专利摘要:
A method of treating process gases coming from a gasification reactor before entry of such process gases into a system of waste heat utilization. The process gases are cooled off to a temperature of at least 800 DEG C. before entry thereof into the waste heat system. Thereafter, the gases are extensively freed of solid matter in a cyclone separator system located ahead of the convective cooling system, and thereafter the gases are cooled off further to a temperature of at least 250 DEG C. in a convective cooling system.
公开号:SU1456020A3
申请号:SU823493800
申请日:1982-09-20
公开日:1989-01-30
发明作者:Дерлинг Рольф;Премель Ульрих
申请人:Л.Унд Ц.Штайнмюллер Гмбх (Фирма);
IPC主号:
专利说明:

one
The invention relates to a method for treating generator gases produced in gas generators before entering them in a heat recovery system.
The purpose of the invention is to increase the efficiency of heat transfer and reduce energy consumption.
The drawing shows a diagram of an apparatus for carrying out the method.
The generator gas leaving the gas generator with a temperature of 1500 ° C is cooled in the pipeline 1 to or below by indirect heat exchange on the pipe cooling surfaces 2 (such as a pipe in a pipe). Between the pipe surfaces 2 and the wall of the pipeline 1, an insulating padding mass 3 is additionally provided. Pipeline 1 is provided on the outside with -. cleaning elements 4 that clean the cooling surfaces as they become soiled. The gases then enter the cyclone 5, in which a part of the solid particles in the gas is deposited.
This cyclone is installed in tank 6. In the cyclone, mixing of the generating gas that started in pipeline 1 continues due to the presence of solid particles in the gas stream. The heat recovery boiler, in which convective heat exchange is carried out, is provided with various cooling surfaces 7 and 8, 9 and 10 arranged along the walls of the boiler, made in the form of
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权利要求:
Claims (1)
[1]
5 claims
A method of treating generator gases produced in gas generators, comprising separating solid particles from gas, supplying gas to a convective cooling system, followed by cooling to 250 ° C or lower, characterized in that, 15, in order to increase heat transfer efficiency and reduce energy consumption, gas before feeding in a convective cooling system, they are pre-cooled to 800 ° C or lower by 20 by means of indirect heat exchange on cooling surfaces that are cleaned as they become contaminated by treatment devices.
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同族专利:
公开号 | 公开日
GB2106931B|1985-06-12|
GB2106931A|1983-04-20|
AU553323B2|1986-07-10|
NL8203432A|1983-04-18|
AU8814782A|1983-03-31|
ZA826804B|1983-07-27|
JPS5858127A|1983-04-06|
FR2513139A1|1983-03-25|
US4478608A|1984-10-23|
DE3137586A1|1983-04-07|
DE3137586C2|1987-08-20|
引用文献:
公开号 | 申请日 | 公开日 | 申请人 | 专利标题

BE519600A|1952-05-10|
JPS5233768B2|1972-04-26|1977-08-30|
US3991557A|1974-07-22|1976-11-16|Donath Ernest E|Process for converting high sulfur coal to low sulfur power plant fuel|
US4018267A|1975-01-10|1977-04-19|Dorr-Oliver Incorporated|Cleaning heat exchanger tubes|
JPS5726632B2|1976-09-17|1982-06-05|
DE2650512B2|1976-11-04|1980-03-20|Gutehoffnungshuette Sterkrade Ag, 4200 Oberhausen|Device for cleaning synthesis gas produced by chemical coal gasification|
US4270493A|1979-01-08|1981-06-02|Combustion Engineering, Inc.|Steam generating heat exchanger|
DE2918859C2|1979-05-10|1983-12-01|Carl Still Gmbh & Co Kg, 4350 Recklinghausen|Gas generator for partially gasifying coal|
US4251228A|1979-05-30|1981-02-17|Texaco Development Corporation|Production of cleaned and cooled synthesis gas|
US4324563A|1979-07-13|1982-04-13|Texaco Inc.|Gasification apparatus with means for cooling and separating solids from the product gas|
GB2053262B|1979-07-13|1983-08-24|Texaco Development Corp|Process and apparatus for producing gaseous mixtures including h2 and co|
US4248604A|1979-07-13|1981-02-03|Texaco Inc.|Gasification process|
DE2951153C2|1979-12-19|1981-11-12|M.A.N. Maschinenfabrik Augsburg-Nürnberg AG, 4200 Oberhausen|Device for cleaning and synthesis gas produced by coal gasification|
CH653360A5|1980-09-19|1985-12-31|Sulzer Ag|HEISSGASKUEHLER AT A coal gasification plant.|GB8312103D0|1983-05-04|1983-06-08|Shell Int Research|Cooling and purifying hot gas|
DE3737359A1|1987-11-04|1989-05-18|Krupp Koppers Gmbh|COOLING BOILER FOR COOLING PARTIAL OXIDATION RAW GAS|
US4838898A|1988-06-30|1989-06-13|Shell Oil Company|Method of removal and disposal of fly ash from a high-temperature, high-pressure synthesis gas stream|
US4859214A|1988-06-30|1989-08-22|Shell Oil Company|Process for treating syngas using a gas reversing chamber|
US5112366A|1990-12-17|1992-05-12|Shell Oil Company|Slag deposition detection|
US5803937A|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|
US5738710A|1995-08-08|1998-04-14|Morikawa Industries Corporation|Control method and apparatus for material adsorbed on adsorbent, and solvent recovering method and apparatus using same|
JP5107903B2|2005-05-02|2012-12-26|シエル・インターナシヨネイル・リサーチ・マーチヤツピイ・ベー・ウイ|Syngas production method and system|
US7587995B2|2005-11-03|2009-09-15|Babcock & Wilcox Power Generation Group, Inc.|Radiant syngas cooler|
JP4847924B2|2006-12-26|2011-12-28|日信工業株式会社|Vehicle disc brake|
US8357215B2|2009-03-04|2013-01-22|General Electric Company|Method and apparatus of particulate removal from gasifier components|
CN102888251B|2012-09-17|2014-07-16|北京神雾环境能源科技集团股份有限公司|Coal-based synthetic gas waste heat recovery system and method|
法律状态:
优先权:
申请号 | 申请日 | 专利标题
DE3137586A|DE3137586C2|1981-09-22|1981-09-22|
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