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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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Поддерживает ввод нескольких поисковых фраз (по одной на строку). При поиске обеспечивает поддержку морфологии русского и английского языка
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Применить Всего найдено 1072. Отображено 190.
22-03-2021 дата публикации

ПИРОЛИЗНАЯ ПЕЧЬ С РАЗДЕЛЬНЫМИ КАМЕРАМИ

Номер: RU2019125586A
Принадлежит: ПИРОэндТЕК СРЛС

РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2019 125 586 A (51) МПК C10J 3/00 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ЗАЯВКА НА ИЗОБРЕТЕНИЕ (21)(22) Заявка: 2019125586, 08.02.2018 (71) Заявитель(и): ПИРОэндТЕК СРЛС (IT) Приоритет(ы): (30) Конвенционный приоритет: (72) Автор(ы): ЛУРАГИ, Фламинио Джакомо (IT) 20.02.2017 IT 102017000018877 (85) Дата начала рассмотрения заявки PCT на национальной фазе: 20.09.2019 R U (43) Дата публикации заявки: 22.03.2021 Бюл. № 9 (86) Заявка PCT: (87) Публикация заявки PCT: WO 2018/149736 (23.08.2018) R U (54) ПИРОЛИЗНАЯ ПЕЧЬ С РАЗДЕЛЬНЫМИ КАМЕРАМИ (57) Формула изобретения 1. Пиролизная печь с раздельными камерами, которая содержит: a. пиролизную камеру (10), в которой обеспечен нагрев топлива по существу в отсутствие кислорода при температуре, которая может вызывать пиролиз топлива; b. камеру (20) сгорания пиролизованного топлива, в которой обеспечено сжигание пиролизованного топлива в присутствии потока воздуха; причем пиролизная камера (10) расположена внутри камеры (20) сгорания и выполнена с возможностью нагрева топочными газами. 2. Печь по п. 1, в которой печь содержит входное отверстие для органического топлива, входное отверстие (12) для воздуха, выходное отверстие (50) в пиролизной камере (10) для синтез-газа и выходное отверстие (40) в камере (20) сгорания для отработанного газа. 3. Печь по любому из пп. 1, 2, в которой в камере (20) сгорания присутствует датчик для измерения концентрации кислорода, предпочтительно лямбда-зонд. 4. Печь по п. 3, в которой обеспечена регулировка потока воздуха в зоне (20) сгорания в зависимости от концентрации кислорода. 5. Печь по любому из пп. 1-4, в которой природное органическое топливо выбрано из топливных гранул, щепы, скорлупы лесного ореха, опилок, биомассы. 6. Печь по любому из пп. 1-5, в которой зона (10) пиролиза состоит из шнекового питателя, и обеспечен вывод синтез-газа, получаемого в результате пиролиза, по трубе (50), соединенной с отсасывающим насосом. ...

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28-06-1984 дата публикации

BATCH TYPE COMBUSTION PROCESS AND APPARATUS

Номер: DE0002967003D1
Принадлежит: HONIGSBAUM RICHARD F, HONIGSBAUM, RICHARD F.

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24-10-2012 дата публикации

A pyrosis process for harnessing energy from waste materials

Номер: GB0201216194D0
Автор:
Принадлежит:

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05-01-2011 дата публикации

Waste management system/method including pyrolysis and power generation

Номер: GB0002471462A
Принадлежит:

System and method of integrated waste management including sorting a combustible waste material from a recyclable material using a separator 3 (e.g. trammel, shredder) and drying the waste material in an airless (e.g. super-heated steam) drier 4 to produce a pyrolysis feedstock. The feedstock may be fed to a pyrolyser 5 to produce pyrogas and char, the char being fed to a gasifier 6 to produce syngas, the pyrogas and syngas being burned off in an oxidiser 7, generating heat to generate electricity in a steam turbine 9 for a local or domestic power grid 15. Excess heat generated by oxidiser 7 may be supplied to pyrolyser 5 or drier 4 and excess heat in turbine 9 may be transferred to a heat recovery unit 24 for use in drier 4.

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24-04-2013 дата публикации

A Reactor for Processing Feed Material

Номер: GB0201304337D0
Автор:
Принадлежит:

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04-09-2019 дата публикации

Treatment of waste material

Номер: GB0201910313D0
Автор:
Принадлежит:

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30-06-2008 дата публикации

Process and system for gasification with in-situ tar removal

Номер: AP0200804469A0
Автор: PAISELY MARK A
Принадлежит:

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30-06-2008 дата публикации

Process and system for gasification with in-situ tar removal

Номер: AP2008004469A0
Автор: PAISELY MARK A
Принадлежит:

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30-06-2008 дата публикации

Process and system for gasification with in-situ tar removal

Номер: AP0200804469D0
Автор: PAISELY MARK A
Принадлежит:

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15-09-2011 дата публикации

PROCEDURE FOR THE TREATMENT OF ABLAUGE

Номер: AT0000522659T
Принадлежит:

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15-10-2011 дата публикации

VERFAHREN UND VORRICHTUNG ZUR ERZEUGUNG EINES GASES

Номер: AT0000509681A1
Автор:
Принадлежит:

The method involves partially gasifying and/or removing fuel in a circulating fluidized bed of a gasification zone (2). The remaining and/or not-converted fuel with a cooled bed material is placed in a combustion zone (3) and is recycled into the circulating fluidized bed of the gasification zone by a separator (8). The exhaust gas obtained from the separator and formed in the combustion zone is supplied to a solid separator (10) to separate the remaining bed material in the exhaust gas. The material is recycled into the combustion zone directly and/or by a bed material container (7). An independent claim is also included for a device for producing gas by gasification of fuel in a reactor.

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15-03-1996 дата публикации

PROCEDURE FOR THE THERMAL UTILIZATION OF WASTE MATERIALS

Номер: AT0000134698T
Принадлежит:

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15-10-1999 дата публикации

PROCEDURE AND MECHANISM FOR THE THERMOLYSE OF WASTE

Номер: AT0000184692T
Принадлежит:

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14-03-1991 дата публикации

SOLID WASTE DISPOSAL UNIT

Номер: AU0005505890A
Автор: KYDD PAUL H, PAUL H. KYDD
Принадлежит:

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13-09-2012 дата публикации

Carbon Conversion System with integrated processing zones

Номер: AU2011223466A1
Принадлежит:

A Carbon Conversion System having four functional units, each unit comprising one or more zones, wherein the units are integrated to optimize the overall conversion of carbonaceous feedstock into syngas and slag. The processes that occur within each zone of the system can be optimized, for example, by the configuration of each of the units and by managing the conditions that occur within each zone using an integrated control system.

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04-05-1989 дата публикации

TREATMENT OF WASTE AND A ROTARY KILN THEREFOR

Номер: AU0000583750B2
Принадлежит:

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09-09-2011 дата публикации

CARBON CONVERSION SYSTEM WITH INTEGRATED PROCESSING ZONES

Номер: CA0002756745A1
Принадлежит:

A Carbon Conversion System having tour functional units, each unit comprising one or more zones, wherein the units are integrated to optimize the overall conversion of carbonaceous feedstock into syngas and slag. The processes that occur within each zone of the system can be optimized, for example, by the configuration of each of the units and by managing the conditions that occur within each zone using an integrated control system.

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04-03-2010 дата публикации

METHOD AND SYSTEM FOR PRODUCTION OF A CLEAN HOT GAS BASED ON SOLID FUELS

Номер: CA0002734315A1
Принадлежит:

Solid fuel can be converted into a clean hot flue gas with a low content of volatile organic compounds (VOC's), NOx and dust, and clean ash with a low carbon content by means of a stage-divided thermal reactor, where the conversion process of the solid fuel is in separate vertical stages (from below and up): ash burn-out, char oxidation and gasification, pyrolysis, drying, and a gas combustion stage where gas from the gasifier is combusted.

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08-12-2005 дата публикации

IMPROVED GASIFIER

Номер: CA0002568029A1
Автор: STEIN, PETER
Принадлежит:

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26-04-2007 дата публикации

PROCESS AND SYSTEM FOR GASIFICATION WITH IN-SITU TAR REMOVAL

Номер: CA0002626537A1
Принадлежит:

The present invention relates to a process and system for gasifying biomass or other carbonaceous feedstocks in an indirectly heated gasifÊer and provides a method for the elimination of condensable organic materials (tars) from the resulting product gas with an integrated tar removal step. More specifically , this tar removal step utilizes the circulating heat carrier to crack the organics and produce additional product gas. As a benefit of the above process, and because the heat carrier circulates through alternating steam a nd oxidizing zones in the process, deactivation of the cracking reactions is eliminated.

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01-08-2017 дата публикации

CHAR-HANDLING PROCESSES IN A PYROLYSIS SYSTEM

Номер: CA0002805386C
Принадлежит: ENSYN RENEWABLES, INC., UOP LLC

Char-handling processes for controlling overall heat balance, ash accumulation, and afterburn in a reheater are provided. Carbonaceous biomass feedstock is pyrolyzed using a heat transfer medium forming pyrolysis products and a spent heat transfer medium. The spent heat transfer medium is separated into segregated char and char-depleted spent heat transfer medium. The char-depleted spent heat transfer medium is introduced into a dense bed of heat transfer medium fluidized by a stream of oxygen-containing regeneration gas. All or a portion of the segregated char is combusted in the dense bed using the stream of oxygen-containing regeneration gas. A portion of the segregated char may be exported out of the pyrolysis system to control the overall heat balance and ash accumulation.

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12-06-2018 дата публикации

SEAL POT DESIGN

Номер: CA0002852763C
Принадлежит: RES USA, LLC, RENTECH INC, RENTECH, INC.

An apparatus including at least one seal pot having at least one penetration through a surface other than the top of the seal pot, each of the at least one penetrations being configured for introduction, into the at least one seal pot, of solids from a separator upstream of the at least one seal pot; a substantially non-circular cross section; or both at least one penetration through a surface other than the top of the seal pot and a substantially non-circular cross section.

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30-07-1998 дата публикации

INSTALLATION FOR GENERATING ENERGY FROM ASSIMILATED URBAN WASTE

Номер: CA0002225594A1
Принадлежит:

La présente invention concerne une installation de valorisation énergétique de déchets urbains et assimilés comportant - un dispositif de broyage (1) des déchets dont les refus sont évacués, - un réacteur à lit fluidisé circulant (2) recevant les déchets broyés par une conduite d'alimentation et comportant un lit fluidisé dense latéral situé sur la paroi du réacteur comportant la conduite d'alimentation en déchets broyés, un conduit d'extraction des éléments lourds non fluidisables étant situé à la base de ce lit fluidisé dense latéral et amènant ceux-ci dans un dispositif trieur de grosses particules (3) refroidissant ces éléments et extrayant les matières inertes non fluidisables, les autres matières étant réintroduites dans le réacteur (2), - un agencement de récupération d'énergie et de traitement des fumées sortant dudit réacteur (2). Selon l'invention, au moins une partie desdits refus sont introduits dans ledit dispositif trieur de grosses particules (3).

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31-05-2017 дата публикации

Burner.

Номер: CH0000711812A1
Автор: ANDRÉ VAN DER VEKEN
Принадлежит:

Un brûleur combustibles gazeux, fluides ou pulvérulents, dans lequel on introduit trois composantes: un combustible (40); un gaz comburant (10), par exemple de l’air, et; un gaz inerte (20), par exemple des gaz issus de la combustion, de l’azote, ou de la vapeur d’eau. Deux composantes, par exemple l’air et le gaz inerte, sont mélangées entre elles (30) et propulsés par un ou plusieurs étages d’injection (95) disposés à des positions différentes relativement au mouvement du combustible.

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30-04-2013 дата публикации

SYSTEM CONVERSION OF CARBON WITH INTEGRATED TECHNOLOGICAL ZONES

Номер: EA0201201197A1
Автор:
Принадлежит:

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30-06-2010 дата публикации

СПОСОБ И СИСТЕМА ДЛЯ ГАЗИФИКАЦИИ С ВНУТРИЦИКЛОВЫМ УДАЛЕНИЕМ СМОЛЫ

Номер: EA0000013703B1

Настоящее изобретение относится к способу и устройству для газификации биомассы или другого углеродсодержащего сырья в модуле для газификации с косвенным нагревом и обеспечивает способ удаления конденсируемых органических материалов (смол) из получаемого газа с интегрированной стадией удаления смолы. Более конкретно, на данной стадии удаления смолы циркулирующий теплоноситель используется для крекинга органических соединений и получения дополнительного количества газа. Преимуществом данного способа и следствием того, что теплоноситель циркулирует по чередующимся паронасыщенной и окислительной зонам, является отсутствие дезактивации реакций крекинга.

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29-06-2012 дата публикации

СИСТЕМА УТИЛИЗАЦИИ ОТХОДОВ

Номер: EA0201290023A1
Принадлежит:

Предлагаются система (1) и способ комплексной утилизации отходов, предусматривающие использование источника (2) горючего отходного материала, сепараторной установки (3) для отделения горючего отходного материала от пригодного для вторичного использования материала, безвоздушной сушильной установки (4) для высушивания горючего отходного материала с целью получения сырья для пиролиза, пиролизной установки (5) для пиролиза сырья с целью формирования угля и пирогаза. Предлагаются система и способ генерации энергии, содержащие систему или способ утилизации отходов согласно изобретению и предусматривающие использование окислительной установки (7) для высокотемпературного окисления синтез-газа, получаемого из сырья для пиролиза, с целью генерации тепла для производства энергии.

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29-04-2011 дата публикации

МНОГОЗОНАЛЬНЫЙ УГЛЕРОДНЫЙ КОНВЕРТОР С ПЛАЗМЕННОЙ ПЛАВКОЙ

Номер: EA0201001375A1
Принадлежит:

Предлагается многозональный углеродный конвертор для преобразования обработанного сырья в синтез-газ и шлак, включающий в себя камеру с зоной конверсии углерода, контактирующей со шлаковой зоной для плавления золы в расплавленный шлак и/или для поддержания шлака в расплавленном состоянии посредством плазменного нагрева. Зоны конверсии углерода и шлака разделены межзональной областью, содержащей преграду для воспрепятствования или ограничения движения материала между этими двумя зонами. Межзональная область может также обеспечивать начальное плавление золы в расплавленный шлак посредством переноса плазменного нагрева из шлаковой зоны.

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30-11-2016 дата публикации

GASIFICATION AND MELTING PLANT

Номер: EA0201691325A1
Автор:
Принадлежит:

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30-08-2011 дата публикации

СПОСОБ И СИСТЕМА ДЛЯ ПРОИЗВОДСТВА ЧИСТОГО ГОРЯЧЕГО ГАЗА НА ОСНОВЕ ТВЕРДЫХ ТОПЛИВ

Номер: EA201170390A1
Принадлежит:

Твердое топливо можно преобразовать в чистый горячий печной газ с низким содержанием летучих органических соединений (ЛОС), NOx и пыли, а также чистой золы с низким содержанием углерода, посредством термического реактора, разделенного на стадии, где процесс конверсии твердого топлива осуществляют в отдельных вертикальных стадиях (снизу вверх): выгорание золы, окисление и превращение в газ угля, пиролиз, стадия сушки и сжигания газа, где сжигается газ из газогенератора.

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10-11-2010 дата публикации

PROCESS AND SYSTEM FOR GASIFICATION WITH IN-SITU TAR REMOVAL

Номер: GE0P20105115B
Принадлежит:

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29-06-1988 дата публикации

Treatment of waste and rotary kiln therefor

Номер: CN0087107033A
Принадлежит:

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31-01-2020 дата публикации

Efficient pyrolyzing garbage device

Номер: CN0107300176B
Автор:
Принадлежит:

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23-06-1978 дата публикации

INSTALLATION ET PROCEDE POUR L'INCINERATION DES RESIDUS

Номер: FR0002372389A
Автор:
Принадлежит:

... a. Installation pour incinération des résidus. b. Des fûts sont ouverts et sont basculés de 180 degrés par un basculeur 3a, 3b sur les raccords 5a, 5b de chargement. Après que les dispositifs de fermeture du basculeur et des raccords ont été ouverts, les résidus parviennent dans la chambre de pyrolyse et s'amoncellent sur les sas 10a, 10b de passage vers la chambre inférieure d'incinération. c. Industrie nucléaire.

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02-04-1999 дата публикации

ENERGY INSTALLATION OF VALORIZATION OF URBAN WASTE AND ASSIMILATE

Номер: FR0002758748B1
Принадлежит: GEC Alsthom Stein Industrie

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31-07-1998 дата публикации

ENERGY INSTALLATION OF VALORIZATION OF URBAN WASTE AND ASSIMILATE

Номер: FR0002758747A1
Принадлежит:

La présente invention concerne une installation de valorisation énergétique de déchets urbains et assimilés comportant: - un dispositif de broyage (1) des déchets dont les refus sont évacués, - un réacteur à lit fluidisé circulant (2) recevant les déchets broyés par une conduite d'alimentation et comportant un lit fluidisé dense latéral situé sur la paroi du réacteur comportant la conduite d'alimentation en déchets broyés, un conduit d'extraction des éléments lourds non fluidisables étant situé à la base de ce lit fluidisé dense latéral et amenant ceux-ci dans un dispositif trieur de grosses particules (3) refroidissant ces éléments et extrayant les matières inertes non fluidisables, les autres matières étant réintroduites dans le réacteur (2), - un agencement de récupération d'énergie et de traitement des fumées sortant dudit réacteur (2). Selon l'invention, au moins une partie desdits refus sont introduits dans ledit dispositif trieur de grosses particules (3).par ...

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15-08-2014 дата публикации

BASKET FIBERGLASS AND PROCESS FOR THE INCINERATION OF WASTE

Номер: FR0003002075A1
Принадлежит:

Le panier selon l'invention permet d'incinérer des déchets durant une durée supérieure à quinze minutes dans un incinérateur sans que les déchets ne soient fondus au préalable, notamment lors de leur insertion dans l'incinérateur. Le panier est constitué principalement d'une enveloppe (10) en fibre de verre : il est, de préférence, renforcé par une structure légère métallique (12) placée à l'extérieur ou à l'intérieur de celle-ci ou intégrée à celle-ci. Une anse de préhension (14) surmonte l'ensemble qui est rigidifié, en haut par un tube métallique (16) auquel est fixée la structure légère métallique (12) et par une base constituée d'une lèchefrite (18) fixé à la base de la structure légère métallique (12). Application à l'incinération des déchets toxiques.

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24-09-2019 дата публикации

METHOD AND EQUIPMENT FOR TREATMENT OF BLACK LIQUOR AT PULP MILL

Номер: BR112012010606A2
Принадлежит:

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19-04-2012 дата публикации

DEVICE FOR THE CONVERSION OF A FUEL

Номер: WO2012049400A1
Принадлежит:

The invention relates to a device for the conversion of a fuel comprising solid components, referred to as solid fuel, into a gaseous fuel. Said device comprises a zone (2) for pyrolysis of the solid fuel comprising pyrolysis means that make it possible to decompose said solid fuel into a pyrolysis gas and into a solid pyrolysis residue, referred to as coke, a zone (3) for combustion of said pyrolysis gas, different from the pyrolysis zone (2), comprising combustion means (31, 32, 33). The device also comprises means for circulating the pyrolysis gas from said pyrolysis zone (2) to the combustion zone (3). According to the invention, said combustion zone (3) is surrounded by said pyrolysis zone (2).

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30-08-2012 дата публикации

HEAT REMOVAL AND RECOVERY IN BIOMASS PYROLYSIS

Номер: WO2012115754A3
Принадлежит:

Pyrolysis methods and apparatuses that allow effective heat removal, for example when necessary to achieve a desired throughput or process a desired type of biomass, are disclosed. According to representative methods, the use of a quench medium (e.g., water), either as a primary or a secondary type of heat removal, allows greater control of process temperatures, particularly in the reheater where char, as a solid byproduct of pyrolysis, is combusted. Quench medium may be distributed to one or more locations within the reheater vessel, such as above and/or within a dense phase bed of fluidized particles of a solid heat carrier (e.g., sand) to better control heat removal.

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19-01-2012 дата публикации

CHAR-HANDLING PROCESSES IN A PYROLYSIS SYSTEM

Номер: WO2012009207A3
Принадлежит:

Char-handling processes for controlling overall heat balance, ash accumulation, and afterburn in a reheater are provided. Carbonaceous biomass feedstock is pyrolyzed using a heat transfer medium forming pyrolysis products and a spent heat transfer medium. The spent heat transfer medium is separated into segregated char and char-depleted spent heat transfer medium. The char-depleted spent heat transfer medium is introduced into a dense bed of heat transfer medium fluidized by a stream of oxygen-containing regeneration gas. All or a portion of the segregated char is combusted in the dense bed using the stream of oxygen-containing regeneration gas. A portion of the segregated char may be exported out of the pyrolysis system to control the overall heat balance and ash accumulation.

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08-12-2005 дата публикации

IMPROVED GASIFIER

Номер: WO2005116524A1
Автор: STEIN, Peter
Принадлежит:

An apparatus and process for converting carbonaceous or other material with calorific value into high quality gas preferably to fuel a reciprocating gas engine for the generation of electricity. Wet fuel is delivered via conveyer (13) to fuel hopper (14). From the hopper the fuel is fed into the dryer (15) by a screw feeder. The dried fuel then is checked for size via a trammel (16) where the correctly sized fuel passes through and the oversized fuel goes onto the reject conveyer (22) where it is delivered for shredding. The correct sized dry fuel is transported via a conveyer (17). The fuel is then fed via a feed system, to avoid the ingress of air, into the gasifier (19) provided with an innovative internal vane configuration. The gas is cooled and cleaned in the gas quench unit (20).

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21-07-2005 дата публикации

WASTES PROCESSING AND RECYCLING METHOD

Номер: WO2005066315A1
Автор: CANTEGRIL, Marc
Принадлежит:

The inventive wastes processing and recycling method for gasifying a wastes flow (FxE) in overheated steam involves a preliminary pyrolisis stage for delivering pyrolisis gases (103) and carbon-containing solid materials (101, 102) at the output which is followed by a stage (303) for pyrolysis gas steam cracking and a stage for gasifying the carbon-containing solid materials for delivering, at the output, a clean gas (Ge) for storing and recycling. Said gasification stage consists in transferring and injecting the carbon-containing solid materials and the pyrolysis cracked gases to a vertical saturated fluidised bed incinerator (301), said gases being used as fluidisation media in said furnace and the carbon-containing solid materials being mixed with the sand bed thereof. Carbon-containing wastes are air-gasified in an air gasification furnace (306) which supplies a hot sand (308) to the furnace (301).

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30-05-2000 дата публикации

Feeding systems for a continuous pyrolysis and gasification process and apparatus

Номер: US6067915A
Автор:
Принадлежит:

PCT No. PCT/GB96/02618 Sec. 371 Date Apr. 27, 1998 Sec. 102(e) Date Apr. 27, 1998 PCT Filed Oct. 25, 1996 PCT Pub. No. WO97/15640 PCT Pub. Date May 1, 1997A method of charging a pyrolytic gas-producing reactor with waste fuel wherein the waste fuel is forced into the reactor by a ram and wherein air is prevented from entering the reactor and pyrolysis gases are prevented from escaping from the reactor by means of an ablative seal which is positioned between the fuel and the ram and which is forced by the action of the ram on the fuel charge into the reactor whilst in sealing engagement with the internal walls of the reactor, the seal being made of a material which will resist the high temperature and chemical conditions in the reactor for at least as long a period as is required for the seal to perform its sealing function and which is thereafter thermally decomposed into products which are not detrimental to the pyrolytic process or to the pyrolytic gases produced by the reactor. Also ...

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18-05-2011 дата публикации

Device and method for creating a gas

Номер: EP2251399A3
Автор: Bosch, Klaus
Принадлежит:

Die vorliegenden Erfindung betrifft ein Verfahren zur Erzeugung eines Gases durch Vergasung von Brennstoffen, insbesondere biogenen Brennstoffen und/oder Kunststoffen, in einem Reaktor umfassend eine Vergasungs- und eine Verbrennungszone, wobei der Reaktor ein fluidisiertes Bettmaterial aufweist, welches kontinuierlich in erhitztem Zustand von der Verbrennungszone in die Vergasungszone und von der Vergasungszone im abgekühlten Zustand zusammen mit nicht vergastem Restbrennstoff zurück in die Verbrennungszone geführt wird, wobei der Brennstoff in die als zirkulierende Wirbelschicht ausgebildete Vergasungszone eingebracht wird, der Brennstoff in der zirkulierenden Wirbelschicht der Vergasungszone bei Luftabschluss unter Bildung eines Produktgases zumindest teilweise ent- bzw. vergast wird und der verbliebene bzw. nicht umgesetzte Restbrennstoff zusammen mit dem abgekühlten Bettmaterial in die Verbrennungszone verbracht wird, wo das Bettmaterial unter Bildung eines schnellen Wirbelbettes fluidisiert ...

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01-10-2008 дата публикации

A HYBRID ENERGY CONVERSION SYSTEM AND PROCESSES

Номер: EP1973840A2
Принадлежит:

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11-02-1998 дата публикации

METHOD AND APPARATUS FOR PRODUCING SUPERHEATED STEAM USING HEAT GENERATED THROUGH INCINERATION OF WASTES

Номер: EP0000823590A1
Принадлежит:

Method and apparatus for producing superheated steam using heat generated through incineration of wastes in which boiler water is used that is pressurized so as to have a boiling point of about 200 to 320 °C, the heating of the boiler water being effected in a plurality of steps, at least two steps, in which the heating of the boiler water up to the boiling point is effected by chlorine containing thermal energy, and in which super-heating from the boiling point to a predetermined temperature to obtain superheated steam is effected by dechlorinated thermal energy, the method and apparatus being characterized in that the heating by the chlorine containing thermal energy is effected by using thermal energy obtained through combustion of pyrolysis gas that is obtained by thermal decomposition means for effecting a pyrolytic reaction by supplying wastes into a space containing a fluid medium having a temperature of 300 °C or greater, and in that the heating by the dechlorinated thermal energy ...

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19-07-2000 дата публикации

MATERIAL CONTROLLED PROCESSING APPARATUS AND METHOD

Номер: EP0000757773B1
Принадлежит: Bio-Oxidation Inc.

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20-04-2008 дата публикации

СПОСОБ ПЕРЕРАБОТКИ КОНДЕНСИРОВАННОГО ГОРЮЧЕГО ПУТЕМ ГАЗИФИКАЦИИ И УСТРОЙСТВО ДЛЯ ЕГО ОСУЩЕСТВЛЕНИЯ

Номер: RU2322641C2

FIELD: processing of condensed fuels. SUBSTANCE: method comprises charging fuel into the cylindrical reactor, supplying the oxygen-containing gasifying agent to the reactor from the side of reactor where the solid products of processing are collected, setting the fuel charged in motion along the axis of the reactor, discharging solid products of processing from the reactor, discharging the drying products from the reactor, and pyrolysis and combustion of gas product so that the fuel is gasified in the heating and drying zone, pyrolysis zone, combustion (oxidation) zone, and cooling zone. The gas is filtered by flowing though the layer of the charged fuel, thus flowing through the cooling zone, combustion zone, pyrolysis zone, and zone of heating and drying in series. The burning is stabilized by means of rotation of the reactor around its axis inclined to horizon under an angle from 22 to 65°. The device for processing of condensed fuel is also presented. EFFECT: enhanced efficiency. 12 cl, 1 dwg, 1 ex ÐÎÑÑÈÉÑÊÀß ÔÅÄÅÐÀÖÈß RU (19) (11) 2 322 641 (13) C2 (51) ÌÏÊ F23G 5/027 (2006.01) F23G 5/20 (2006.01) F27B 7/00 (2006.01) ÔÅÄÅÐÀËÜÍÀß ÑËÓÆÁÀ ÏÎ ÈÍÒÅËËÅÊÒÓÀËÜÍÎÉ ÑÎÁÑÒÂÅÍÍÎÑÒÈ, ÏÀÒÅÍÒÀÌ È ÒÎÂÀÐÍÛÌ ÇÍÀÊÀÌ (12) ÎÏÈÑÀÍÈÅ ÈÇÎÁÐÅÒÅÍÈß Ê ÏÀÒÅÍÒÓ (21), (22) Çà âêà: 2006114599/03, 02.05.2006 (24) Äàòà íà÷àëà îòñ÷åòà ñðîêà äåéñòâè ïàòåíòà: 02.05.2006 (43) Äàòà ïóáëèêàöèè çà âêè: 27.11.2007 (45) Îïóáëèêîâàíî: 20.04.2008 Áþë. ¹ 11 C 2 2 3 2 2 6 4 1 Àäðåñ äë ïåðåïèñêè: 142432, Ìîñêîâñêà îáë., ã. ×åðíîãîëîâêà, ïðêò Àêàä. Ñåìåíîâà, 1, äèðåêòîðó ÈÏÕÔ ÐÀÍ, àêàäåìèêó Ñ.Ì. Àëäîøèíó C 2 R U (73) Ïàòåíòîîáëàäàòåëü(è): Íåêîììåð÷åñêà îðãàíèçàöè Ó÷ðåæäåíèå Èíñòèòóò ïðîáëåì õèìè÷åñêîé ôèçèêè Ðîññèéñêîé àêàäåìèè íàóê (ñòàòóñ ãîñóäàðñòâåííîãî ó÷ðåæäåíè (ÈÏÕÔ ÐÀÍ) (RU) (54) ÑÏÎÑÎÁ ÏÅÐÅÐÀÁÎÒÊÈ ÊÎÍÄÅÍÑÈÐÎÂÀÍÍÎÃÎ ÃÎÐÞ×ÅÃÎ ÏÓÒÅÌ ÃÀÇÈÔÈÊÀÖÈÈ È ÓÑÒÐÎÉÑÒÂÎ ÄËß ÅÃÎ ÎÑÓÙÅÑÒÂËÅÍÈß (57) Ðåôåðàò: Èçîáðåòåíèå îòíîñèòñ ê ìåòîäàì ïåðåðàáîòêè êîíäåíñèðîâàííûõ òîïëèâ, â òîì ÷èñëå òâåðäûõ ãîðþ÷èõ îòõîäîâ, ïóòåì ...

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20-09-2002 дата публикации

СПОСОБ ПЕРЕРАБОТКИ МАТЕРИАЛА, ВКЛЮЧАЮЩЕГО В СЕБЯ АЛЮМИНИЙ И ПЛАСТМАССУ

Номер: RU2189310C2

FIELD: processing of waste materials including combinations of aluminium and plastic. SUBSTANCE: method for processing of material including combinations of aluminium and plastic, for example, bottle caps having a plastic coating, consists in pyrolysis of plastic in an inert atmosphere by heating to a temperature of about 550 C and cracking of gases or vapors that are released in the process of pyrolysis, reburning of coke remaining on aluminium in the process of pyrolysis is accomplished. The invention provides for a device for processing of material including combinations of aluminium and plastic, containing a means for pyrolysis, provided with a heater for heating to a temperature equal approximately to 550 C, charging devices for bottle caps with a plastic coating that are to be processed, and a discharging device of aluminium material. The device is provided with a device for reburning of coke residues adhered to aluminium material connected to the device for unloading of the means for pyrolysis made in the form of a drum. EFFECT: produced closed cycle of processing of old bottle cap and production of new aluminium caps with a plastic coating. 10 cl, 1 dwg огсезгс пы сэ РОССИЙСКОЕ АГЕНТСТВО ПО ПАТЕНТАМ И ТОВАРНЫМ ЗНАКАМ (19) ВИ "” 2 189 310 '” С2 (51) МПК? В 29 В 17/00, С 40В 53/00, Е 23 С 5/027/В 29 К 105:22, В 291 12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ РОССИЙСКОЙ ФЕДЕРАЦИИ (21), (22) Заявка: 99128040/12, 29.05.1998 (24) Дата начала действия патента: 29.05.1998 (30) Приоритет: 30.05.1997 МЕ 1006179 (46) Дата публикации: 20.09.2002 (56) Ссылки: УР 56-133432 А, 19.10.1981. КЦ 94031022 А, 10.07.1996. КЦ 2081372 СЛ, 10.06.1997. 4$ 3650830 А, 21.03.1972. ОЕ 3909696 АЛ, 27.09.1990. МАКАРОВ В.М. и др. Использование амортизированных шин и отходов производства резиновых изделий. - Л.: Химия, 1986, с.215-218. АЛЕКСЕЕВ Г.М. и др. Индустриальные методы санитарной очистки городов. Л.: Стройиздат, 1983, с.19-21, 9-15. (85) Дата перевода заявки РСТ на национальную фазу: 30.12. ...

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27-04-2016 дата публикации

ТЕПЛООТВОД И ВЫДЕЛЕНИЕ ПРИ ПИРОЛИЗЕ БИОМАССЫ

Номер: RU2582607C2

Изобретение относится к пиролизу и установке, в которой твердый теплоноситель отделяют от продуктов реакции пиролиза и охлаждают при помощи закалочной среды для улучшения регулирования температуры. Закалочную среду применяют в качестве либо первичного, либо вторичного типа теплоотвода, что позволяет в большей степени регулировать температуру способа, в частности, в подогревателе, в котором сжигают древесный уголь в качестве твердого побочного продукта пиролиза. Закалочную среду распределяют в одно или более местоположений внутри резервуара подогревателя, например, поверх и/или внутри слоя плотной фазы псевдоожиженных частиц твердого теплоносителя для лучшего регулирования теплоотвода. Технический результат - создание способов пиролиза с улучшенным теплопереносом. 3 н. и 7 з.п. ф-лы, 2 ил.

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10-07-2015 дата публикации

СПОСОБ И УСТРОЙСТВО ДЛЯ ОБРАБОТКИ ОТХОДОВ

Номер: RU2554970C2

FIELD: process engineering. SUBSTANCE: invention relates to disposal of, particularly, municipal waste. Waste processing process for production of synthesis-gas comprises the step of pyrolysis. This step includes processing of wastes in pyrolysis unit to get the offgas and solid coal material not suspended in said offgas. This process comprises plasma processing step consisting in plasma processing of off gas and solid coal material at plasma processing unit in the presence of oxygen and, if required, steam. Note here that said plasmas processing unit is separated from pyrolysis plant. EFFECT: decreased amount of solid wastes and harmful materials in processed gases. 15 cl, 5 dwg, 6 tbl РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 554 970 C2 (51) МПК F23G 5/027 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ (21)(22) Заявка: ИЗОБРЕТЕНИЯ К ПАТЕНТУ 2011100145/03, 11.01.2011 (24) Дата начала отсчета срока действия патента: 29.06.2006 Приоритет(ы): (30) Конвенционный приоритет: (73) Патентообладатель(и): ЭДВАНСТ ПЛАЗМА ПАУЭР ЛИМИТЕД (GB) (45) Опубликовано: 10.07.2015 Бюл. № 19 2 5 5 4 9 7 0 R U 2004060587 A1, 22.07.2004. БЕРНАДИНЕР М.Н. и др., Огневая переработка и обезвреживание промышленных отходов, Москва, "Химия", 1990, с.18,19. JP 2003147373 A, 21.05.2003 Адрес для переписки: 129090, Москва, ул. Б. Спасская, 25, строение 3, ООО "Юридическая фирма Городисский и Партнеры" (54) СПОСОБ И УСТРОЙСТВО ДЛЯ ОБРАБОТКИ ОТХОДОВ (57) Реферат: Изобретение относится к способу обработки получения отходящего газа и не взвешенного в отходов, особенно городских отходов. отходящем газе твердого угольного материала, Техническим результатом является уменьшение и стадию плазменной обработки, содержащую количества твердых отходов, которые плазменную обработку отходящего газа и не получаются в результате процесса обработки взвешенного в отходящем газе твердого отходов, а также уменьшение количества опасных угольного материала в установке для плазменной материалов в ...

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20-03-2015 дата публикации

СПОСОБ ПЕРЕРАБОТКИ ГОРЮЧИХ УГЛЕРОД- И/ИЛИ УГЛЕВОДОРОДСОДЕРЖАЩИХ ПРОДУКТОВ И РЕАКТОР ДЛЯ ЕГО ОСУЩЕСТВЛЕНИЯ

Номер: RU2544669C1

FIELD: chemistry. SUBSTANCE: method for processing combustible carbon- and/or hydrocarbon-containing products involves sequential layered furnace-charge processing in a reactor in the presence of a catalyst. In the reactor, the furnace charge drives top down through heating zones of refinement (9), pyrolysis (8), carbonisation (7), burning (6) products to generate a solid residue unloaded from a solid residue unload zone (2) with an unload window (3) from a working chamber of the reactor in cycles paying attention to keep it sealed. The sealed working chamber (1) of the reactor comprises a supply zone of wet fine particles of waste solid fuel including pyrolysis and carbonisation (14) integrated with oxygen agent supply (4) and heating (5) zones. An oxygen agent supply channel (15) is coupled with a dosage tank (16) of wet fine particles of waste solid fuel, which are used to generate a fluid flow in the zone (14) of the reactor. An additional amount of the oxygen agent is additionally supply into the reactor as a part of the basic flow; the amount is expected to be adequate to make fine particles of waste solid fuel burn in the following after the pyrolysis (8) and carbonisation (7) zones and transform their moisture into overheated vapour. EFFECT: inventions provide the complete recycling of fine fractions of processing products, enable producing high-calorie gas and increasing yield and quality of the finished products. 6 cl, 1 dwg, 2 tbl, 1 ex РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 544 669 C1 (51) МПК C10B 49/02 (2006.01) C10J 3/72 (2006.01) F23G 5/027 (2006.01) C10B 53/00 (2006.01) C10B 57/00 (2006.01) B09B 3/00 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ (21)(22) Заявка: ИЗОБРЕТЕНИЯ К ПАТЕНТУ 2014103344/05, 03.02.2014 (24) Дата начала отсчета срока действия патента: 03.02.2014 (45) Опубликовано: 20.03.2015 Бюл. № 8 (56) Список документов, цитированных в отчете о поиске: RU 2385343 C1, 27.03.2010; . RU (73) Патентообладатель(и ...

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20-07-2012 дата публикации

СПОСОБ И УСТРОЙСТВО ДЛЯ ОБРАБОТКИ ОТХОДОВ

Номер: RU2011100145A
Принадлежит:

... 1. Способ обработки отходов, содержащий: ! (i) стадию пиролиза, содержащую обработку отходов в установке для пиролиза для получения отходящего газа и не взвешенного в воздухе, твердого угольного материала; и ! (ii) стадию плазменной обработки, содержащую плазменную обработку отходящего газа и не взвешенного в воздухе, твердого угольного материала в установке для плазменной обработки в присутствии кислорода и, по выбору, пара, при этом установка для плазменной обработки отделена от установки для пиролиза. ! 2. Способ по п.1, дополнительно содержащий, стадию, на которой подвергают отходы микробиологической обработке, которая предпочтительно является стадией аэробной микробиологической обработки, до стадии пиролиза. ! 3. Способ по п.1, при котором стадию пиролиза проводят при температуре 400°С или более. ! 4. Способ по п.1, при котором отношение кислорода к пару на стадии плазменной обработки составляет по весу от 10:1 до 2:5. ! 5. Способ по п.1, дополнительно содержащий стадию сушки отходов ...

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20-12-2013 дата публикации

СПОСОБ И УСТРОЙСТВО ДЛЯ ОБРАБОТКИ ЧЕРНОГО ЩЕЛОКА ЦЕЛЛЮЛОЗНОГО ПРОИЗВОДСТВА

Номер: RU2012123390A
Принадлежит:

... 1. Способ обработки черного щелока целлюлозного производства для регенерации содержащихся в нем химических реагентов и энергии, отличающийся стадиями, в которых- вводят черный щелок в пиролитический реактор, включающий по существу не содержащую кислорода камеру,- подают в пиролитический реактор каустифицирующий материал, который состоит из оксида натрия (NaO) и оксида металла (MO) и который нагрет в топочном устройстве, в результате чего черный щелок подвергается газификации и образует газообразные компоненты и остаточное твердое вещество,- направляют газообразные компоненты, образовавшиеся в пиролитическом реакторе, на дальнейшую утилизацию,- транспортируют твердое вещество, образовавшееся в пиролитическом реакторе, в топочное устройство, где содержащееся в нем горючее вещество выгорает с помощью кислорода, содержащегося в воздухе, подводимом в топочное устройство, и остается каустифицирующий материал, состоящий из оксида натрия (NaO) и оксида металла (MO),- возвращают часть каустифицирующего ...

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26-09-1996 дата публикации

Carbonising waste to form e.g. pyrolysis prod.

Номер: DE0019510390A1
Принадлежит:

In the heat treatment of waste, the waste (A) is fed to a carbonisation drum (12a,12b) to form a pyrolysed material (f) and a carbonisation gas (s), non-carbonaceous fractions (w1-w4) are removed. The processed pyrolysis material (f') and the carbonisation gas (s) are fed to the combustion chamber (24) of a power plant (4), with a fuel (b), e.g. coal or coal dust, also being fed to the combustion chamber.

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28-08-1997 дата публикации

Evaluating residues and waste material in blast furnace

Номер: DE0019606575A1
Принадлежит:

Evaluating residues and waste material in a blast furnace comprises: (a) thermally treating the materials in a pyrolysis reactor by heating to 300-800 deg C to produce pyrolysis coke and pyrolysis gas; (b) mechanically processing the coke into fine granules; and (c) adding the finely ground coke and gas to the blast furnace.

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07-07-2005 дата публикации

Verfahren zur thermischen Behandlung und stofflichen Verwertung von Klärschlamm

Номер: DE0010224077B4
Принадлежит: FEUSTEL HANS ULRICH, FEUSTEL, HANS ULRICH

Verfahren zur thermischen Behandlung und stofflichen Verwertung von Klärschlamm durch Kompaktierung, Trocknung und Vergasung, geregelte Nachverbrennung der Ofengase und Aufschmelzen unter reduzierenden Bedingungen in einem mit Sauerstoff und/oder Verbrennungswind betriebenen Schacht-Schmelz-Vergaser oder Schacht-Schmelz-Ofen, gekennzeichnet dadurch, dass der beispielsweise aus den Kläranlagen für kommunale und/oder industrielle Wässer stammende Klärschlamm mit einer Feuchte von bis zu 85 % mit, bezogen auf die feuchte Masse Klärschlamm, bis 5 Zement, bis 5 % Kalk und bis 6 % Zuschlagstoffe mit dem Klärschlamm vermischt, in Formen zu Formkörpern mit einer Schacht-Schmelz-Ofen gerechten Größe verstampft oder verpresst, danach ausgelagert und nach einer Aushärtezeit bis zur Einstellung der Gattierungs- und Thermofestigkeit dem Schacht-Schmelz-Ofen zugeführt, in diesem stufenweise durch geregelte Verbrennungsmittelzufuhr und/oder geregelte Zufuhr anderer fester und/oder flüssiger und/oder gasförmiger ...

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03-08-2005 дата публикации

Waste treatment process and apparatus

Номер: GB0000513299D0
Автор:
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19-04-2006 дата публикации

Waste Treatment Process And Apparatus

Номер: GB0000604691D0
Автор:
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27-01-2021 дата публикации

Treatment of waste material

Номер: GB0002585873A
Принадлежит:

A method of treating comminuted waste material comprising heating comminuted waste material in a heating chamber 28 using one or more heating means (40 fig. 4) to generate a combustible gas, measuring or determining 29 the temperature in the heating chamber, comparing the temperature in the heating chamber with a predetermined temperature range and adjusting the amount of heat applied by the one or more heating means to the heating chamber to maintain the temperature in the heating chamber. The heating means may comprise a combustion means, where the amount of heat applied by the combustion means comprises varying the flow rate of air supplied, or varying the flow rate of fuel, or altering the ratio of components of a fuel mixture. The temperature may be measured by a sensor outside or inside the heating chamber. Steam may be introduced into the heating chamber. A portion of the combustible gas generated may be supplied or recirculated to the heating means for heating the chamber. The heating ...

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13-09-1972 дата публикации

Номер: GB0001289144A
Автор:
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15-12-2008 дата публикации

WASTE TREATMENT PROCEDURE AND - DEVICE

Номер: AT0000417229T
Принадлежит:

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15-10-2010 дата публикации

VERFAHREN UND VORRICHTUNG ZUR ERZEUGUNG EINES GASES

Номер: AT0000508002B1
Автор:
Принадлежит:

Die vorliegenden Erfindung betrifft ein Verfahren zur Erzeugung eines Gases durch Vergasung von Brennstoffen, insbesondere biogenen Brennstoffen und/oder Kunststoffen, in einem Reaktor umfassend eine Vergasungs- und eine Verbrennungszone, wobei der Reaktor ein fluidisiertes Bettmaterial aufweist, welches kontinuierlich in erhitztem Zustand von der Verbrennungszone in die Vergasungszone und von der Vergasungszone im abgekühlten Zustand zusammen mit nicht vergastem Restbrennstoff zurück in die Verbrennungszone geführt wird, wobei der Brennstoff in die als zirkulierende Wirbelschicht ausgebildete Vergasungszone eingebracht wird, der Brennstoff in der zirkulierenden Wirbelschicht der Vergasungszone bei Luftabschluss unter Bildung eines Produktgases zumindest teilweise ent- bzw. vergast wird und der verbliebene bzw. nicht umgesetzte Restbrennstoff zusammen mit dem abgekühlten Bettmaterial in die Verbrennungszone verbracht wird, wo das Bettmaterial unter Bildung eines schnellen Wirbelbettes fluidisiert ...

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15-05-1993 дата публикации

DISPOSAL UNIT FOR CELEBRATIONS WASTE.

Номер: AT0000089065T
Принадлежит:

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15-01-1996 дата публикации

VERFAHREN UND SCHACHTOFEN ZUR UMSETZUNG KÖRNIGEN IONENTAUSCHERHARZES IN BRENNGAS

Номер: ATA17292A
Автор:
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15-03-1985 дата публикации

MECHANISM AND BURN OF FIRM AND IF NECESSARY ZUSÛTZLICH FLÙSSIGER OF WASTE MATERIALS

Номер: AT0000721777A
Автор:
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15-07-2003 дата публикации

PLANT TO THERMOLYSE AND FOR THE ENERGETIC UTILIZATION OF WASTE

Номер: AT0000244381T
Принадлежит:

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15-03-1994 дата публикации

PROCEDURE AND MECHANISM FOR THE TREATMENT OF SEWAGE SLUDGE.

Номер: AT0000101587T
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04-07-1994 дата публикации

Heat generator assembly for material processing

Номер: AU0005898494A
Принадлежит:

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26-07-2012 дата публикации

Process and system for gasification with in-situ tar removal

Номер: AU2006304867B2
Принадлежит: TAYLOR BIOMASS ENERGY LLC

The present invention relates to a process and system for gasifying biomass or other carbonaceous feedstocks in an indirectly heated gasifÊer and provides a method for the elimination of condensable organic materials (tars) from the resulting product gas with an integrated tar removal step. More specifically, this tar removal step utilizes the circulating heat carrier to crack the organics and produce additional product gas. As a benefit of the above process, and because the heat carrier circulates through alternating steam and oxidizing zones in the process, deactivation of the cracking reactions is eliminated.

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07-06-2011 дата публикации

METHOD FOR TREATMENT OF SPENT LIQUOR

Номер: CA0002491650C
Принадлежит: METSO POWER OY

Method for treatment of spent liquor at a pulp mill, in which method at least a part of the spent liquor flow (10) arriving from the evaporation plant is taken to a pyrolysis reactor (1), wherein it is pyrolysed at a temperature of 300-800~C in order to separate evaporable compounds (12) from coke (11) remaining in a solid state. The pyrolysis products (12), which are gases or liquids, may be used as fuel or they may be processed further. The coke (11) resulting from the pyrolysis is burnt in a soda recovery boiler (3) or in a gasification reactor (2) to regenerate cooking chemicals. The method is suitable for recovery of chemicals and energy both in sulphate and sulphite processes and also in cooking methods based on organic solvents.

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29-11-2018 дата публикации

MATERIALS RECYCLING APPARATUS

Номер: CA0003064693A1
Принадлежит: HICKS & ASSOCIATES

Materials recycling processes that include a combustion stage can operate very efficiently, but can produce exhaust gases that are high in carbon monoxide and the like. We describe a treatment unit which comprises a chamber for receiving the material, a heat source for (preferably) heat-treating the material and for initiating combustion, and a gas outlet from the chamber, which allows the gas that is exhausted via the outlet to be supplied to the air inlet of an associated boiler unit, with the air inlet and a separate fuel inlet feeding a burner for combusting fuel from the fuel inlet in air from the air inlet in order to heat a transfer fluid. In this way, the unburnt elements of the gas expelled from the chamber are included in the combustion process of the boiler unit and fully combusted. A corresponding method is also disclosed.

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07-01-2016 дата публикации

A GASIFIER

Номер: CA0002954107A1
Принадлежит:

There is disclosed a gasifier (500) comprising: a gasification chamber (518); a feedstock inlet (520) opening into the gasification chamber (518) for introducing feedstock material and primary combustible gas; a gas outlet (523) opening into the gasification chamber; and a flow path between the feedstock inlet (520) and the gas outlet (523) which passes through the gasification chamber (518), a portion of the flow path having an upwards component within the gasification chamber so that particulate material entrained in the primary combustible gas separates from the primary combustible gas and falls towards the bed of feedstock material. There is also disclosed a gasifier (500) comprising: a chamber wall (510) defining a gasification chamber (518); an ash grate (526) disposed in the gasification chamber (518); and a rotary crusher (532) disposed in the gasification chamber (518) above the ash grate (532) and provided with at least one crushing element (536); wherein in use rotation of the ...

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26-07-2007 дата публикации

A HYBRID ENERGY CONVERSION SYSTEM AND PROCESSES

Номер: CA0002637587A1
Принадлежит:

Disclosed are flexible hybrid conversion systems that can be used with a wide spectrum of resources and feedstock. The disclosed systems can be sufficiently versatile to provide many added value products including clean energy, synthetic fuels and chemical products. Processes and system disclosed herein can produce, for example, shaft power and/or electricity from the expansion of species change of hot, hydrogen-laden syngas produced by gasification or steam reforming of inferior feedstock such as coal, bitumen, tar from sands and wastes, including biomass, municipal solid waste (MSW) sewage sludge and certain industrial wastes. This disclosure also teaches innovative system thermal integration methods of endothermic and exothermic processes and reaction enhancement approaches for the economic, clean and flexible production of synthetic gaseous and liquid fuels as well as chemicals.

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08-11-2007 дата публикации

METHOD FOR PROCESSING CONDENSED FUEL BY GASIFICATION AND A DEVICE FOR CARRYING OUT SAID METHOD

Номер: CA0002650979A1
Принадлежит:

The invention relates to a method for processing condensed fuels, including solid fuel wastes, by pyrolysis and by gasifying the organic constituent thereof. The inventive method can be used for efficiently processing fuels, including fine-dispersed and easily sintering fuels. The inventive method consists in loading a condensed fuel in a reactor to which a gasifying oxygen-containing agent is supplied in a countercurrent manner, in organising a fuel pyrolysis in the reactor and, subsequently, in burning/gasifying pyrolysis carbon residues in the fuel dense layer. The reactor is embodied in the form of a rotary tilting furnace whose tilt angle to the horizon is equal to 22-65° and which is rotatable for stabilising a burning process. Combustible gases produced during pyrolysis and gasification can be used in the form of a fuel.

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24-06-1999 дата публикации

FUEL GASIFICATION SYSTEM

Номер: CA0002314986A1
Принадлежит:

An integrated gasifying furnace comprising a gasifying room (1) for gasifying a fluidized medium inside an interface-carrying fluidized bed, a char combustion room (2) for burning char generated by the gasification in the gasifying room and heating the fluidized medium inside a similar-interface-carrying fluidized bed and an energy recovery device (3), wherein (1) and (2) are constructed integrally and partitioned by a partition wall at a portion vertically above the interface of the fluidized bed and an opening for communication between (1) and (2) is provided at the lower portion of the partition wall, whereby the fluidized medium heated in (2) is moved from (2) to (1) through the opening. The above arrangement eliminates the need of any special pressure balance control or mechanical fluidized medium handling means between the gasifying room and the char combustion room, ensures a stable supply of a product gas of excellent quality, and provides a fuel gasification that allows a high ...

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28-06-2013 дата публикации

МНОГОЗОНАЛЬНЫЙ УГЛЕРОДНЫЙ КОНВЕРТОР С ПЛАЗМЕННОЙ ПЛАВКОЙ

Номер: EA0000018207B1

Предлагается многозональный углеродный конвертор для преобразования обработанного сырья в синтез-газ и шлак, включающий в себя камеру с зоной конверсии углерода, контактирующей со шлаковой зоной, для плавления золы в расплавленный шлак и/или для поддержания шлака в расплавленном состоянии посредством плазменного нагрева. Зоны конверсии углерода и шлака разделены межзональной областью, содержащей преграду для воспрепятствования или ограничения движения материала между этими двумя зонами. Межзональная область может также обеспечивать начальное плавление золы в расплавленный шлак посредством переноса плазменного нагрева из шлаковой зоны.

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12-10-2015 дата публикации

METHOD AND SYSTEM FOR PRODUCTION OF A CLEAN HOT GAS BASED ON SOLID FUELS

Номер: UA0000109765C2
Автор:
Принадлежит:

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30-04-2015 дата публикации

TECHNOLOGY EFFECTIVE AND PURE BURNING OF MACROMOLECULAR SUBSTANCES AND ITS EQUIPMENT

Номер: EA0201490685A1
Автор:
Принадлежит:

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25-06-2011 дата публикации

СПОСОБ, СИСТЕМА (ВАРИАНТЫ) И УСТРОЙСТВО ДЛЯ ГАЗИФИКАЦИИ БИОМАССЫ ИЛИ ДРУГОГО УГЛЕРОДСОДЕРЖАЩЕГО СЫРЬЯ, УСТРОЙСТВО ДЛЯ ОБРАБОТКИ СИНТЕЗ-ГАЗА

Номер: UA0000094919C2

Способ и устройства для газификации биомассы или другого углеродсодержащего сырья в модуле для газификации с непрямым нагреванием, которые обеспечивают извлечение конденсированных органических материалов (смол) из получаемого газа с интегрированной стадией извлечения смолы. На стадии извлечения смолы используется циркулирующий теплоноситель для крекинга органических соединений и получения дополнительного количества газа. Преимуществом данного способа и следствием того, что теплоноситель циркулирует паронасыщенной и окислительной чередующимися зонами, является отсутствие дезактивации реакций крекинга.

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28-02-2014 дата публикации

GASIFICATION AND MELTING INSTALLATION

Номер: EA0201391135A1
Автор:
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30-10-2008 дата публикации

СПОСОБ И СИСТЕМА ДЛЯ ГАЗИФИКАЦИИ С ВНУТРИЦИКЛОВЫМ УДАЛЕНИЕМ СМОЛЫ

Номер: EA0200801129A1
Принадлежит:

Настоящее изобретение относится к способу и устройству для газификации биомассы или другого углеродсодержащего сырья в модуле для газификации с косвенным нагревом и обеспечивает способ удаления конденсируемых органических материалов (смол) из получаемого газа с интегрированной стадией удаления смолы. Более конкретно, на данной стадии удаления смолы циркулирующий теплоноситель используется для крекинга органических соединений и получения дополнительного количества газа. Преимуществом данного способа и следствием того, что теплоноситель циркулирует по чередующимся паронасыщенной и окислительной зонам, является отсутствие дезактивации реакций крекинга.

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19-03-2014 дата публикации

Method and devices for burning macromolecular matters efficiently and cleanly

Номер: CN102322630B
Автор: LIU WEIQI
Принадлежит:

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31-12-2014 дата публикации

Fluidized-bed gasification method and facility therefor

Номер: CN0102124084B
Принадлежит:

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26-01-2007 дата публикации

METHOD FOR PROCESSING AND RECYCLING OF WASTE

Номер: FR0002863920B1
Автор: CANTEGRIL
Принадлежит: THALES

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20-09-1996 дата публикации

PROCESS AND INSTALLATION OF THERMOLYSIS OF WASTE

Номер: FR0002722436B1
Автор: MARTIN, MARTY
Принадлежит: IFP ENERGIES NOUVELLES

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14-06-2012 дата публикации

Waste management system

Номер: US20120145051A1
Автор: John Gerard Sweeney
Принадлежит: Individual

A system and method of integrated waste management having a source of a combustible waste material, a separator for separating the combustible waste material from a recyclable material, an airless drier for drying the combustible waste material to generate a pyrolysis feedstock, and a pyrolyser for pyrolysing the pyrolysis feedstock to form char and pyrogas. The system and method for power generation may also use an oxidiser for the high-temperature oxidation of syngas generated from the pyrolysis feedstock to generate heat for power production.

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05-12-2013 дата публикации

Gasification melting facility

Номер: US20130319300A1

This gasification melting facility includes: a fluidized bed gasification furnace that generates pyrolysis gas by thermally decomposing waste and discharges incombustibles; a vertical cyclone melting furnace that includes a pyrolysis gas duct through which the pyrolysis gas is introduced; a pyrolysis gas passage that connects the fluidized bed gasification furnace with the pyrolysis gas duct of the vertical cyclone melting furnace; pulverizer that pulverize the incombustibles into pulverized incombustibles so that the particle size of the incombustibles becomes fine; and airflow transporter that puts the pulverized incombustibles in the pyrolysis gas passage, and separating metal contained in the pulverized incombustibles by a difference in specific gravity while conveying the pulverized incombustibles together with airflow. The pyrolysis gas and the pulverized incombustibles are melted in the vertical cyclone melting furnace.

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12-12-2013 дата публикации

Char-Handling Processes in a Pyrolysis System

Номер: US20130327629A1
Принадлежит: Ensyn Renewables Inc

Char-handling processes for controlling overall heat balance, ash accumulation, and afterburn in a reheater are provided. Carbonaceous biomass feedstock is pyrolyzed using a heat transfer medium forming pyrolysis products and a spent heat transfer medium. The spent heat transfer medium is separated into segregated char and char-depleted spent heat transfer medium. The char-depleted spent heat transfer medium is introduced into a dense bed of heat transfer medium fluidized by a stream of oxygen-containing regeneration gas. All or a portion of the segregated char is combusted in the dense bed using the stream of oxygen-containing regeneration gas. A portion of the segregated char may be exported out of the pyrolysis system to control the overall heat balance and ash accumulation.

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13-02-2020 дата публикации

SEPARATED CHAMBERS PYROLYSIS FURNACE

Номер: US20200048559A1
Принадлежит:

The present invention is directed to an apparatus for domestic hot water and electricity production by the use of a natural organic fuel, the apparatus comprising a separated chambers pyrolysis furnace comprising: a) a pyrolysis chamber wherein the fuel is heated, substantially in the absence of oxygen at a temperature capable of causing pyrolysis of fuel; b) a combustion chamber of the pyrolyzed fuel, wherein the pyrolyzed fuel is burned in the presence of an air flux. The invention is also directed to an apparatus for the production of domestic hot water and electricity, which apparatus comprises: the above defined furnace; b) a heat exchanger connected to the exit of the exhausted gas, wherein domestic water is heated; c) a power generator connected with the exit of syngas, wherein syngas produced in the pyrolysis chamber is used as a fuel. 21250104020. Apparatus according to claim 1 , wherein the furnace comprises an entrance for the organic fuel claim 1 , an entrance () for air claim 1 , an exit () in the pyrolysis chamber () for syngas and an exit () in the combustion chamber () for the exhausted gas.320. Apparatus according to claim 1 , wherein in the combustion chamber () it is present a probe for the measurement of oxygen concentration claim 1 , preferably a lambda probe.420. Apparatus according to claim 3 , wherein the airflow inside the combustion zone () is regulated as a function of oxygen concentration.5. Apparatus according to claim 1 , wherein the natural organic fuel is selected from pellet claim 1 , chips claim 1 , hazelnut shells claim 1 , sawing claim 1 , biomasses.61050. Apparatus according to claim 1 , wherein the pyrolysis zone () consists of a cochlea claim 1 , and the syn-gas produced by pyrolysis is extracted through pipe () connected to an aspiration pump.72011401011. Apparatus according to claim 1 , wherein the combustion zone () is fed by a star valve () claim 1 , and the exhaust fumes pipe () is connected to the pyrolysis zone () ...

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21-05-2020 дата публикации

MATERIALS RECYCLING APPARATUS

Номер: US20200158334A1
Принадлежит:

Materials recycling processes that include a combustion stage can operate very efficiently, but can produce exhaust gases that are high in carbon monoxide and the like. We describe a treatment unit which comprises a chamber for receiving the material, a heat source for (preferably) heat-treating the material and for initiating combustion, and a gas outlet from the chamber, which allows the gas that is exhausted via the outlet to be supplied to the air inlet of an associated boiler unit, with the air inlet and a separate fuel inlet feeding a burner for combusting fuel from the fuel inlet in air from the air inlet in order to heat a transfer fluid. In this way, the unburnt elements of the gas expelled from the chamber are included in the combustion process of the boiler unit and fully combusted. A corresponding method is also disclosed. 1. Materials treatment apparatus comprising a treatment unit , a boiler unit and a control apparatus for the treatment unit ,the treatment unit comprising a chamber for receiving the material, a heat source for heat-treating the material and for initiating combustion of the material; and a gas outlet from the chamber;the boiler unit comprising a fuel inlet and an air inlet, each feeding a burner for combusting fuel from the fuel inlet in air from the air inlet in order to heat a fluid;wherein the gas outlet from the chamber feeds gas to the burner of the boiler unit i. activate the heat source thereby to initiate heat-treatment of the material in the chamber,', 'ii. optionally, extract pyrolysis products from the chamber,', 'iii. vent the chamber thereby to admit oxygen and initiate combustion of remaining material in the chamber, and', 'iv. allow exhaust of combustion products via the gas outlet to the boiler unit., 'wherein the control apparatus is adapted to2. Materials treatment apparatus according to in which the gas from the gas outlet of the chamber is blended with the fuel supply of the boiler unit and supplied via the fuel ...

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19-07-2018 дата публикации

High-temperature pyrolysis incineration apparatus

Номер: US20180202656A1
Автор: Bok Joo Yang
Принадлежит: Shin Poong Co Ltd

A high-temperature pyrolysis incineration apparatus that forces external air to a combustion chamber while burning an incineration processing material injected therein at a high temperature within a combustion chamber is provided. The apparatus includes an air-supply tube disposed at the center of the combustion chamber, a fuel supply pipe installed at an upper edge of the inside of the combustion chamber, a punching plate disposed at the bottom of the combustion chamber, a stirring rod rotatably installed at an upper surface of the punching plate using the air-supply tube as a fixing shaft, a heat recovery device disposed outside of the combustion chamber, and a circulation pipe extending from a lid of the combustion chamber to the outside that returns to a location corresponding to an upper portion of the stirring rod at a wall of the combustion chamber via the inside of the heat recovery device.

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03-08-2017 дата публикации

Waste Incinerator

Номер: US20170218274A1
Автор: Shizheng YU, Xiuying YU
Принадлежит: Individual

A waste incinerator, in a vertical structure and including from the top down: a drying section, a destructive distillation section, a reduction section, and a combustion section. The combustion section includes: two layers of grate bars, a first combustion layer, a second combustion layer, and a third combustion layer. The heat produced from the combustion in the combustion section is used to heat the carbide in the reduction section. The heated carbide reduces CO 2 produced in the combustion into CO (coal gas). The coal gas ascends to the destructive distillation section through the ambient coal gas chamber to heat and destructively distillate the waste to produce the pyrogenic coal gas and the carbide. The carbide drops to the combustion section for combustion, and the pyrogenic coal gas and the coal gas are collected by the draft fan.

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13-09-2018 дата публикации

APPARATUS FOR ENDOTHERMIC REACTIONS

Номер: US20180258349A1
Принадлежит:

A carbonaceous feed pyrolysis apparatus is provided including two or more hot particle fluidised beds, one of which contains a combustion zone, and one or more positive displacement apparatus for the transfer of hot particles beds. Also provided is a bio-oil production process including two or more fluidised beds, a first combustion zone carried out in one or more combustion fluidised beds in which a particulate material is fluidised and heated, and a second pyrolysis zone carried out in one or more pyrolysis fluidised beds in which hot particles heated in the combustion zone are used for pyrolysis of bio-mass, the combustion zone being operated at or about atmospheric pressure at a temperature of from 400° C. to 1100° C., and the pyrolysis zone being operated at a pressure of from atmospheric to 100 Barg at a temperature of from 400° C. to 900° C. 120-. (canceled)30. An endothermic reaction process , comprising: two or more fluidized bed zones comprising a first fluidized bed zone and a second fluidized bed zone;', 'a second fluidized bed zone gas feed comprising a closed gas loop configured such that, in use, a portion of a gas produced in the second fluidized bed zone is recycled in the closed gas loop to the first fluidized bed zone, such that the recycled gas is used as a gaseous fuel for the first fluidized bed zone, either fully or in part;', 'an apertured divider having one or more apertures therethrough connecting at least two of the fluidized bed zones;', 'a mass transfer device for transferring particulate matter from at least one fluidized bed zone to an other fluidized bed zone;', 'a gas loop purge configured such that, in use, a part of the recycled gas stream from the second fluidized bed zone is purged from the closed gas loop; and', 'a flow rate regulator configured to, in use, regulate a flow rate to a predeterminable rate;, 'providing an endothermic reaction apparatus, comprisingcombusting a carbonaceous material in a presence of oxygen in a hot ...

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11-12-2014 дата публикации

Apparatuses and Methods for Controlling Heat for Rapid Thermal Processing of Carbonaceous Material

Номер: US20140363343A1
Принадлежит: Ensyn Renewables Inc

Embodiments of apparatuses and methods for controlling heat for rapid thermal processing of carbonaceous material are provided herein. The apparatus comprises a reheater for containing a fluidized bubbling bed comprising an oxygen-containing gas, inorganic heat carrier particles, and char and for burning the char into ash to form heated inorganic particles. An inorganic particle cooler is in fluid communication with the reheater to receive a first portion of the heated inorganic particles. The inorganic particle cooler is configured to receive a cooling medium for indirect heat exchange with the first portion of the heated inorganic particles to form first partially-cooled heated inorganic particles that are fluidly communicated to the reheater and combined with a second portion of the heated inorganic particles to form second partially-cooled heated inorganic particles. A reactor is in fluid communication with the reheater to receive the second partially-cooled heated inorganic particles.

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13-07-2012 дата публикации

Pyrolysis apparatus using molten metal

Номер: KR101165403B1
Принадлежит: 한국생산기술연구원

PURPOSE: A pyrolysis device using liquid metal is provided to easily remove a char by selectively performing the char and oxidation and reduction of liquid metal because a temperature condition is properly controlled by controlling an air volume. CONSTITUTION: A pyrolysis device(100) using liquid metal comprises a hollow reactor(10), a circulating pump(20), a buffer tank(30), a plurality of nozzles(31), and an air supply source(40). The hollow reactor accommodate liquid metal(11). The circulating pump is connected to the reactor. The buffer tank receives the liquid metal from the circulating pump. The nozzles are joined to the buffer tank and spray the liquid metal of the buffer tank to inside of the reactor. The air supply source supplies air to the liquid metal of the reactor. A char generated from fuel of the reactor and liquid metal are reacted with air has flown in to the lower part of the reactor and burned.

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24-09-2008 дата публикации

Waste treatment method and waste treatment apparatus

Номер: JP4154029B2
Принадлежит: Toshiba Corp

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22-11-1994 дата публикации

Fluidized bed reactor and system and method utilizing same

Номер: US5365889A
Автор: John T. Tang
Принадлежит: Foster Wheeler Energy Corp

A fluidized bed reactor and system and method utilizing same for the combustion of waste fuels in which the reactor vessel is divided into three vessels. Waste fuel is introduced into the fluidized bed within one vessel where it is mixed with bed make-up material that is controlled to provide an ideal environment for the generation of pyrolytic gases. The fluidized bed material is pneumatically and gravitationally conveyed downwardly, and injected into a fluidized bed within the second vessel where the involatile organic material undergoes combustion in an oxidizing atmosphere. The bed material in the second vessel is pneumatically conveyed upwardly and divided into two portions, one of which is recycled back to the first vessel. The other portion of the bed material in the second vessel is circulated to a fluidized bed within the third vessel where heat is recovered. The bed material in the heat recovery vessel is gravitationally conveyed back to the second vessel to regulate the temperature in the latter vessel.

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30-11-2001 дата публикации

Method and equipment for disposing wastes

Номер: KR100315592B1

본 발명은 폐기물의 가스화 처리를 효율 좋게 할 수 있는 동시에, 유해 물질이 되는 다이옥신 및 염소 가스 등이 환경으로 배출되는 것을 방지할 수 있는 폐기물의 처리 방법 및 폐기물 처리 장치를 제공한다. 또 폐기물을 열에너지로 변환하여 전기 에너지로서 유효하게 활용하는 동시에, 2차 폐기물의 양을 대폭적으로 삭감할 수 있는 폐기물의 처리 방법 및 폐기물 처리 장치를 제공한다. The present invention provides a waste treatment method and a waste treatment apparatus that can make gasification of waste efficiently and can prevent the release of dioxins, chlorine gas, etc., which are hazardous substances, into the environment. The present invention also provides a waste treatment method and a waste treatment apparatus capable of converting waste into thermal energy to effectively use it as electrical energy and at the same time significantly reducing the amount of secondary waste. 본 발명의 폐기물의 처리 방법은 유기물을 포함하는 폐기물(a)을 공기를 차단한 상태에서 건류하여 열분해 가스(b)와 건류 잔류물(c)로 분리하는 열분해 공정과, 열분해 가스(b)를 열분해함으로써 저분자의 탄화수소를 함유하는 개질 가스(e)를 얻는 가스 개질 공정과, 건류 잔류물(c)을 냉각하여 고형화하는 잔류물 냉각 공정과, 이 고형화한 건류 잔류물을 분쇄 및 선별하여 열분해 차콜(g)을 얻는 기계적 처리 공정과, 이 열분해 차콜(g)을 도입하여 고온 연소를 하여 무기질 성분을 용융시키는 동시에 저분자의 탄화수소를 함유하는 가스화 가스(i)를 얻는 용융 가스화 공정을 갖는 것을 특징으로 한다. The waste treatment method of the present invention comprises a pyrolysis step of distilling waste (a) containing organic matter into a pyrolysis gas (b) and a dry distillation residue (c) in a state in which air is blocked, and a pyrolysis gas (b). A gas reforming step of obtaining a reformed gas (e) containing a low molecular hydrocarbon by pyrolysis, a residue cooling step of cooling and solidifying the dry residue (c), and a pyrolysis char by pulverizing and selecting the solidified dry residue. a mechanical treatment step of obtaining (g) and a melt gasification step of introducing the pyrolysis char (g) to perform high temperature combustion to melt the inorganic components and to obtain a gasification gas (i) containing low molecular hydrocarbons. do.

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20-07-2011 дата публикации

Procedure and device for treatment of waste

Номер: RU2424468C2

FIELD: oil and gas production. SUBSTANCE: procedure for treatment of waste consists in: stage of gasification corresponding to treatment of waste in installation for gasification at presence of oxygen and steam for production of end gas and solid coal material not suspended in end gas and in stage of plasma treatment corresponding to plasma processing end gas and solid coal material not suspended in end gas in installation for plasma treatment at presence of oxygen and, by choice, of steam. Also, the installation for plasma treatment is separated from installation of gasification. EFFECT: production of burning gas with low content of suspended particles, resin gaseous hydrocarbons and other harmful substances. 43 cl, 5 dwg, 6 tbl, 2 ex РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) 2 424 468 (13) C2 (51) МПК F23G 5/027 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ, ПАТЕНТАМ И ТОВАРНЫМ ЗНАКАМ (12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ (21)(22) Заявка: 2008103121/03, 29.06.2006 (24) Дата начала отсчета срока действия патента: 29.06.2006 (73) Патентообладатель(и): ЭДВАНСТ ПЛАЗМА ПАУЭР ЛИМИТЕД (GB) 2 4 2 4 4 6 8 (43) Дата публикации заявки: 10.08.2009 Бюл. № 22 2 4 2 4 4 6 8 R U (56) Список документов, цитированных в отчете о поиске: ЕР 0952393 A1 (KABUSHIKI KAISHA KOBE SEIKO SHO), 27.10.1999. JP 2003-147373 A (ISHIDA MICHIO, et.al.), 21.05.2003. US 6021723 A (JOHN A. VALLOMY), 08.02.2000. WO 2004/060587 A1 (INTERNATIONAL WASTE INDUSTRIES LIMITED), 22.07.2004. GB 1551020 A (REFUSE DERIVED FUELS LTD), 22.08.1979. Биомасса как источник энергии, под ред. Соуфера С. и др. - М.: (см. прод.) C 2 C 2 (45) Опубликовано: 20.07.2011 Бюл. № 20 (85) Дата начала рассмотрения заявки PCT на национальной фазе: 29.01.2008 (86) Заявка PCT: GB 2006/002409 (29.06.2006) (87) Публикация заявки РСТ: WO 2007/000607 (04.01.2007) Адрес для переписки: 129090, Москва, ул.Б.Спасская, 25, стр.3, ООО "Юридическая фирма Городисский и Партнеры", пат.пов. Е.И.Емельянову, рег.№ 174 (54) СПОСОБ И УСТРОЙСТВО ...

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25-11-1999 дата публикации

폐기물의 처리 방법 및 폐기물 처리 장치

Номер: KR19990082914A

본 발명은 폐기물의 가스화 처리를 효율 좋게 할 수 있는 동시에, 유해 물질이 되는 다이옥신 및 염소 가스 등이 환경으로 배출되는 것을 방지할 수 있는 폐기물의 처리 방법 및 폐기물 처리 장치를 제공한다. 또 폐기물을 열에너지로 변환하여 전기 에너지로서 유효하게 활용하는 동시에, 2차 폐기물의 양을 대폭적으로 삭감할 수 있는 폐기물의 처리 방법 및 폐기물 처리 장치를 제공한다. 본 발명의 폐기물의 처리 방법은 유기물을 포함하는 폐기물(a)을 공기를 차단한 상태에서 건류하여 열분해 가스(b)와 건류 잔류물(c)로 분리하는 열분해 공정과, 열분해 가스(b)를 열분해함으로써 저분자의 탄화수소를 함유하는 개질 가스(e)를 얻는 가스 개질 공정과, 건류 잔류물(c)을 냉각하여 고형화하는 잔류물 냉각 공정과, 이 고형화한 건류 잔류물을 분쇄 및 선별하여 열분해 차콜(g)을 얻는 기계적 처리 공정과, 이 열분해 차콜(g)을 도입하여 고온 연소를 하여 무기질 성분을 용융시키는 동시에 저분자의 탄화수소를 함유하는 가스화 가스(i)를 얻는 용융 가스화 공정을 갖는 것을 특징으로 한다.

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18-07-2012 дата публикации

气化设备的氨处理方法和装置

Номер: CN102597183A
Принадлежит: IHI Corp

通过氨回收装置(13)从双塔式气化设备的气化炉(1)中生成的气化气体(6)中分离回收氨废气(17)(氨),将氨废气(17)作为脱硝用还原剂注入旋风分离器(10)的入口,该旋风分离器(10)将在燃烧炉(2)中加热的床层物料(4)从燃烧排气(9)中分离并返回气化炉(1),使氨废气(17)与高温的燃烧排气(9)接触,通过非催化分解法还原净化NO x ,同时将氨废气(17)的过量部分分配供给上述燃烧炉(2)的一次空气(8)中进行燃烧处理。

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04-08-2017 дата публикации

一种基于生物质类固废及危废的以废治废处置工艺

Номер: CN107008731A

本发明公开了一种基于生物质类固废及危废的以废治废处置工艺,选择适合热解气化的生物质类固废/危废物质为原料,经预处理后输送到气化系统中进行热解气化得到生物质燃气与灰渣,将燃气与灰渣分别送入熔渣炉内,利用生物质类废弃物气化所得的燃气进行高温熔融焚烧,分解破坏掉二噁英类有毒害的有机质成分,并完成灰渣的熔融,熔融的灰渣经水淬后形成玻璃态熔渣将重金属包裹于熔渣内,实现危废物质的稳定固化,可满足超低浸出毒性的排放要求。本发明充分利用生物质类固废/危废气化燃气为灰渣熔融固化提供热能,解决了固废/危废焚烧灰渣易产生二次污染、稳定化处置能耗大以及运行成本高的问题,达到了以废治废的目的。

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03-01-1995 дата публикации

Apparatus and method for thermal cleaning of articles

Номер: KR950001256A

본 발명은 공간(3)내로 위치되고 제거될 재료가 열분해 되는 온도까지 가열되는 세정될 물품(4)를 열적 세정하는, 특히 금속제 물품(4)로부터 플라스틱과 같은 재료를 제거하기 위한 방법에 관한 것으로, 세정될 물품(4)의 온도는 측정 공간(7), 특히 작업물 아래에 위치되어 용융된 플라스틱을 수집하는데 또한 사용되는 수용부(9)내에 위치된 온도 감지기에 의해 제어되는 것을 특징으로 한다.

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19-05-2020 дата публикации

Waste incineration system

Номер: CN111174211A

本发明公开一种垃圾焚烧系统,包括顺序设置的干燥裂解炉、高温气化炉、过氧燃尽炉和燃尽室,将垃圾投入干燥裂解炉中,干燥输送炉排上的垃圾被干燥、破碎、部分裂解,然后从炉排缝隙落入流化裂解布风室顶部的流化裂解区和空气进行裂解反应,产生的高温裂解气进入高温气化炉;在高温气化炉中,裂解固态产物和空气进行气化反应,进入气化炉的裂解气和水蒸气与高温气化炉内高温焦炭及反应气进行重整反应,生成易燃尽反应气并进入燃尽室中,产生的气化反应渣进入过氧燃尽炉;在过氧燃尽炉中,气化反应渣与空气反应进行燃尽,产生的过氧烟气进入燃尽室;在燃尽室中,高温气化反应与高温过氧烟气进行混合燃烧,保证二噁英充分脱除。

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07-08-2013 дата публикации

Gas generating furnace purging method and apparatus

Номер: JP5256811B2
Принадлежит: IHI Corp

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25-07-1995 дата публикации

Method of treatment of activated sludge

Номер: RU2040490C1
Автор: Айхер Макс
Принадлежит: Айхер Макс

FIELD: treatment of activated sludge. SUBSTANCE: activated sludge is disinfected and rendered harmless in successively performed stages: drying, anaerobic treatment at a temperature of 250 to 350 C and roasting at a temperature of at least 1250 C; it is suggested to carry out all stages, including the conveying of treated material, in the conditions of continuous flow, the treatment stages to be carried in succession make up a closed cycle. Removed from this system are vapor in the drying stage, conversion gas in the anaerobic treatment stage, after which these waste products get condensed. Heat contained in flue gases formed in the process of roasting is used first for heating the anaerobic treatment stage and then- the drying stage. Due to the use of flue gases for heating the treatment stages in succession of natural temperature drop, it becomes possible to treat the activated sludge without any use energy from without, i.e. consumption of energy required for treatment of activated sludge is almost completely satisfied by the heat of combustion of organic components of activated sludge. EFFECT: no injury to environment due to treatment of activated sludge in a closed cycle. 12 cl, 3 dwg ОбБбУ0УО0сС ПЧ ГЭ РОССИЙСКОЕ АГЕНТСТВО ПО ПАТЕНТАМ И ТОВАРНЫМ ЗНАКАМ ЗВО”” 2040 490‘ (51) МПК 13) Сл С 02 Е 11/18 12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ РОССИЙСКОЙ ФЕДЕРАЦИИ (21), (22) Заявка: 5001263/26, 20.08.1991 (30) Приоритет: 01.09.1990 ЕР 90116810.4 (46) Дата публикации: 25.07.1995 (56) Ссылки: Европейский патент М 0347808, кл. С О2Е 11/10, 1989. (71) Заявитель: Макс Айхер[ОЕ] (72) Изобретатель: Макс Айхер[ОЕ] (73) Патентообладатель: Макс Айхер[ОЕ] (54) СПОСОБ ОБРАБОТКИ АКТИВНОГО ИЛА И УСТАНОВКА ДЛЯ ЕГО ОСУЩЕСТВЛЕНИЯ (57) Реферат: Изобретение относится к способу обработки активного ила. При обработке активного ила, заключающейся в его обеззараживании и обезвреживании, осуществляемой на — последовательно проводимых стадиях, а именно сушка, анаэробная обработка при температуре ...

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02-06-2015 дата публикации

Apparatuses and methods for controlling heat for rapid thermal processing of carbonaceous material

Номер: US9044727B2
Принадлежит: Ensyn Renewables Inc

Embodiments of apparatuses and methods for controlling heat for rapid thermal processing of carbonaceous material are provided herein. The apparatus comprises a reheater for containing a fluidized bubbling bed comprising an oxygen-containing gas, inorganic heat carrier particles, and char and for burning the char into ash to form heated inorganic particles. An inorganic particle cooler is in fluid communication with the reheater to receive a first portion of the heated inorganic particles. The inorganic particle cooler is configured to receive a cooling medium for indirect heat exchange with the first portion of the heated inorganic particles to form first partially-cooled heated inorganic particles that are fluidly communicated to the reheater and combined with a second portion of the heated inorganic particles to form second partially-cooled heated inorganic particles. A reactor is in fluid communication with the reheater to receive the second partially-cooled heated inorganic particles.

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23-08-2016 дата публикации

Char-handling processes in a pyrolysis system

Номер: US9422478B2
Принадлежит: Ensyn Renewables Inc

Char-handling processes for controlling overall heat balance, ash accumulation, and afterburn in a reheater are provided. Carbonaceous biomass feedstock is pyrolyzed using a heat transfer medium forming pyrolysis products and a spent heat transfer medium. The spent heat transfer medium is separated into segregated char and char-depleted spent heat transfer medium. The char-depleted spent heat transfer medium is introduced into a dense bed of heat transfer medium fluidized by a stream of oxygen-containing regeneration gas. All or a portion of the segregated char is combusted in the dense bed using the stream of oxygen-containing regeneration gas. A portion of the segregated char may be exported out of the pyrolysis system to control the overall heat balance and ash accumulation.

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13-09-2016 дата публикации

Heat removal and recovery in biomass pyrolysis

Номер: US9441887B2
Принадлежит: Ensyn Renewables Inc

Pyrolysis methods and apparatuses that allow effective heat removal, for example when necessary to achieve a desired throughput or process a desired type of biomass, are disclosed. According to representative methods, the use of a quench medium (e.g., water), either as a primary or a secondary type of heat removal, allows greater control of process temperatures, particularly in the reheater where char, as a solid byproduct of pyrolysis, is combusted. Quench medium may be distributed to one or more locations within the reheater vessel, such as above and/or within a dense phase bed of fluidized particles of a solid heat carrier (e.g., sand) to better control heat removal.

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03-09-2019 дата публикации

Apparatuses and methods for controlling heat for rapid thermal processing of carbonaceous material

Номер: US10400175B2
Принадлежит: Ensyn Renewables Inc

Embodiments of apparatuses and methods for controlling heat for rapid thermal processing of carbonaceous material are provided herein. The apparatus comprises a reheater for containing a fluidized bubbling bed comprising an oxygen-containing gas, inorganic heat carrier particles, and char and for burning the char into ash to form heated inorganic particles. An inorganic particle cooler is in fluid communication with the reheater to receive a first portion of the heated inorganic particles. The inorganic particle cooler is configured to receive a cooling medium for indirect heat exchange with the first portion of the heated inorganic particles to form first partially-cooled heated inorganic particles that are fluidly communicated to the reheater and combined with a second portion of the heated inorganic particles to form second partially-cooled heated inorganic particles. A reactor is in fluid communication with the reheater to receive the second partially-cooled heated inorganic particles.

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08-06-2021 дата публикации

Heat removal and recovery in biomass pyrolysis

Номер: US11028325B2
Принадлежит: Ensyn Renewables Inc

Pyrolysis methods and apparatuses that allow effective heat removal, for example when necessary to achieve a desired throughput or process a desired type of biomass, are disclosed. According to representative methods, the use of a quench medium (e.g., water), either as a primary or a secondary type of heat removal, allows greater control of process temperatures, particularly in the reheater where char, as a solid byproduct of pyrolysis, is combusted. Quench medium may be distributed to one or more locations within the reheater vessel, such as above and/or within a dense phase bed of fluidized particles of a solid heat carrier (e.g., sand) to better control heat removal.

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06-08-2013 дата публикации

Char-handling processes in a pyrolysis system

Номер: US8499702B2
Принадлежит: Ensyn Renewables Inc

Char-handling processes for controlling overall heat balance, ash accumulation, and afterburn in a reheater are provided. Carbonaceous biomass feedstock is pyrolyzed using a heat transfer medium forming pyrolysis products and a spent heat transfer medium. The spent heat transfer medium is separated into segregated char and char-depleted spent heat transfer medium. The char-depleted spent heat transfer medium is introduced into a dense bed of heat transfer medium fluidized by a stream of oxygen-containing regeneration gas. All or a portion of the segregated char is combusted in the dense bed using the stream of oxygen-containing regeneration gas. A portion of the segregated char may be exported out of the pyrolysis system to control the overall heat balance and ash accumulation.

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01-09-2017 дата публикации

A kind of indirect thermal cracking and lime-ash burning melting furnace and its processing method

Номер: CN107120656A
Автор: 周冲
Принадлежит: 周冲

本发明属于有机固废处理技术领域。特别涉及一种高效节能使用范围广的间接热裂解及灰渣燃烧熔融炉:带回转的热裂解及灰渣燃烧熔融炉体和回转筒体/回转窑密封装置;所述的回转热裂解及灰渣燃烧熔融炉体包括中间带螺旋推送装置的间接热裂解筒体和筒体外部带螺旋逆向推送灰渣燃烧熔融加热炉,所述回转密封装置包括回转筒体、进料端集料罩、出料端集料罩、水封填充密封圈、氮气紧急密封气室以及鱼鳞密封片。所述可回转间接热裂解筒体内衬碳化硅材质的耐热钢制圆筒,内部设有可旋转的绞龙,筒体外部固定有耐高温陶瓷绞龙片。本发明将裂解炉、二次燃烧室、熔融炉整合到一个炉体内,可利用裂解后产生的不凝气、冷凝油、碳渣作补充为燃料使用,大大降低了热量消耗,同时将剩余灰渣熔融达到安全填埋标准。

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28-12-2018 дата публикации

Castoff fusing curing process system and method

Номер: CN106524175B

本发明公开了一种废弃物熔融固化处理系统及方法,使用本发明处理垃圾,垃圾输送能力更强,垃圾处理量更大,能够减少热损耗和提高热交换效率,热量的回收效率较高,且能够有效地减少污染物排放量。熔融固化处理系统包括沿进料方向依次设置的熔融炉膛、层流通道、水冷破碎系统和水封除渣系统,熔融炉膛侧墙设置有高温燃烧器、气化剂入口,水冷破碎系统包括水冷系统、水冷腔以及玻璃体粉碎机。方法包括,步骤A、起炉、烘炉;步骤B、使残渣进入熔融炉膛内熔融;步骤C、使无机废弃物在层流通道内熔融;步骤D、熔融渣水冷固化成玻璃体渣,并破碎、排渣;步骤E、待废弃物熔融渣排出完后,关闭废弃物熔融固化处理系统。

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08-04-2008 дата публикации

Waste treatment process and apparatus

Номер: KR20080031152A
Принадлежит: 테트로닉스 엘티디

폐기물을 처리하기 위한 방법이: (ⅰ)(a) 상기 폐기물을 산소 및 스팀의 존재하의 가스화 유닛 내에서 처리하여 오프가스 및 차르를 생성시키는 단계를 포함하는 가스화 단계, 또는 (b) 상기 폐기물을 열분해 유닛 내에서 처리하여 오프가스 및 차르를 생성시키는 열분해 단계; 및 (ⅱ) 상기 오프가스 및 상기 차르를 산소 및, 선택적으로 스팀의 존재하의 플라즈마 처리 유닛 내에서 플라즈마 처리하는 단계를 포함하는 플라즈마 처리 단계를 포함한다.

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12-10-2016 дата публикации

Produce the method and system of cleaning steam based on solid fuel

Номер: CN102203220B
Автор: J·D·本特森
Принадлежит: DALL ENERGY HOLDING APS

固体燃料通过分阶段热反应器被转变为具有低含量的挥发性有机化合物(VOC)、NOx和粉尘的清洁热烟道气和具有低含碳量的清洁灰,其中固体燃料的转变过程分为独立的竖直阶段(从下到上):灰燃尽、炭氧化和气化、热解、干燥和气体燃烧阶段,来自气化器的气体在此中燃烧。

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23-07-2014 дата публикации

A multi-zone carbon conversion system with plasma melting

Номер: CN102144126B

提供一种将处理过的原料转化成合成气和熔渣的多段碳转化器,其包括:腔室,包括和熔渣段连通的碳转化段,以通过施加等离子热量来将灰熔融成熔融的熔渣/或者用于将熔渣保持为熔融状态。所述碳转化段和所述熔渣段由段间区域隔开,所述段间区域包括阻滞体以阻止或限制物质在两个段之间的运动。所述段间区域也可以提供通过影响来自熔渣段的等离子热量的传递来将灰初始熔融为熔融的熔渣。

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20-10-1998 дата публикации

Method and apparatus for producing combustible gases from solid fuel, method and apparatus for treating raw phosphates

Номер: RU2120460C1
Принадлежит: Ормат Инк.

FIELD: production of combustible gases. SUBSTANCE: method involves subjecting portion of solid fuel to pyrolysis in pyrolysis reactor 43 to produce combustible gases and carbon-bearing material; feeding carbon-bearing material from reactor 43 into furnace 45 to obtain combustion products containing glowing flue gases and ash particles; separating ashes from combustion products in separator 47 and directing large ash particles into pyrolysis reactor 43; feeding another portion of solid fuel through pipeline 42 and burning it in furnace together with carbon-bearing material fed from reactor 43; treating raw phosphates in similar way; separating portion of ashes from separator 47 for heating air supplied into furnace 45. Construction of apparatuses for accomplishing methods is described in Specification. Method allows low-quality fuels and phosphates with relatively low content of organic material to be used. EFFECT: increased efficiency and provision for complete extraction of organic substance from raw material. 15 cl, 10 dwg О9ЗУОСТсС ПЧ ГЭ РОССИЙСКОЕ АГЕНТСТВО ПО ПАТЕНТАМ И ТОВАРНЫМ ЗНАКАМ (19) (51) МПК ВИ” 2 120 460 ' 13) СЛ С 40В 49/16, 53/06, С 10 4 3/58 12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ РОССИЙСКОЙ ФЕДЕРАЦИИ (21), (22) Заявка: 93004581/25, 24.03.1993 (30) Приоритет: 25.03.1992 Ш 101361 30.03.1992 Ш 101424 (46) Дата публикации: 20.10.1998 (56) Ссылки: ЗЦ, авторское свидетельство, 1122682, кл. С 10 В 53/06, 1984. Ц$, патент, 4211606, кл. С 10 В 49/18, 1980. (71) Заявитель: Ормат Инк. (1$) (72) Изобретатель: Даниэль Голдман (11), Борис Синякевич (ЦА), Бенджамин Дорон (Ш), Люсьен И.Броники (11), Эли Йаффе (1) (73) Патентообладатель: Ормат Инк. (1$) (54) СПОСОБ И УСТРОЙСТВО ДЛЯ ПОЛУЧЕНИЯ ГОРЮЧИХ ГАЗОВ ИЗ ТВЕРДОГО ТОПЛИВА, СПОСОБ И УСТРОЙСТВО ДЛЯ ОБРАБОТКИ СЫРЫХ ФОСФАТОВ (57) Реферат: Порцию твердого топлива подвергают пиролизу в пиролизном реакторе (43) с получением горючих газов и углеродсодержащего материала. Последний затем подают из реактора (43) в печь (45) для ...

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18-01-2017 дата публикации

Solid organic material cracking system

Номер: CN106338067A
Автор: 周昆, 姚波, 康琪

本发明提供一种固体有机材料裂解系统,包括微波发生器、与微波发生器连接的复合裂解腔、油气分离装置,所述复合裂解腔上开设有复合裂解腔进气口和复合裂解腔出气口,所述油气分离装置上开设有油气分离装置进气口和油气分离装置出气口,还包括气体加热装置,所述气体加热装置上开设有气体加热装置进气口和气体加热装置出气口,所述气体加热装置进气口与油气分离装置出气口连通,所述气体加热装置出气口与复合裂解腔进气口连通,所述油气分离装置进气口与复合裂解腔出气口连通,所述裂解系统还包括原料预加热装置,所述原料预加热装置与复合裂解腔连接。该系统结构简单,操作方便,易控,采用该系统裂解固体有机材料能有效减少能耗。

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15-03-2019 дата публикации

High temperature pyrolysis burning facility

Номер: CN106352349B
Автор: 梁福周
Принадлежит: New Wind Of Co

本发明提供一种高温热解焚烧设备,该高温热解焚烧设备将外部空气强制供给到燃烧室,同时在与外部隔离的燃烧室内在高温下燃烧注入其中的焚烧处理材料,其中空气供给管(10)被固定地设置在燃烧室(2)的中央;燃料供给管道(14)被安装在燃烧室(2)内部的上部边缘处;燃烧室(2)的下部部分的底部形成有冲孔板(28);利用空气供给管(10)作为固定轴旋转的搅拌棒(30)被设置在其底部的中央;且在燃烧室(2)外部的一侧处设置有热回收装置(4);并且循环管道(48)从燃烧室(2)的盖(12)的一侧延伸到外部,以经由热回收装置(4)的内部返回至燃烧室(2)的壁中与搅拌棒(30)的上部部分相对应的位置。

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06-03-2018 дата публикации

Staged biomass fractionator

Номер: US9909067B2
Принадлежит: Cool Planet Energy Systems Inc

Various biomass reactors systems and methods of pyrolyzing biomass are disclosed. One type of biomass reactor system comprises a plurality of biomass processing stations configured in series, each station comprising an auger reactor including an auger inlet for receiving biomass and a transfer screw for conveying the biomass through the auger reactor.

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20-02-2013 дата публикации

Method and device for the pyrolysis and gasification of material mixtures containing organic components

Номер: EP1399527B1
Принадлежит: Herhof Verwaltungs GmbH

The invention is used for the pyrolysis and gasification of material mixtures containing organic components. The organic materials or the material mixture containing organic components are brought into contact with a heat transfer medium, preferably the ash from a combustion reactor, and pyrolysed in a pyrolysis reactor, preferably a shaft reactor. The coke which is generated by pyrolysis is combusted with an air supply in a combustion reactor, preferably in a fluidized bed reactor. The condensable components of the crude gas which is generated by pyrolysis are cracked in a cracking reactor, preferably by means of a catalyst. In order to improve said method, the heat transfer medium is transported using overheated steam (50) as a fluidizing medium.

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16-01-2003 дата публикации

Method and device for pyrolysis and gasification of mixtures containing organic components

Номер: DE10228100A1
Принадлежит: Herhof Umwelttechnik GmbH

The invention is used for the pyrolysis and gasification of material mixtures containing organic components. The organic materials or the material mixture containing organic components are brought into contact with a heat transfer medium, preferably the ash from a combustion reactor, and pyrolysed in a pyrolysis reactor, preferably a shaft reactor. The coke which is generated by pyrolysis is combusted with an air supply in a combustion reactor, preferably in a fluidized bed reactor. The condensable components of the crude gas which is generated by pyrolysis are cracked in a cracking reactor, preferably by means of a catalyst. In order to improve said method, the heat transfer medium is transported using overheated steam (50) as a fluidizing medium.

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23-11-2018 дата публикации

burner

Номер: CN108884997A
Автор: A.范德韦肯
Принадлежит: Fire Power Technology Co Ltd

本发明涉及用于气态、流体或粉末燃料的燃烧器,三个成分引入燃烧器中:燃料(40);氧化气体(10),例如,空气;以及惰性气体(20),例如,由燃烧产生的气体、氮气或水蒸气。两个成分,例如,空气和惰性气体,混合在一起,且由关于燃料的移动布置在不同位置处的至少一个喷射级(95)推进。

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01-09-2000 дата публикации

Method and apparatus for producing superheated steam using heat generated through incineration of wastes

Номер: KR100264723B1

본 발명은 약 200。C∼ 320。C 전후에 비점을 갖도록 가압시킨 보일러수를 사용하여, 그 보일러수의 가열을 적어도 2단계 이상의 복수단계로 하여, The present invention uses a boiler water pressurized to have a boiling point around 200 ° C. to 320 ° C., and the heating of the boiler water is performed in at least two or more steps. 상기 대략 비점온도까지의 가열을 염소함유 열에너지로서 행하고, Heating to the above boiling point temperature is performed as chlorine-containing thermal energy; 상기 대략 비점온도로 부터 소정온도의 과열증기를 얻는 과열을 염소를 함유하지 않은 탈염소에너지로, 행하는 것을 특징으로하는 것으로, 구체적으로는 상기 염소함유 열에너지로의 가열은, 약 300。C 이상의 유동매체를 함유하는 공간내에 폐기물을 공급하여 열분해 반응을 행하는 열분해 수단으로 얻는 열분해가스의 연소열 에너지를 이용하여 행하도록 하고, 탈염소열 에너지로의 가열은, 상기 열분해 수단에서 취출된 미분해 잔사 및 유동사로 이루어진 차르혼합물을 공기에 의해서 유동시키면서 상기 미분해 잔사를 연소하는 차르연소수단에 의해 얻는 열에너지를 이용하여 수행한다. Superheating to obtain superheated steam having a predetermined temperature from the boiling point temperature is performed by dechlorination energy containing no chlorine. Specifically, heating to the chlorine-containing heat energy is about 300 ° C. or more. The waste is supplied to the space containing the medium to perform the pyrolysis means obtained by the pyrolysis means for the pyrolysis reaction, and the heat to the dechlorination heat energy is the undecomposed residue and the flow taken out from the pyrolysis means. Char mixtures of yarns are flowed by air, and heat energy is obtained by char combustion means for burning the undecomposed residues.

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07-01-2022 дата публикации

Coupling equipment and method for fluidized bed oxygen-enriched combustion and moving bed pyrolysis gasification

Номер: CN113898956A

本发明涉及废弃物处理技术领域,尤其涉及一种流化床富氧燃烧与移动床热解气化的耦合设备及方法。该耦合设备包括:流化床提升管、第一高温旋风分离器、移动床反应器、第二高温旋风分离器、氧气提供装置和高温过热器;其中,流化床提升管与第一高温旋风分离器连接;第一高温旋风分离器与移动床反应器连接,移动床反应器与第二高温旋风分离器连接,高温过热器与第二高温旋风分离器连接,氧气提供装置与所述移动床反应器连接。本发明提供的流化床富氧燃烧与移动床热解气化的耦合设备不仅低碳环保而且原料适应性广,兼顾能量利用率高,污染小,产品品质好等优点。

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20-10-2017 дата публикации

A kind of system and method for house refuse cleaning treatment

Номер: CN107262505A

本发明涉及一种生活垃圾清洁处理的系统和方法,其中,方法包括:将生活垃圾进行分选,用于分选出无机物、可燃物及有机质;将所述可燃物进行热解处理,产生固体炭和热解油气混合物;将所述热解油气混合物进行分离净化处理,得到热解油和净化热解气;将所述有机质进行厌氧消化产生沼气,将所述沼气进行净化处理;将所述固体炭、热解油、净化热解气及净化沼气送入燃烧装置进行燃烧,通过换热产蒸汽,且将所述蒸汽用于发电。整个工艺不仅解决了垃圾处理过程中二噁英及飞灰污染等问题,还将高热值的可燃物与低热值的有机质分别进行高效利用,增加了工艺的清洁性,降低了运行成本,经济性好,易于工业化推广。

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03-08-1994 дата публикации

Fluidized-bed reactor and system with and using method

Номер: CN1090219A
Автор: 唐遵义
Принадлежит: Foster Wheeler Energy Corp

一种燃烧废物燃料的流化床反应器和系统以及 利用该反应燃烧废物燃料的方法,其中,把反应器分 成三个部分。废物燃料被引入到一个室内的流化床, 废物燃料在其内与成床物料混合,控制成床物料以便 为产生热解气体提供一个理想的环境。流态化的成 床物料被气动地和靠自重地向下输送,并被喷入第二 室内的流化床中,其中,非挥发性有机化合物在氧化 气氛中燃烧。在第二室内的成床物料被气动地向上 输送并被分成两部分,在其中的一部分成床物料循环 回到第一室内。在第二室内的另一部分成床物料流 到第三室内的流化床中,在第三室中回收热量。在回 收室内的成床物料靠重力输送回到第二室内以便调 节后一室内的温度。

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20-01-2006 дата публикации

Partition wall for use in a heat exchange and the method thereof

Номер: KR100543903B1
Принадлежит: 미츠이 조센 가부시키 가이샤

본 발명의 목적은, 열 변형하기 어렵고, 더스트 부착량도 저하할 수 있는 열교환기의 통로벽 구조 및 열교환기의 통로벽의 제조방법을 제공하는 것이다. 본 발명에 있어서는, 공기통로와 배기가스통로를 분리하는 칸막이벽의 구조로서, 상기 칸막이벽은 한쪽 면이 상기 공기통로에 접하는 금속벽과 한쪽 면이 상기 배기가스통로에 접하는 내화벽으로 이루어지고, 또한 상기 금속벽의 다른쪽 면과 상기 내화벽의 다른쪽 면 사이에 제 1 간극부를 형성함과 동시에, 상기 제 1 간극부에 상기 금속벽의 관통구멍을 연통시켜, 상기 배기가스통로에 부식성 성분 및 더스트를 함유하는 연소배기가스를 흐르게 하는 통로벽에 있어서, 상기 금속벽의 상기 다른쪽 면에, 상기 내화벽을 유지하는 복수의 유지부재를 고정하는 것을 특징으로 한다.

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23-05-2012 дата публикации

Waste management system

Номер: CN102472486A
Принадлежит: 约翰·杰勒德·斯维尼

本发明涉及一种综合垃圾处理系统(1)和方法,其包括可燃垃圾源(2)的使用,用于从可回收材料中分离所述的可燃垃圾的分离器(3),用于将所述的可燃垃圾干燥以产生热解原料的真空干燥器(4)和用于将所述的热解原料高温分解以生成焦炭和热解气体的热解器(5)。用于发电的系统和方法,包括根据本发明的垃圾处理系统或方法,还包括氧化器(7),用于将从所述的热解原料产生的合成气高温氧化以产生用于发电的热量。

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23-02-1995 дата публикации

Plant for thermal waste disposal and method for operating such a plant

Номер: DE4327953A1
Принадлежит: SIEMENS AG

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20-06-2015 дата публикации

Method and apparatus for processing black liquor of pulp mill

Номер: RU2553882C2
Принадлежит: Валмет Пауэр Ой

FIELD: chemistry. SUBSTANCE: invention relates to a method and an apparatus for processing black liquor of a pulp mill for recovering energy and chemicals therefrom. A method of processing black liquor of a pulp mill for recovering chemicals and energy contained therein includes steps of feeding black liquor into a pyrolysis reactor having a substantially oxygen-free chamber, wherein temperature in the pyrolysis reactor is maintained in the range of 400 to 600°C, feeding into the pyrolysis reactor causticising material which consists of sodium oxide (Na 2 O) and a metal oxide (M x O y ) comprising at least one of the following metal oxides: titanium oxide (TiO 2 ), iron oxide (Fe 2 O 3 ) and manganese oxide (Mn 2 O 3 ),where said causticising material is heated in a furnace unit where temperature is maintained in the range of 600 to 1000°C, leading to gasification of black liquor and formation of gaseous components and a residual solid substance, feeding the gaseous components formed in the pyrolysis reactor for further recycling, transporting the solid substance formed in the pyrolysis reactor into the furnace unit, where fuel contained therein is burnt using oxygen contained in air fed into the furnace unit, leading causticising material consisting of sodium oxide (Na 2 O) and a metal oxide (M x O y ), returning part of the causticising material formed in the furnace unit into the pyrolysis reactor and transporting part of it into a dissolving tank, where water is added, to form sodium hydroxide (NaOH) and a metal oxide (M x O y ), returning the formed sodium hydroxide (NaOH) into the pulping process and at least the main part of the remaining metal oxide (M x O y ) into the furnace where it forms causticising material with sodium oxide (Na 2 O). The apparatus for processing black liquor of a pulp mill for recovering chemicals and energy contained therein includes a furnace unit, a pyrolysis reactor into which black liquor is fed and where the black liquor ...

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08-08-2017 дата публикации

Processing method for application of city life garbage

Номер: CN107023837A
Автор: 刘军亮
Принадлежит: Wobang Environmental Protection Co Ltd

本发明公开了一种用于城镇生活垃圾的处理方法,包括步骤:生活垃圾自上而下进入热解气化炉并点火进行燃烧,热解气化炉内自上而下依次设置为干燥层、贫氧的热解气化层和富氧的燃烧层;热解气化炉内的热空气在引风机作用下与进入热解气化炉内的生活垃圾相向运动;热解气化层产生的可燃性气体经换热冷却后循环至燃烧层再次燃烧;热解气化炉外排的气体经冷却后进行尾气净化处理,冷却过程中产生的液态焦油与后续的生活垃圾混合后再次进入热解气化炉;燃烧产生的无害灰渣进行排渣处理。本发明具有减容、减质效果好,处理周期短且不受垃圾组分的限制,尾气排放量少且便于控制,对于选址无严格要求、适用性广等优点。

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26-11-2014 дата публикации

Apparatuses and methods for controlling heat for rapid thermal processing of carbonaceous material

Номер: CN104169395A
Принадлежит: Ensyn Renewables Inc

本文提供用于控制含碳物质的快速热处理的热量的装置和方法的实施方式。该装置包括再热器,该再热器用于包括包含含氧气体、无机热载体颗粒和炭的流化沸腾床,以及用于将该炭燃烧为灰分以形成加热的无机颗粒。无机颗粒冷却器与该再热器流体连通,以接收该加热的无机颗粒的第一部分。该无机颗粒冷却器被配置以接收用于与该加热的无机颗粒的该第一部分进行间接热交换以形成第一部分地被冷却的加热的无机颗粒的冷却介质,该第一部分地被冷却的加热的无机颗粒被流动传递至该再热器中并与该加热的无机颗粒的第二部分混合,以形成第二部分地被冷却的加热的无机颗粒。反应器与该再热器流体连通,以接收该第二部分地被冷却的加热的无机颗粒。

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09-01-2004 дата публикации

PROCESS FOR PRODUCING FOOD FUMES BY PYROLYSIS, USE OF A REACTOR PARTICULARLY SUITABLE FOR SAID PROCESS, FUMES AND SMOKED FOODSTUFFS OBTAINED

Номер: FR2841745A1

La présente invention concerne le domaine de la production de fumées à usage agro-alimentaire et a pour objet un procédé caractérisé en ce qu'il comprend essentiellement les étapes consistant à introduire la matière organique à pyrolyser dans un réacteur comprenant essentiellement une enceinte chauffable sensiblement hermétique contenant au moins un élément tubulaire ascendant mis en vibration et recevant ladite matière, au niveau de la partie basse dudit élément tubulaire, chauffer ladite matière organique à une température comprise entre 200 °C et 800 °C, de préférence entre 300 °C et 400 °C, afin d'en provoquer la pyrolyse lors de son déplacement, sous l'effet des vibrations, dans le ou les éléments tubulaires ascendants et extraire la matière consumée et les fumées produites au niveau de la partie haute dudit ou desdits éléments tubulaires. The present invention relates to the field of the production of smoke for agro-food use and relates to a process characterized in that it essentially comprises the steps consisting in introducing the organic material to be pyrolyzed in a reactor essentially comprising a substantially hermetic heatable enclosure. containing at least one ascending tubular element vibrated and receiving said material, at the bottom of said tubular element, heating said organic material to a temperature between 200 ° C and 800 ° C, preferably between 300 ° C and 400 ° C, in order to cause pyrolysis during its movement, under the effect of vibrations, in the ascending tubular element or elements and extract the consumed material and the fumes produced at the top of said tubular element or elements.

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31-07-1998 дата публикации

ENERGY ENHANCEMENT INSTALLATION OF URBAN AND ASSIMILE WASTE

Номер: FR2758748A1
Принадлежит: GEC Alsthom Stein Industrie

Installation de valorisation énergétique de déchets urbains et assimilés comportant: - un dispositif de broyage (1) des déchets dont les refus sont triés en un premier flux de matières inertes peu pollués en matières organiques et en un second flux de matières inertes pollués en matières organiques ou d'éléments lourds combustibles, ce second flux étant évacué par une première sortie (S1), - un réacteur à lit fluidisé (2) recevant les déchets broyés, - un cyclone (11) de séparation des solides dans lequel sont amenés les gaz en sortie du réacteur (2), - une chaudière de récupération (15) dans laquelle s'évacuent les gaz en sortie du cyclone (11) et équipée d'un premier ensemble d'échangeurs de chaleur (18), et qui comporte une trémie de dépoussiérage dont sont évacués des particules solides par une deuxième sortie (S2), - un second ensemble d'échangeurs de chaleur (23) disposés dans une chambre (22) où sont amenés les gaz, - un dispositif de traitement final des gaz dont sont évacués des matières solides résultant du traitement par une troisième sortie (S3', S3"), - un four de fusion et de vitrification (6) indépendant relié à chacune desdites sorties par des conduites à passage commandé.par. Installation for energy recovery of urban and similar waste comprising: - a device for shredding (1) waste whose rejects are sorted into a first flow of inert materials little polluted in organic matter and in a second flow of inert materials polluted in organic matter or heavy fuel elements, this second stream being discharged through a first outlet (S1), - a fluidized bed reactor (2) receiving the ground waste, - a solids separation cyclone (11) into which the gases are fed at the outlet of the reactor (2), - a recovery boiler (15) in which the gases at the outlet of the cyclone (11) are discharged and equipped with a first set of heat exchangers (18), and which comprises a dust collection hopper from which solid particles are discharged via a ...

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06-11-1998 дата публикации

METHOD AND PLANT FOR HEAT TREATMENT OF WASTE

Номер: FR2754589B1
Автор: Louis Rousseau
Принадлежит: SOC ET ET REALISATIONS EN PROD

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06-11-2009 дата публикации

Method and apparatus for treating black liquor in a cellulose factory

Номер: FI20096152A0
Автор: Timo Honkola
Принадлежит: METSO POWER OY

The invention relates to a method and equipment for treating pulp mill black liquor so as to recover the energy in chemicals therein. In the invention the black liquor is pyrolysed in a pyrolysis reactor (4), where causticizing material consisting of metal oxide and sodium oxide and heated in a burning unit (6) is conveyed, and gaseous components formed in pyrolysis are conveyed for utilization and solids are returned to the burning unit.

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07-07-1978 дата публикации

Purifying waste water contg. soluble and insoluble pollutants - by adding lime and carbon di:oxide, reacting, then decanting

Номер: FR2373492A1

Purifying waste water contg. pollutants in soln. and in suspension comprises adding to the water lime and CO2 to form calcium carbonate crystals. The water is left in the presence of the crystals for a sufficient time to absorb the materials in soln. and to flocculate the material in suspension. The sludge formed is then decanted and the purified water sepd.. The process is carried out in a reactor comprising an external reservoir with an outlet for extracting the sludge at the bottom and means for drawing off the purified water at the top. In the intermediate area is provided means for introducing CO2 bubbles near the bottom of the intermediate area; at least one conduit for feeding milk of lime or water and lime into the intermediate area and at least one other conduit feeding in the waste water. The process provides a physico-chemical method which is both very economic and gives excellent results independently of variations in the water treated. It may be used alone or in combination with other known processes.

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23-06-1978 дата публикации

INSTALLATION AND PROCEDURE FOR THE INCINERATION OF RESIDUES

Номер: FR2372389A1
Автор: [UNK]
Принадлежит: Kernforschungsanlage Juelich GmbH

a. Installation pour incinération des résidus. b. Des fûts sont ouverts et sont basculés de 180 degrés par un basculeur 3a, 3b sur les raccords 5a, 5b de chargement. Après que les dispositifs de fermeture du basculeur et des raccords ont été ouverts, les résidus parviennent dans la chambre de pyrolyse et s'amoncellent sur les sas 10a, 10b de passage vers la chambre inférieure d'incinération. c. Industrie nucléaire. at. Installation for incineration of residues. b. Drums are opened and are tilted 180 degrees by a rocker 3a, 3b on the connectors 5a, 5b for loading. After the closing devices of the rocker and of the fittings have been opened, the residues reach the pyrolysis chamber and accumulate on the locks 10a, 10b passing through to the lower incineration chamber. vs. Nuclear industry.

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25-04-2014 дата публикации

DEVICE FOR TRANSFORMING A FUEL

Номер: FR2965816B1
Принадлежит: S3D SAS

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07-04-1988 дата публикации

Treatment of waste and a rotary kiln therefor

Номер: WO1988002284A1
Принадлежит: Neutralysis Industries Pty. Ltd.

A method for the treatment of waste materials wherein solid and/or liquid wastes are mixed with a binding material; the mixture is passed through an extruder to form pellets of waste; the pellets pass through a pyrolysis zone in a furnace or kiln to drive off at least a portion of the volatile gases in the waste, the pellets are passed through an oxidation zone in the furnace or kiln where the excess oxygen causes the remaining volatile gases and at least a portion of the fixed carbon in the waste to be oxidized and the pellets are passed through a vitrification zone in the furnace or kiln to vitrify the silicates present in the pellets to form a solid aggregate.

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20-10-2016 дата публикации

Heat control devices and methods for fast thermal processing of carbon-containing material

Номер: RU2600351C2
Принадлежит: Энсин Реньюэблс, Инк.

FIELD: chemistry. SUBSTANCE: invention relates to chemical industry and can be used for control of heat when quick heat treatment of carbon containing material. Device includes heater (14) with fluidized bed, containing oxygen-containing gas, inorganic particles of heat carrier and charcoal. Cooler (15) of inorganic particles is connected by liquid medium with heater (14) for receiving and cooling of first part of heated inorganic particles. Formed first partially cooled hot inorganic particles are fed to heater (14) and combined with second part of heated inorganic particles to form second partially cooled hot inorganic particles, which are fed to reactor (12). EFFECT: invention makes it possible to increase speed of thermal processing without exceeding design temperature of heater. 10 cl, 3 dwg РОССИЙСКАЯ ФЕДЕРАЦИЯ (19) RU (11) (13) 2 600 351 C2 (51) МПК C10B 49/18 (2006.01) C10G 9/30 (2006.01) C10G 55/04 (2006.01) ФЕДЕРАЛЬНАЯ СЛУЖБА ПО ИНТЕЛЛЕКТУАЛЬНОЙ СОБСТВЕННОСТИ (12) ОПИСАНИЕ (21)(22) Заявка: ИЗОБРЕТЕНИЯ К ПАТЕНТУ 2014115983/05, 14.09.2012 (24) Дата начала отсчета срока действия патента: 14.09.2012 (72) Автор(ы): КУЛПРАТХИПАНДЖА Сатхит (US), ПАЛМАС Паоло (US) (73) Патентообладатель(и): ЭНСИН РЕНЬЮЭБЛС, ИНК. (US) Приоритет(ы): (30) Конвенционный приоритет: (43) Дата публикации заявки: 27.10.2015 Бюл. № 30 R U 22.09.2011 US 13/240,570 (45) Опубликовано: 20.10.2016 Бюл. № 29 (85) Дата начала рассмотрения заявки PCT на национальной фазе: 22.04.2014 2 6 0 0 3 5 1 (56) Список документов, цитированных в отчете о поиске: US 3694346 A, 26.09.1972. SU 827949 A, 07.05.1981. RU 2009149700 A1, 20.07.2011. RU 2009133415 А1, 20.04.2011. US 4306619 A, 22.12.1981. (86) Заявка PCT: 2 6 0 0 3 5 1 R U C 2 C 2 US 2012/055384 (14.09.2012) (87) Публикация заявки PCT: WO 2013/043485 (28.03.2013) Адрес для переписки: 129090, Москва, ул. Б. Спасская, 25, строение 3, ООО "Юридическая фирма Городисский и Партнеры" (54) УСТРОЙСТВА И СПОСОБЫ РЕГУЛИРОВАНИЯ ТЕПЛА ДЛЯ БЫСТРОЙ ТЕРМИЧЕСКОЙ ...

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20-02-1992 дата публикации

Waste combustion with pure oxygen, melting mineral component - gives redn. of waste gas vol., facilitating sepn. of impurities

Номер: DE4026245A1
Принадлежит: HPM TECHNOCOMMERZ TECHNOLOGIE

Thermal treatment of waste and residues is carried out by combustion, using undiluted pure O2 as oxidant. Combustion is pref. carried out so that the mineral constituents melt, pref. by keeping the temp. above the m.pt. of these. The O2 may be diluted by mixing with pt. of the waste gas or with N2, water, steam and/or CO2. Additives, pref. fly ash or slag from waste combustion and/or reaction prods. from waste gas purificn., may be used which melt at a temp. below the m.pt. of the minerals or in the same temp. range. The waste pref. is mixed with carbonaceous material (I), pref. coal, coke, pyrolysis residues, spent coke from waste gas purificn. plants, bitumen, tar, oil and/or wood, which is burnt with undiluted O2, so that the minerals melt. The waste and (I) pref. are mixed and pulverised to dust before combustion in a suitable smelter. USE/ADVANTAGE - The use of pure O2 reduces the volume of waste gas formed in the combustion of 1 t household waste from ca. 6000 cu.m to 1800 cu.m, i.e. 30% of the usual amt. Reducing the vol. increases the concn. of impurities, which facilitates sepn. and (extensive) elimination of the emission of harmful organic matter, esp, dioxins, chlorinated phenols, hexachlorobenzene, polyaromatic cpds. and incompletely burnt impurities. In an example, a mixt. of 1 kg dry residue (slag, fly ash and reaction prods. from waste gas purificn.) and 100 g mineral coal was pulverised finely and burnt in a smelter in an O2 atmos. The residue melted at 1600 deg.C, forming a glass, which set to a prod. resistant to leaching on cooling. 0.22 cu.m waste gas, mainly CO2, were formed.

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13-05-2022 дата публикации

Wind-solar driven solid waste treatment multi-connection device system

Номер: CN114484449A
Автор: 刘文巍, 姚华, 许东东, 黄云
Принадлежит: Institute of Process Engineering of CAS

本发明提供了一种风光驱动固废处理的多联供装置系统,所述多联供装置系统包括固废热解单元、化学链燃烧与发电单元、海水淡化与供热单元以及气体存储单元。本发明将固废热解、化学链燃烧以及先进储热相融合,通过聚焦太阳光,向热解装置和化学链燃烧反应器补充反应热能,并将风能转化的电能作为旋转设备的动力源,使燃烧产物中的二氧化碳更容易分离与存储,有效利用海岛地区太阳能、风能等丰富的可再生资源,降低传统化石能源的消耗;同时还可向外界提供电力输出、热力输出和淡水等多种资源,就地实现海岛生活垃圾的减量化、无害化和资源化,解决海岛地区电力、热力和淡水资源紧缺的问题。

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18-08-2020 дата публикации

Deep purification equipment for hazardous waste incineration flue gas and purification treatment method thereof

Номер: CN111550797A

本发明提出一种危废物焚烧烟气的深度净化设备,包括回转窑、锅炉、急冷塔、喷雾塔、复合式除尘器、第一烟气换热器、反应器、脱酸塔、除尘器以及烟囱;所述回转窑、锅炉、急冷塔、喷雾塔、复合式除尘器、第一烟气换热器、脱酸塔、除尘器以及烟囱通过管道依次连接,所述反应器连接于所述第一烟气换热器上,所述锅炉上设置有喷水器,所述喷雾塔上设置有喷雾器,所述复合式除尘器上设置有喷粉器。通过对烟气进行换热实现烟气脱硝去除烟气中的氮氧化物,并且在复合式除尘器中喷入活性碳粉可以去除烟气中的二噁英,还通过喷粉器喷入小苏打粉和脱酸塔去除烟气中的酸性气体,有利于实现有机危险废物焚烧烟气的超净排放。

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31-10-2000 дата публикации

Plant for thermally processing waste materials and method of operating such plant

Номер: PL179627B1
Принадлежит: SIEMENS AG

A thermal disposal plant has a pyrolysis reactor (8) with a first heating arrangement (20) for indirectly heating waste (A) and a second heating arrangement (22, 22a) for directly heating waste (A) within the pyrolysis reactor (8). The pyrolysis reactor (8) converts waste (A) into low temperature carbonization gas (s) and solid pyrolysis residues (r). Both substances (s, r) are supplied to a high temperature reactor (32) for burning, if required after going through a conditioning arrangement (34). According to the invention, the first heating arrangement (20) ensures the basic heating of waste (A) in the pyrolysis reactor (8). For that purpose, a special energy carrier (b) or the lost heat from the smoke gas (R) of the high temperature reactor (32) may be used. Additional heating is supplied according to need by means of the second heating arrangement (22, 22a) by feeding air into the pyrolysis reactor(8).

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02-06-1999 дата публикации

Method and device for the production of fuels

Номер: DE69509315D1
Принадлежит: ROMANA MACERI CENTRO ITALIA S

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20-08-2013 дата публикации

Waste treatment process and apparatus

Номер: KR101298907B1

폐기물을 처리하기 위한 방법이: (ⅰ)(a) 상기 폐기물을 산소 및 스팀의 존재하의 가스화 유닛 내에서 처리하여 오프가스 및 차르를 생성시키는 단계를 포함하는 가스화 단계, 또는 (b) 상기 폐기물을 열분해 유닛 내에서 처리하여 오프가스 및 차르를 생성시키는 열분해 단계; 및 (ⅱ) 상기 오프가스 및 상기 차르를 산소 및, 선택적으로 스팀의 존재하의 플라즈마 처리 유닛 내에서 플라즈마 처리하는 단계를 포함하는 플라즈마 처리 단계를 포함한다. A method for treating waste includes: (i) a gasification step comprising (a) treating the waste in a gasification unit in the presence of oxygen and steam to produce offgas and char, or (b) removing the waste. A pyrolysis step of treating in a pyrolysis unit to produce offgas and char; And (ii) plasma treating the offgas and the char in a plasma processing unit in the presence of oxygen and, optionally, steam.

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20-11-2018 дата публикации

Method and system for production of a clean hot gas based on solid fuels

Номер: CA2734315C
Автор: Jens Dall Bentzen
Принадлежит: DALL ENERGY HOLDING APS

Solid fuel can be converted into a clean hot flue gas with a low content of volatile organic compounds (VOC's), NOx and dust, and clean ash with a low carbon content by means of a stage-divided thermal reactor, where the conversion process of the solid fuel is in separate vertical stages (from below and up): ash burn-out, char oxidation and gasification, pyrolysis, drying, and a gas combustion stage where gas from the gasifier is combusted.

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30-06-1994 дата публикации

FLUIDIZED BED REACTOR AND SYSTEM AND METHOD USING THE SAME.

Номер: MX9307081A
Автор: John Tsin-Yee Tang
Принадлежит: Foster Wheeler Energy Corp

Se describe un reactor de lecho fluidizado, y el sistema y el método para utilizar el mismo, para la combustión de sustancias combustibles de desecho, en el cual el recipiente del reactor está dividido en tres recipientes. La sustancia combustible de desecho se introduce en el lecho fluidizado, dentro de un recipiente, donde se mezcla con el material de complemento del lecho, que se controla para proporcionar un medio ambiente ideal para la generación de gases pirolíticos. El material del lecho fluidizado se transporta en forma neumática y gravitacional hacia abajo, y se inyecta en un lecho fluidizado dentro del segundo recipiente, donde el material orgánico no volátil, se somete a la combustión en una atmósfera oxidante. El material del lecho en el segundo recipiente se transporta en forma neumática hacia arriba y se divide en dos porciones, una de las cuales se recircula nuevamente al primer recipiente. La otra porción del material del lecho en el segundo recipiente, se circula a un lecho fluidizado, dentro del tercer recipiente, donde se recupera el calor. El material del lecho en el recipiente de recuperación de calor se transporta en forma gravitacional nuevamente al segundo recipiente, para regular la temperatura en este último recipiente.

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27-08-1997 дата публикации

Installation and method for heat treatment of wastes

Номер: RU2088631C1
Принадлежит: Сименс АГ

FIELD: waste disposal. SUBSTANCE: installation includes low-temperature carbonization reactor 2 for converting waste into low-temperature carbonization gas and solid residue; combustion chamber 8 receiving above-mentioned gas as fuel; apparatus 20 for separating solid residue into coarse and small particles, the latter being directed into combustion chamber to be burned. Dust-like and liquid wastes are directly introduced into combustion chamber as supplementary fuel. Combustion chamber is provided with pipeline 35 to withdraw molten slag, which is further cooled, for instance, in water bath. Smoke fumes are removed through pipeline 10. EFFECT: improved process flowsheet. 19 cl, 1 dwg $59338 0% ПЧ ГЭ РОССИЙСКОЕ АГЕНТСТВО ПО ПАТЕНТАМ И ТОВАРНЫМ ЗНАКАМ (19) ВИ” 2 088 631 ' 13) СЛ 61 МП’ С 10 В 53/00 12) ОПИСАНИЕ ИЗОБРЕТЕНИЯ К ПАТЕНТУ РОССИЙСКОЙ ФЕДЕРАЦИИ (21), (22) Заявка: 5010962/04, 05.03.1992 (30) Приоритет: 06.03.1991 ОЕ Р 4107200.6 (46) Дата публикации: 27.08.1997 (56) Ссылки: 1. Патент Великобритании М 1562492, кл. С 10 В 5300, 1980. 2. Заявка ФРГ М 3811820, кл. С 10 + 3/64, 1989. (71) Заявитель: Сименс АГ (0Е) (72) Изобретатель: Карл Май[0Е], Клаус Ридле[АТ], Херберт Тратц[ОЕ], Георг Лезель [ОЕ] (73) Патентообладатель: Сименс АГ (0Е) (54) УСТАНОВКА ДЛЯ ТЕРМИЧЕСКОЙ ОБРАБОТКИ ОТХОДОВ И СПОСОБ ТЕРМИЧЕСКОЙ ОБРАБОТКИ ОТХОДОВ (57) Реферат: Использование: в термической обработке отходов. Сущность изобретения: установка включает реактор 2 швелевания для переработки отходов в швельгаз и твердый остаток, камеру сгорания 8, к которой для сжигания подводят швельгаз, устройство 20 для разделения твердого остатка на крупные и мелкие частицы, мелкие частицы подводят к камере сгорания 8 для сжигания. Непосредственно к камере сгорания 8 подводят пылевидные отходы и/или жидкие отходы, дополнительное топливо. Камера сгорания снабжена трубопроводом 35 для отвода — расплавленного — шлака. Шлак охлаждают, например, в водяной бане. По трубопроводу 10 дымового газа отводят дымовой газ ...

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16-01-2001 дата публикации

Combustion plant

Номер: JP2001500604A

(57)【要約】 燃焼工程のための燃焼プラントは、燃焼ガスを発生しながら燃料の燃焼が行われる燃焼室1と、燃焼ガスと脱ガスされた燃焼性残余生成物とを生成するように配置されたガス化装置40とを含む。更に、燃焼プラントはガス化装置から前記残余生成物を排出し、燃焼室において残余生成物を燃焼させるため残余生成物を燃焼室へ供給するように配置された搬送手段6、44を含む。前記の供給を簡単にするために、ガス化装置から排出された残余生成物を冷却する手段45が配置されている。

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18-02-2016 дата публикации

Vertical negative pressure garbage dry-distillation incinerator free of dioxin-production and waste gas emission

Номер: WO2016023412A1
Автор: 余式正
Принадлежит: 余式正

一种无二噁英和无废气排放的立式负压垃圾干馏焚烧炉,炉子采用立式结构,炉膛内部自上而下形成干燥段、干馏段、还原段、燃烧段和灰渣段,设两层炉条把燃烧段分隔成燃烧层、续燃层和燃尽层(也是灰渣段),垃圾干燥后在干馏段分解成干馏煤气和碳化物残渣,碳化物降到燃烧段接触空气燃烧,产生的热量加热还原段的碳化物,高温的碳化物把燃烧产生的CO 2 还原生成气化煤气CO,气化煤气从垃圾周围的燃气室上升提供垃圾干馏和干燥的热量,抽风机或罗茨鼓风机收集干馏煤气和气化煤气作为资源化利用,依靠炉条的特殊设计,实现自动拨火,用燃烧温度闭环自动控制维持炉内稳定燃烧,实现不产生二噁英和无废气排放的彻底无害化,变废为宝的真正减量化和资源高效利用,以及采用标准单元组合可以组合成大型焚烧炉。

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10-12-1992 дата публикации

Automotive gas turbine starter - delivers fuel in cone from coaxial nozzle inside trumpet shaped flame holder

Номер: DE4118284A1
Принадлежит: Daimler Benz AG

The starter is for an automotive gas turbine with a pre-mixing chamber for fuel and compressed-air heated by the turbine exhaust. The combustion chamber is separated from the pre-mixing one by a central trumper-shaped flame-holder leading into it, and round which the mixture flows in an annular patter. A staring mixture of fuel and air, ignited by a sparking plug, is delivered from inside the trumpet mouth into the combustion chamber. The starting fuel is delivered from the outlet (7) of a nozzle (7) co-axial to the flame-holder (4), and in a zone. This penetrates into an annular air current flowing along the insde wall of the trumpet portion and which emanates from an annular gap (8) round the nozzle. ADVANTAGE - Prevents environmentally-harmful smoke generation and pollutant emission.

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27-05-2015 дата публикации

Apparatuses and methods for controlling heat for rapid thermal processing

Номер: EP2758491A4
Принадлежит: Ensyn Renewables Inc

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31-12-2014 дата публикации

Zero effluent discharge biomass gasification

Номер: WO2014207755A1

Zero effluent discharge biomass gasification system (100) to facilitate no effluent discharge to the environment mainly comprises of gasifier (1); double lock hopper feeding system comprises of coal charger (20) comprising of coal feeding system (19) and coal feeding hopper (21); water sealed controlled gas shut off valve (25); primary gas cooler cum settling chamber (2); tar catcher (3); two way water seal controlled valve-1 (4); indirectly cooled final gas cooler cum settling chamber (10); sets of gas condenser-1 (5) and gas condenser-2 (6) and gas condenser-3 (7) and gas condenser-4 (8); through two-way water sealed controlled valve-2 (9) chilled water from water chilling plant (13); settling chamber (10); a rotary kiln cum effluent evaporator (11); tar and tarry waste water storage tank (30); high pressure tar pump (18); a burner (11a); producer gas supply pipe to the tar cracker (29); producer gas supply pipe to plant (31); rotary kiln (11b); Nickel or Tungston wire mesh catalyst (11c); kiln exit section (11d); effluent evaporator (11e) and sealed blower (23)

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17-04-2020 дата публикации

Air-classified regulation and control pyrolysis and combustion integrated furnace

Номер: CN108758638B
Автор: 王一迪, 王伟, 陈坦
Принадлежит: TSINGHUA UNIVERSITY

本发明公开了一种空气分级调控热解燃烧一体炉,包括一热解炉主体,所述热解炉主体被耐火层围合形成一燃烧加热区,所述热解炉主体上开设有第一进气口,所述第一进气口与燃烧器相连通,其中,所述热解炉主体还包括一斜向穿过所述燃烧加热区的螺杆热解管,所述螺杆热解管顶部设置有搅拌料斗,生物质废物经所述搅拌料斗处理后进入螺杆热解管内,所述螺杆热解管顶部还设置有一合成气导管,所述合成气导管一端与所述螺杆热解管顶部相连通,另一端伸入至所述燃烧加热区内。本发明解决了原有的热解设备在热解过程中容易产生焦油造成设备凝结的问题。

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24-09-2003 дата публикации

Waste-gasified fusion furnace and method of operating the fusion furnace

Номер: EP1347236A1

A waste gasification-melting furnace comprises a gasifying furnace body 2 of a shaft furnace type, for drying and thermally decomposing waste sequentially supplied from above into the furnace 1 by using a high-temperature gas; and a melting chamber furnace 3 provided integrally with a lower end discharge port 2b of the gasifying furnace body 2, for receiving residue of the waste A resulting from pyrolysis, the melting chamber furnace 3 being provided with a heating and melting burner directed toward a slope of the residue, wherein the melting chamber furnace 3 is provided with a discharge port 6 through which molten substances containing molten slag and molten metal are discharged, and a gas feeding pipe 8 connected to a header duct 9, for feeding the high-temperature gas generated during heating and melting the residue inside the melting chamber furnace 3 to the gasifying furnace body 2.

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30-08-2012 дата публикации

Heat removal and recovery in biomass pyrolysis

Номер: CA2828037A1
Принадлежит: Ensyn Renewables Inc

Pyrolysis methods and apparatuses that allow effective heat removal, for example when necessary to achieve a desired throughput or process a desired type of biomass, are disclosed. According to representative methods, the use of a quench medium (e.g., water), either as a primary or a secondary type of heat removal, allows greater control of process temperatures, particularly in the reheater where char, as a solid byproduct of pyrolysis, is combusted. Quench medium may be distributed to one or more locations within the reheater vessel, such as above and/or within a dense phase bed of fluidized particles of a solid heat carrier (e.g., sand) to better control heat removal.

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23-08-2006 дата публикации

Fuel gasification system

Номер: CN1271176C
Принадлежит: Ebara Corp

一种集成气化炉包括气化室(1),用于气化其中的流化介质以形成具有界面的气化室流化床,焦炭燃烧室(2),用于燃烧在气化室中气化生成的焦炭,并加热流化介质以形成类似的具有界面的流化床,和能量回收装置(3),其中,(1)和(2)整体构建,并由在流化床界面垂直上方的位置的隔板隔开,并且,在隔板的下部提供连通(1)和(2)开孔,由此,在(2)中被加热的流化介质经此开口从(2)流入(1)。上述设置消除了对气化炉与焦炭燃烧炉之间的压力平衡控制和机械流化介质处理装置的需求,确保了质量优异的生成气体的稳定供应,并提供了能高效地回收能量的燃料气化方法。即使使用含有氯的可燃废物材料作为燃料,也能使蒸汽过热器(管)的腐蚀最低化,并高效地发电。

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08-06-2016 дата публикации

Charcoal processing method in pyrolysis system

Номер: CN103380196B
Принадлежит: Ensyn Renewables Inc

提供用于控制再热器中的整体热平衡、灰分累积和后燃的碳处理方法。使用传热介质热解含碳的生物质原料,形成热解产物和减效的传热介质。将该减效的传热介质分为分离炭和炭贫化的减效的传热介质。将该炭贫化的减效的传热介质引入传热介质的密相床层,该密相床层由含氧的再生气体流流化。使用该含氧的再生气体流,在该密相床层中燃烧该分离炭的全部或部分。可以将该分离炭的部分排出热解系统,以控制所述整体热平衡和灰分累积。

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01-11-2001 дата публикации

POWER SYSTEMS INTENDED FOR A PROCEDURE AND INSTALLATION OF CONTINUOUS GASIFICATION AND GASIFICATION.

Номер: ES2160258T3
Принадлежит: Compact Power Ltd

LA INVENCION SE REFIERE A UN METODO PARA CARGAR UN REACTOR PIROLITICO DE PRODUCCION DE GAS CON COMBUSTIBLE RESIDUAL, DE FORMA QUE DICHO COMBUSTIBLE SE INTRODUCE A PRESION EN EL INTERIOR DEL REACTOR MEDIANTE UN PISTON Y EVITANDOSE LA ENTRADA DE AIRE EN EL REACTOR Y EL ESCAPE DE GASES DE PIROLISIS MEDIANTE CIERRE HERMETICO ABLATIVO, SITUADO ENTRE EL COMBUSTIBLE Y EL PISTON. DICHO CIERRE SE INTRODUCE A PRESION EN EL REACTOR MEDIANTE LA ACCION DEL PISTON SOBRE LA CARGA DE COMBUSTIBLE, SITUANDOSE SIMULTANEAMENTE EN CONTACTO HERMETICO CON LAS PAREDES INTERNAS DEL REACTOR Y ESTA HECHO DE UN MATERIAL RESISTENTE A LAS ELEVADAS TEMPERATURAS Y A LAS CONDICIONES QUIMICAS DEL INTERIOR DEL REACTOR, DURANTE UN PERIODO AL MENOS TAN LARGO COMO SEA REQUERIDO POR EL CIERRE HERMETICO PARA LLEVAR A CABO SU FUNCION DE CIERRE. A CONTINUACION, SE DESCOMPONE TERMICAMENTE EN PRODUCTOS QUE NO SON NOCIVOS PARA EL PROCESO PIROLITICO O PARA LOS GASES PIROLITICOS PRODUCIDOS POR EL REACTOR. ASIMISMO, SE DESCRIBE UN METODODE ALIMENTACION DE MATERIALES PARTICULADOS AL INTERIOR O A TRAVES DE UN RECIPIENTE TUBULAR. DICHO METODO CONSISTE EN EMPUJAR EL MATERIAL A TRAVES DEL RECIPIENTE, POR EJEMPLO MEDIANTE MEDIOS DE PISTON, Y EVITAR O REMEDIAR EL ATASCO DEL MATERIAL PARTICULADO COMPACTO, MEDIANTE LA APLICACION DE UNA FUERZA NEUTRA O NEGATIVA AL MATERIAL, EN UNA POSICION AGUAS ARRIBA RESPECTO A LA POSICION EN LA CUAL SE PRODUCIRIA EN CASO CONTRARIO EL ATASCO. THE INVENTION REFERS TO A METHOD FOR LOADING A GAS PRODUCTION PIROLITIC REACTOR WITH RESIDUAL FUEL, SO THAT SUCH FUEL IS INTRODUCED PRESSELY INSIDE THE REACTOR BY A PISTON AND AVOIDING THE AIR INTAKE IN THE REACTOR AND ESCAPE GASES OF PIROLISIS THROUGH ABLATIVE HERMETIC CLOSURE, SITUATED BETWEEN THE FUEL AND THE PISTON. SUCH CLOSURE IS INTRODUCED PRESSELY IN THE REACTOR THROUGH THE PISTON'S ACTION ON THE FUEL LOAD, SITUATING SIMULTANEOUSLY IN HERMETIC CONTACT WITH THE INTERNAL WALLS OF THE REACTOR AND IS MADE OF A MATERIAL RESISTANT TO THE HIGH ...

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05-06-1996 дата публикации

Process for the elimination of the residues of the waste incinerators like active carbon and/or active coal

Номер: EP0714679A1
Автор: John Dr. Rizzon
Принадлежит: Metallgesellschaft AG

The method involves one or more burners (7) being positioned in the cover (10) of the oven's (1) primary chamber (2). On one or more points (22) on the oven cover, secondary air is introduced into the primary chamber, and at one or more points on the oven cover, tertiary air is introduced into the primary chamber. The primary and secondary air is oxygen enriched air. The residue, active coke and/or active carbon are inserted into the oven's primary chamber set to a temperature of 1250 to 1500 degrees C. The molten material discharged leaves the primary chamber with flue gases. The molten material is run through the secondary chamber (5) and disposed of as slag.

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30-11-2001 дата публикации

FEEDING SYSTEMS FOR A CONTINUOUS PYROLYSIS AND GASIFICATION PROCESS AND APPARATUS

Номер: PT873382E
Принадлежит: Compact Power Ltd

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27-09-2001 дата публикации

Exploitation of hydrocarbon-containing wastes, produces combustible fuel by distillation of feedstock at atmospheric pressure, excluding air

Номер: DE10010163A1
Автор: Ralf Laskowski
Принадлежит: Individual

Das Gebiet, auf das sich die Erfindung bezieht, ist das thermische Cracken kohlenwasserstoffhaltiger Eintragsstoffe. Ein bevorzugtes Anwendungsgebiet der Erfindung ist die Verwertung von Altstoffen wie Altöl, Abfallfetten aus Gaststätten oder Schlachtereien bzw. der Fleisch- und Wurstwarenproduktion, Altgummi, Polymeren, Holzspänen und anderen kohlenwasserstoffhaltigen Altstoffen auch in Form von Gemischen. Die Aufgabe der Erfindung besteht darin, eine Technologie zur Verwertung von kohlenwasserstoffhaltigen Altstoffen zu schaffen, die sich durch einfach beherrschbare Prozeßbedingungen sowie die Vermeidung des Entstehens von insbesondere schadstoffhaltigen Nebenprodukten auszeichnet und darüber hinaus für eine dezentrale Anwendung in Wohngebieten geeignet ist. Die Aufgabe wird erfindungsgemäß gelöst durch ein Verfahren zur Verwertung von kohlenwasserstoffhaltigen Altstoffen durch Spalten und Verbrennung eines kondensierten Spaltprodukts zur Erzeugung von Reaktionswärme sowie eine Anlage zur Durchführung des Verfahrens, wobei die Eintragsstoffe unter Luftabschluß bei 180 bis 250 DEG C verdampfen, anschließend der Abdampf unter Luftabschluß kondensiert, das Kondensat bei atmosphärischem Druck gesammelt und danach der Verbrennung zugeführt wird.

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14-07-2017 дата публикации

The small-sized domestic garbage pyrolysis processing system of villages and small towns level

Номер: CN106949479A
Автор: 饶勇
Принадлежит: Individual

本发明涉及垃圾处理技术领域,具体涉及村镇级小型生活垃圾热解处理系统;包括依次连通设置的热解炉、除硫脱硝喷淋塔、旋风除尘器、二恶英去除塔及循环冷却水净化池,所述热解炉内设置有一燃室,所述一燃室还连通设置有二燃室,所述一燃室内设置有旋转搅拌破桥机构,所述旋转搅拌破桥机构包括中部设置的幅轮和设置在下端可往下运动的顶杆,所述旋转搅拌破桥机构下方设置有翻板式炉排机构,所述二恶英去除塔内设置有双极文丘里射流曝气机,所述双极文丘里射流曝气机包括两个双极文丘里管、与两个双极文丘里管连接的空压机、热解焚烧高温烟气管道及冷却水管道,所述循环冷却水净化池与二恶英去除塔的顶部连通;本发明可简化垃圾前处理工艺,降低垃圾处理成本和设备投资,同时有效去除二恶英。

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19-01-1991 дата публикации

Patent IN167988B

Номер: IN167988B
Принадлежит: Neutralysis Ind Pty Ltd

PCT No. PCT/AU87/00338 Sec. 371 Date May 20, 1988 Sec. 102(e) Date May 20, 1988 PCT Filed Oct. 2, 1987 PCT Pub. No. WO88/02284 PCT Pub. Date Apr. 7, 1988.Method and apparatus for treating waste materials to produce aggregates wherein pellets comprised of a mixture of solids, liquid wastes and clay are dried by hot air in a dryer. The pellets are then fed to the pyrolysis zone of a rotary kiln wherein they are heated by hot gas from an oxidation zone of the kiln to drive off most of the volatile gases. Remaining volatile gases and the fixed carbon in the waste are oxidized in the oxidation zone, and the silicates in the clay are vitrified in a vitrification zone of the kiln to produce aggregates which are crushed and screened. Volatile gases given off from the pyrolysis zone are mixed with exhaust gases from the dryer to feed the burner for the vitrification zone and to supply oxygen to the oxidation zone.

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03-02-1998 дата публикации

Multi-fuel, combined cycle power plant method and apparatus

Номер: US5713195A
Принадлежит: Ormat Industries Ltd

A power plant includes a gas turbine unit having a compressor for compressing ambient air, a burner for burning fuel and heating air compressed by said compressor, and a turbine for expanding air heated by said burner to drive said compressor and produce hot exhaust gases. The plant further includes a combustor for containing particles of solid fuel which are fluidized by the exhaust gases from the turbine to produce hot products of combustion that include coarse ash particulate. Apparatus is provided for generating power from the hot products of combustion.

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07-08-2013 дата публикации

Gasification furnace structure of gasification equipment

Номер: JP5256802B2
Принадлежит: IHI Corp

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