RU94008855A - METHOD OF GASIFICATION UNDER PRESSURE OF HIGHLY WASTE COMBUSTIBLE - Google Patents

METHOD OF GASIFICATION UNDER PRESSURE OF HIGHLY WASTE COMBUSTIBLE

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Publication number
RU94008855A
RU94008855A RU94008855/04A RU94008855A RU94008855A RU 94008855 A RU94008855 A RU 94008855A RU 94008855/04 A RU94008855/04 A RU 94008855/04A RU 94008855 A RU94008855 A RU 94008855A RU 94008855 A RU94008855 A RU 94008855A
Authority
RU
Russia
Prior art keywords
gas
cooling
pipe
crude gas
gasification
Prior art date
Application number
RU94008855/04A
Other languages
Russian (ru)
Other versions
RU2122565C1 (en
Inventor
Дюррфельд Райнер
Коволь Йоханнес
КУСКЕ Эберхард
Нирманн Ханс
Вильмер Герхард
Вольфф Йоахим
Original Assignee
Крупп-Копперс ГмбХ
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from EP93104291A external-priority patent/EP0616022B1/en
Application filed by Крупп-Копперс ГмбХ filed Critical Крупп-Копперс ГмбХ
Publication of RU94008855A publication Critical patent/RU94008855A/en
Application granted granted Critical
Publication of RU2122565C1 publication Critical patent/RU2122565C1/en

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Claims (1)

Способ газификации под давлением высокодисперсных горючих состоит в том, что в сосуде под давлением, который рассчитан на давление процесса газификации под давлением, концентрически располагаются реактор газификации, труба для (быстрого) охлаждения и конвекционный котел. Выходящий из реактора газификации аксиально вверх неочищенный газ вводится в прикрепленную вверху трубу для охлаждения. Вводится холодный газ. Смешанный газовый поток из неочищенного газа и холодного газа с помощью ротационно-симметричного в отношении оси трубы для охлаждения поворотного заслона изменяет направление на 180° и преобразуется в имеющий форму идущего по полому цилиндру газовый поток. Такой газовый поток вводится в выполненный в виде полого цилиндра конвекционный котел, который концентрически окружает трубу для охлаждения. Поток неочищенного газа при выходе из конвекционного котла отводится из него с помощью устройства для отвода неочищенного газа. Скорость потока неочищенного газа устанавливается так, чтобы увлеченные с неочищенным газом частицы шлаков и золы за счет изменения направления на 180° вносились в выполненный в виде пологого цилиндра конвекционный котел. Скорость потока в устройстве для отвода неочищенного газа устанавливается так, что увлеченные частицы шлаков и золы выносятся.The method of gasification under the pressure of highly dispersed combustible is that in the pressure vessel, which is designed for the pressure of the gasification process under pressure, the gasification reactor, the pipe for (rapid) cooling and the convection boiler are located concentrically. The crude gas exiting the gasification reactor axially upwards is introduced into the top-mounted pipe for cooling. Cold gas is injected. The mixed gas stream from the crude gas and the cold gas is rotated symmetrically with respect to the axis of the pipe for cooling the rotary valve and changes direction by 180 ° and is converted into a gas stream having a shape going through the hollow cylinder. Such a gas stream is introduced into a convection boiler made in the form of a hollow cylinder, which concentrically surrounds the pipe for cooling. The flow of crude gas at the exit of the convection boiler is discharged from it using a device for venting the raw gas. The flow rate of the crude gas is set so that particles of slags and ash entrained with the crude gas are brought into the convection boiler made in the form of a gentle cylinder by changing the direction by 180 °. The flow rate in the device for removal of the crude gas is set so that the entrained particles of slag and ash are removed.
RU94008855A 1993-03-16 1994-03-15 Method of gasifying fine fuels under pressure RU2122565C1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
EP93104291A EP0616022B1 (en) 1993-03-16 1993-03-16 Process for pressure gasification of fine particulate fuels
EP93104291.5 1993-03-16

Publications (2)

Publication Number Publication Date
RU94008855A true RU94008855A (en) 1995-11-10
RU2122565C1 RU2122565C1 (en) 1998-11-27

Family

ID=8212704

Family Applications (1)

Application Number Title Priority Date Filing Date
RU94008855A RU2122565C1 (en) 1993-03-16 1994-03-15 Method of gasifying fine fuels under pressure

Country Status (10)

Country Link
US (1) US5441547A (en)
EP (1) EP0616022B1 (en)
CN (1) CN1041107C (en)
DE (1) DE59300598D1 (en)
DK (1) DK0616022T3 (en)
ES (1) ES2078078T3 (en)
GR (1) GR3018065T3 (en)
PL (1) PL173329B1 (en)
RU (1) RU2122565C1 (en)
ZA (1) ZA939354B (en)

Families Citing this family (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5803937A (en) * 1993-01-14 1998-09-08 L. & C. Steinmuller Gmbh Method of cooling a dust-laden raw gas from the gasification of a solid carbon-containing fuel
DE102007027601A1 (en) 2007-06-12 2008-12-18 Uhde Gmbh Production and cooling of gaseous coal gasification products
DE102008012734A1 (en) 2008-03-05 2009-09-10 Uhde Gmbh Method for obtaining synthesis gas by gasification of liquid or finely comminuted solid fuels, involves producing synthesis gas in reaction chamber arranged over reactor, in which ingredients are supplied
KR101568433B1 (en) 2007-09-18 2015-11-11 티센크루프 인더스트리얼 솔루션스 아게 Gasification reactor and method for entrained-flow gasification
DE102007044726A1 (en) 2007-09-18 2009-03-19 Uhde Gmbh Synthesis gas producing method, involves drying and cooling synthesis gas in chamber, arranging water bath below another chamber, and extracting produced and cooled synthesis gas from pressure container below or lateral to latter chamber
DE102008012732A1 (en) * 2008-03-05 2009-09-10 Uhde Gmbh Gasification device with slag removal
DE102009005464A1 (en) 2009-01-21 2010-08-05 Uhde Gmbh Device for producing crude gas containing carbon monoxide or hydrogen by gasification of an ash-containing fuel with oxygen-containing gas in a gasification reactor, comprises connected gas cooling chamber, and tapered connecting channel
DE102008015801B4 (en) 2008-03-27 2019-02-28 Thyssenkrupp Industrial Solutions Ag Apparatus for the production of synthesis gas with a gasification reactor followed by a quenching chamber
BRPI0910041B1 (en) 2008-03-27 2018-02-06 Uhde Gmbh "DEVICE FOR THE PRODUCTION OF GROSS GAS, WITH CO OR H2 CONTENT, BY GASIFICATION OF GRAY FUEL"
DE102008057410B4 (en) 2008-11-14 2019-07-04 Thyssenkrupp Industrial Solutions Ag Apparatus for the production of synthesis gas with a gasification reactor followed by quenching
US8357215B2 (en) * 2009-03-04 2013-01-22 General Electric Company Method and apparatus of particulate removal from gasifier components
US20100325956A1 (en) * 2009-06-30 2010-12-30 General Electric Company Cooling chamber assembly for a gasifier
DE102009034867A1 (en) * 2009-07-27 2011-02-03 Uhde Gmbh gasification reactor
DE102011107726B4 (en) 2011-07-14 2016-06-30 Thyssenkrupp Industrial Solutions Ag Apparatus and method for introducing renewable fuels into the region of the radiation vessel wall of gasification reactors
DE102011110213A1 (en) 2011-08-16 2013-02-21 Thyssenkrupp Uhde Gmbh Method and device for recirculating exhaust gas from a gas turbine with subsequent waste heat boiler
JP5518161B2 (en) * 2012-10-16 2014-06-11 三菱重工業株式会社 Gasifier

Family Cites Families (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR1070615A (en) * 1951-12-12 1954-08-03 Babcock & Wilcox France Steam generator combined with a syngas production device
DE1596323A1 (en) * 1967-06-06 1970-04-02 Walther & Cie Ag Synthesis gas generator with gas cooler, which are arranged in a pressure cylinder
DE3107156A1 (en) * 1981-02-26 1982-09-16 L. & C. Steinmüller GmbH, 5270 Gummersbach SYSTEM FOR THE PRODUCTION OF GASEOUS PRODUCTS
CH656637A5 (en) * 1981-10-26 1986-07-15 Sulzer Ag GAS COOLER ARRANGEMENT TO COAL GASIFICATION SYSTEM.
FR2530796A1 (en) * 1982-07-21 1984-01-27 Creusot Loire THERMAL CONVERSION AND RECOVERY DEVICE
EP0115094A3 (en) 1982-12-29 1985-05-22 Shell Internationale Researchmaatschappij B.V. Process and apparatus for the production of synthesis gas
GB2164951A (en) * 1984-09-26 1986-04-03 Shell Int Research Method and apparatus for producing synthesis gas
DE3711314A1 (en) * 1987-04-03 1988-10-13 Babcock Werke Ag DEVICE FOR COOLING A SYNTHESIS GAS IN A QUENCH COOLER
DE3809313A1 (en) * 1988-03-19 1989-10-05 Krupp Koppers Gmbh METHOD AND DEVICE FOR COOLING PARTIAL OXIDATION GAS
DE3816340A1 (en) * 1988-05-13 1989-11-23 Krupp Koppers Gmbh METHOD AND DEVICE FOR COOLING A HOT PRODUCT GAS THAT STICKY OR. MELT-LIQUID PARTICLES INCLUDED
US4859213A (en) * 1988-06-20 1989-08-22 Shell Oil Company Interchangeable quench gas injection ring
US4859214A (en) * 1988-06-30 1989-08-22 Shell Oil Company Process for treating syngas using a gas reversing chamber
DE3824233A1 (en) * 1988-07-16 1990-01-18 Krupp Koppers Gmbh PLANT FOR THE PRODUCTION OF A PRODUCT GAS FROM A FINE-PARTIC CARBON SUPPORT
DD280975B3 (en) * 1989-03-31 1993-03-04 Noell Dbi Energie Entsorgung METHOD AND DEVICE FOR COOLING AND CLEANING GASES LOADED WITH SLUDGE OR DUST
JP2659849B2 (en) * 1990-05-30 1997-09-30 三菱重工業株式会社 Pressurized gasifier

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