEHUMIDIFICATION SYSTEMS AND METHODS AT LOW TOP BRINE TEMPERATURES

Номер: US20190300386A1
Принадлежит: Gradiant Corporation

Embodiments described generally relate to systems comprising a humidifier (e.g., a bubble column humidifier) and a heating device (e.g. a heat exchanger), and associated methods. In certain embodiments, the heating device heats a first liquid stream comprising a condensable fluid in liquid phase (e.g., water) and a dissolved salt (e.g., NaCl) to a relatively low temperature (e.g., about 90° C. or less) prior to the first liquid stream entering the humidifier through a main humidifier liquid inlet. In some cases, the system comprising the humidifier and the heating device requires only low-grade heat to operate, which may be advantageous due to the low cost and high availability of such heat. 1. A humidifier system , comprising:a humidifier comprising a main humidifier liquid inlet, a main humidifier gas inlet, a main humidifier liquid outlet, an intermediate humidifier liquid outlet, a main humidifier gas outlet, and a plurality of stages, wherein the plurality of stages comprises a first stage, a last stage, and one or more intermediate stages positioned between the first stage and the last stage, wherein the intermediate humidifier liquid outlet is a liquid outlet of the first stage or one of the one or more intermediate stages; anda first heating device, wherein a first liquid inlet of the first heating device comprises or is fluidically connected to the intermediate humidifier liquid outlet, and wherein a first liquid outlet of the first heating device comprises or is fluidically connected to the main humidifier liquid inlet, andwherein the first liquid inlet of the first heating device is configured to receive a first liquid stream comprising a condensable fluid in liquid phase and a dissolved salt, and wherein the main humidifier gas inlet is configured to receive a gas stream comprising a non-condensable gas.289-. (canceled)90. The humidifier system according to claim 1 , wherein the humidifier is configured to produce a vapor-containing humidifier gas outlet ...

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10-10-2019 дата публикации

Solvent Separation Apparatus and Solvent Separation Method

Номер: US20190308115A1
Автор: Lee Sung Kyu, Shin Joon Ho
Принадлежит: LG CHEM, LTD.

The present invention relates to a solvent separation apparatus and a solvent separation method, and the solvent separation apparatus and the solvent separation method according to the present application can reduce the used amount of cooling water and the used amount of steam, in a process of separating a polymer and a solvent. 1. A solvent separation apparatus comprising: a stripping unit in which a solvent outlet , a polymer outlet and an inlet are formed; a water tank having a water outlet; a heat exchange zone; a mixing zone for mixing water in the water tank with a polymer solution and a piping system , wherein the piping system comprises a first line connecting the water outlet and the mixing zone , a second line connecting the mixing zone and the inlet of the stripping unit; and a third line configured so that a mixture of a solvent and water can be discharged from the solvent outlet of the stripping unit ,wherein in the first line, an oily water outlet and an oily water inlet are formed, the piping system further comprises a fourth line configured so that a part of the water moving through the first line can be discharged through the oily water outlet and then recovered to the first line through the oily water inlet, and the third and fourth lines are configured to cross through via the heat exchange zone such that the water discharged through the oily water outlet can be heat-exchanged with the mixture of the solvent and the water moving through the third line and then recovered to the oily water inlet.2. The solvent separation apparatus according to claim 1 , wherein the heat exchange zone comprises a condensing zone and a sub-cooling zone claim 1 , the third line is configured so that the discharged mixture of the solvent and the water passes sequentially through the condensing zone and the sub-cooling zone claim 1 , and the fourth line is configured so that the water discharged to the oily water outlet is introduced into the oily water inlet after ...

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16-11-2017 дата публикации

Water Production, Filtration and Dispensing System

Номер: US20170326470A1
Принадлежит:

A water production system with a thermal separation device that defines a cold region and a hot region, a fluid-air heat exchanger located remotely from the thermal separation device and exposed to air, and a fluid circulation loop that thermally connects the cold region of the thermal separation device to the fluid-air heat exchanger so as to cool the fluid-air heat exchanger and condense water from ambient air to produce water pure enough so that with further treatment it can be made potable. Also disclosed are filtration and dispensing features that are appropriate for a potable water supply. 1. A water production , storage , filtration , and delivery system , comprising:a thermal separation device that defines a cold region and a hot region;a first liquid-based heat exchanger coupled to the cold region of the thermal separation device;a second liquid-based heat exchanger coupled to the hot region of the thermal separation device;a first liquid-air heat exchanger located remotely from the thermal separation device and exposed to air;a first pumped liquid circulation loop that thermally connects the first liquid-based heat exchanger to the first liquid-air heat exchanger so as to cool the first liquid-air heat exchanger and condense water from ambient air;an accumulator tank that receives the condensed water;a water holding tank that stores water;one or more water level sensors that sense an amount of water;a first system water outlet;one or more water filters in a fluid path between the accumulator tank and the water holding tank;one or more water filters in a fluid path between the water holding tank and the first water system outlet;a first water pump with an inlet fluidly coupled to the accumulator tank outlet and the water holding tank, and with an outlet fluidly coupled to the first system water outlet;a water purification process that purifies the water; anda controller that is operatively coupled to the water level sensors and the first pump, where the ...

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08-11-2018 дата публикации

Method for Separating Gases and Vapors in a Cascading Coolant Horizontal Spray Tower

Номер: US20180320964A1
Принадлежит:

A process for separating a gas and a vapor is disclosed. A cross-flow horizontal spray vessel comprising horizontally-situated sections is provided. Each of the sections comprise a spray nozzle or nozzles, and a collection hopper. A carrier gas, comprising a product vapor, is passed through the sections. A contact liquid is provided through the spray nozzle or nozzles such that the carrier gas passes across the contact liquid and a portion of the product vapor desublimates, condenses, crystallizes, or combinations thereof as a product solid into the contact liquid, leaving a product-depleted carrier gas. The contact liquid and the product solid are passed to a next preceding upstream spray nozzle or nozzles such that a temperature profile is established across the sections by the contact liquids, as the contact liquids are progressively warmer. The contact liquid and the product solid are removed. The product-depleted carrier gas is removed. 2. The process of claim 1 , wherein the temperature profile of the vessel varies less than a counter-current flow vessel temperature profile.3. The process of claim 1 , wherein the passing the contact liquid and the product step is accomplished by pumping.4. The process of claim 3 , further comprising providing a process controller.5. The process of claim 4 , wherein the pumping is accomplished by pumps comprising variable speed drives wherein pumping speeds are controlled by the process controller.6. The process of claim 3 , further comprising providing heat exchangers between the collection hoppers and the next preceding upstream spray nozzle or nozzles claim 3 , the heat exchangers modifying the temperature profile to increase efficiency of separations.7. The process of claim 3 , further comprising providing solid-liquid separation devices between the collection hoppers and the next preceding upstream spray nozzle or nozzles claim 3 , the solid-liquid separation devices removing the product solid from the contact liquid.8. ...

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24-11-2016 дата публикации

TRANSIENTLY-OPERATED DESALINATION SYSTEMS AND ASSOCIATED METHODS

Номер: US20160339354A1
Принадлежит: Gradiant Corporation

Systems and methods related to desalination systems are described herein. According to some embodiments, the desalination systems are transiently operated and/or configured to facilitate transient operation. In some embodiments, a liquid stream comprising water and at least one dissolved salt is circulated through a fluidic circuit comprising a desalination system. In some embodiments, a portion of the desalination system (e.g., a humidifier) is configured to remove at least a portion of the water from the liquid stream to produce a concentrated brine stream enriched in the dissolved salt. In certain cases, the concentrated brine stream is recirculated through the fluidic circuit until the concentrated brine stream reaches a relatively high density (e.g., at least about 10 pounds per gallon) and/or a relatively high salinity (e.g., a total dissolved salt concentration of at least about 25 wt %). In certain embodiments, additional salt is added to the concentrated brine stream to produce an ultra-high-density brine stream (e.g., a brine stream having a density of at least about 11.7 pounds per gallon). Some aspects relate to a system that is configured to promote energy efficiency by recovering heat from the recirculated concentrated brine stream upon discharge from the fluidic circuit. 1. A method for producing a concentrated brine stream , comprising:supplying a first liquid stream comprising water and at least one dissolved salt at an initial concentration to a fluidic circuit comprising a humidifier, wherein the humidifier removes at least a portion of the water from the first liquid stream to produce a first concentrated brine stream comprising water and the at least one dissolved salt at a second concentration higher than the initial concentration of the first liquid stream;recirculating the first concentrated brine stream through the fluidic circuit to remove at least a portion of the water from the first concentrated brine stream, forming a recirculated first ...

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