DD150313A3 - Device for gasification of absorbent fuels in flying cloud - Google Patents

Device for gasification of absorbent fuels in flying cloud Download PDF

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Publication number
DD150313A3
DD150313A3 DD20815878A DD20815878A DD150313A3 DD 150313 A3 DD150313 A3 DD 150313A3 DD 20815878 A DD20815878 A DD 20815878A DD 20815878 A DD20815878 A DD 20815878A DD 150313 A3 DD150313 A3 DD 150313A3
Authority
DD
German Democratic Republic
Prior art keywords
cooling
slag
reaction space
gasification
ash
Prior art date
Application number
DD20815878A
Other languages
German (de)
Inventor
Friedrich Berger
Peter Goehler
Dieter Koenig
Klaus-Otto Kuhlbrodt
Klaus Lucas
Helmut Peise
Manfred Schingnitz
V P Semenov
E A Gudymov
A I Jegorov
N P Majdurov
I G Achmatov
V P Gavrilin
V G Fedotov
E V Avraamov
Original Assignee
Friedrich Berger
Peter Goehler
Dieter Koenig
Kuhlbrodt Klaus Otto
Klaus Lucas
Helmut Peise
Manfred Schingnitz
V P Semenov
E A Gudymov
A I Jegorov
N P Majdurov
I G Achmatov
V P Gavrilin
V G Fedotov
E V Avraamov
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
Application filed by Friedrich Berger, Peter Goehler, Dieter Koenig, Kuhlbrodt Klaus Otto, Klaus Lucas, Helmut Peise, Manfred Schingnitz, V P Semenov, E A Gudymov, A I Jegorov, N P Majdurov, I G Achmatov, V P Gavrilin, V G Fedotov, E V Avraamov filed Critical Friedrich Berger
Priority to DD20815878A priority Critical patent/DD150313A3/en
Publication of DD150313A3 publication Critical patent/DD150313A3/en

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Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/46Gasification of granular or pulverulent flues in suspension
    • C10J3/48Apparatus; Plants
    • C10J3/485Entrained flow gasifiers
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/02Fixed-bed gasification of lump fuel
    • C10J3/06Continuous processes
    • C10J3/08Continuous processes with ash-removal in liquid state
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/46Gasification of granular or pulverulent flues in suspension
    • C10J3/48Apparatus; Plants
    • C10J3/52Ash-removing devices
    • C10J3/526Ash-removing devices for entrained flow gasifiers
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/72Other features
    • C10J3/74Construction of shells or jackets
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/72Other features
    • C10J3/74Construction of shells or jackets
    • C10J3/76Water jackets; Steam boiler-jackets
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/72Other features
    • C10J3/78High-pressure apparatus
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/72Other features
    • C10J3/82Gas withdrawal means
    • C10J3/84Gas withdrawal means with means for removing dust or tar from the gas
    • C10J3/845Quench rings
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00Details of gasification processes
    • C10J2300/09Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0913Carbonaceous raw material
    • C10J2300/093Coal
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00Details of gasification processes
    • C10J2300/09Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0953Gasifying agents
    • C10J2300/0956Air or oxygen enriched air
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00Details of gasification processes
    • C10J2300/09Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0953Gasifying agents
    • C10J2300/0959Oxygen
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00Details of gasification processes
    • C10J2300/09Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0953Gasifying agents
    • C10J2300/0969Carbon dioxide
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00Details of gasification processes
    • C10J2300/09Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0953Gasifying agents
    • C10J2300/0973Water
    • C10J2300/0976Water as steam

Abstract

The invention relates to a device for gasifying ash-containing fuels with a gasification agent containing free oxygen in the flying cloud and at temperatures above the melting point of the ash, preferably under elevated pressure. The object of the invention is the design of a reactor for the gasification of ash-containing fuels in the flying cloud, in which the safe Überefuehrung the molten slag formed in the reaction chamber, optionally together with hot, formed in the reaction space gas, is guaranteed in a cooling and Granulierteil. According to the invention, the slag-removal opening, which projects beyond the bottom of the reaction space, has one or more depressions, at which or which the liquid slag flows over like a jet and enters the cooling zone as a compact jet.

Description

-λ- 20 8 15 8

Apparatus for gasifying ash-containing fuels in the flying cloud

Field of application of the invention

The invention relates to an apparatus for gasifying ash-containing fuels with a gasification agent containing free oxygen in the flying cloud and at temperatures above the melting point of the ash, preferably under elevated pressure.

Characteristic of the known technical solutions In the technology of "gas production, the gasification of pulverized coal with a mixture of oxygen and water vapor or carbon dioxide has been introduced as a pandemic reaction in the plug cloud, in which the gasification takes place at such temperatures that the mineral constituents of the In principle, the same technologies are used for the gasification of ash-rich liquid fuels (tars, residual oils) and mixtures of suspensions of liquid and ash-containing solid fuels, especially when the gasification takes place under elevated pressure, the 'difficult technical task to perform the gasification serving reactor so that the Schlackenfluß dominated and the slag can be safely discharged from the system .. There are technical solutions usual

- 2 - 2 0 8 15 8

in which the molten liquid slag is granulated and cooled in water within the reactor and suspended as granules suspended in water from the pressure system is discharged. The operability of such reactors is the design of the sluice sluice-spout from the hot part of the reactor, the reaction chamber in the strict sense, in the cooling and Granulierteil decisive »In the GDR exclusion patent 119 266 a reactor for the gasification of pulverized coal under pressure is described Its reaction space consists of a wasserbeaufschlagten, protected by a layer of refractory ramming tube wall construction. "For the flow of liquid slag in the Granulierteil a central opening in the bottom of the reaction space is provided, the contours are formed by the correspondingly designed pipe wall construction with ramming mass coating. The bottom of the reaction space is slightly inclined towards the Schlackenabflußöffnung. The opening is provided with a sharp Schlaeken drip edge.

There is a similar solution in principle known for a little above the atmospheric pressure gasification plant, where the upper edge of the central SchlakkeablaufÖffnung is like a dam, so that the slag is accumulated on the floor of the reaction space and overflows over the dam (Ullmann's Encyclopadie der technischen Chemie , 3rd edition, Volume 1o, page 416, 1958) "It is also known to transfer liquid slag and hot gas via a bottom opening with drip edge together in a cooling space, see, for. B. Meunier, Gasification of Solid Fuels ..., Weinheim / Bergstraße, 1962, page 453 ·

Finally, DP-OS 2-325 2o4 describes a reactor for the pulverization of coal dust under pressure, in which hot gas and liquid slag are common

20 8 15 8

withdrawn downwards via a central opening in the bottom of the reaction space, whereby a slag bath is maintained at the bottom of the reaction space through a dam around the central opening »

The load on the slag discharge opening due to the action of the liquid slag and the high temperatures in the reaction space is considerable. It is increased even more when hot reaction gas is simultaneously discharged from the reaction space through this slag discharge opening. In case of execution in ceramic material infiltration of the liquid slag into the stone material or dissolution of the ceramic material or a part of the structural constituents of the ceramic material in the slag in the long run is inevitable "When executed as a tube construction with coating by ramming mass is for the same reasons and because of local differences in heat dissipation from the ramming layer in the cooling pipes often ragged locally rammed mass. This leads to the breaking out of the protective layer and to local overheating of the pipe walls. As a result, the slag discharge opening becomes a wearing part, which limits the travel time of the entire unit.

Object of the invention

The aim of the invention is an apparatus for gasifying ash-containing fuels, in particular coal dust with a free oxygen-containing gasification agent as a plam reaction in the plug cloud, in spite of seizure of liquid slag in the reaction chamber high reliability and long travel time is guaranteed.

20,8158

Explanation of the essence of the invention

- The object of the invention is the design of a reactor for the gasification ash-containing fuels, in particular coal dust with a free oxygen-containing gasification agent as IPlammenreaktion in the plug cloud, consisting of a reaction space for. the course of the gasification reaction at Teniperaturen above the melting point of the ash · and a cooling and granulation below it, in which the safe transfer of the molten slag formed in the reaction chamber optionally together with hot, formed in the reaction space gas, in a: Cooling and granulating guaranteed and which is suitable for operation under elevated pressure,

- According to the invention this object is achieved in that the bottom of the reaction space is provided with a preferably centrally located, consisting of a recessed into the ground annular body slag discharge opening, which connects the reaction space with the cooling and Granulierteil "

The upper edge of the annular body protrudes like a dam above the surrounding bottom of the reaction space. With this embodiment, the liquid slag located at the bottom of the reaction space is dammed up in order to increase its residence time in the hot reaction space and to homogenize the composition and splitting properties of the slag.

The dam-like above the surrounding bottom of the reaction space protruding upper edge of the cast iron body is inventively provided with one or more wells on or at which the liquid slag overflows like a jet and enters the cooling zone as a compact beam.

2 0 8 15 8

- x In a preferred embodiment of the invention, the annular body consists of Einein-laid in a plurality of turns and a casted iron in steel pipe, which is provided with a supply and an outlet for cooling water. The metallic contact between

see steel pipe turns and cast iron, and the good thermal conductivity of the cast iron guarantee intensive cooling of the slag drain opening designed in this way, a dense coating of the annular body with a solidified thin slag layer and the permanent adherence to the outer contour of Schlackenabflußöffnung. The reaction space is often surrounded by a water-cooled screen from donated, coated with refractory ramming tubes.

In such a Pail an embodiment of the invention is characterized in that the supply and the discharge for the cooling water for cooling the annular body with the cooling water supply system of the cooling 'is connected tube screen for the reaction space, so that a uniform cooling system for cooling tube screen and slag drain opening consists ,

An operation of reactors for the gasification of coal dust in the flying cloud is characterized in that the crude gas generated and the slag are cooled by injecting water together and thereby the crude gas is saturated with water vapor. "The water vapor content is for subsequent gas conversion stages, in particular for the catalytic CO Conversion needed. An embodiment of the invention which complies with this mode of operation is characterized in that the cooling water discharge of the slag discharge opening is connected to the water distribution device for the direct cooling and saturation of the raw gas. In this way it is achieved that the heat content of the cooling of the slag

- 6 - "20 8 15 8

heated water inlet opening to increase the saturation temperature of the raw gas and thus can be used to improve the CO conversion,

embodiment

The invention will be explained by the following embodiment with Figures 1 and 2. 1 shows a schematic representation of a reactor for the gasification of pulverized coal as a flame reaction in the flying cloud, FIG. 2 shows an enlarged detail of the slag discharge opening,

The reactor 1 for the gasification of pulverized coal under pressure consists of the reaction space 2 and the cooling and Gr anulierteil 3 α The reaction space 2 is surrounded by a wasserbeaufschlagten cooling pipe screen 4, the reaction chamber side is coated with ramming mass 5. At the top of the reaction space 2 of the burner-.6 is arranged, which serves the supply of coal dust, oxygen and steam. The reaction space 2 is closed down through the bottom 7, which is created by appropriate design of the cooling tube screen. In the center of the bottom, the slag drain opening 8 is arranged, which is formed by the annular body 9, which in turn is held by a cooled support structure 12. During operation, such temperatures prevail in the reaction space that the ash contained in the pulverized coal becomes molten slag which, together with the crude gas formed, passes through the slag discharge opening 8 into the cooling and granulating section 3. becomes. A water distribution device 13 shown schematically as a nozzle in FIG. 1 serves for the direct cooling of raw gas μ 1 slag,

The cooling and granulating 3 is further provided with a raw gas outlet nozzle 15 and a bottom opening 16. The bottom opening 16 serves the common Ab-

-7-208158

Fülirung of granulated slag and unvaporized injection water from the reactor, which collect in the lower half of the cooling and granulation 3.

As Pigo 2 further shows, is in the slag outlet 8 forming, made of cast iron annular body 9 in several turns and the shape of the annular body 9 in accordance with a steel pipe 17 poured, which is connected to a water supply line 1o and -abführungsleitung 11. The upper edge of the annular body 9 protrudes above the level of the bottom 7 of the Reaktionsruumes 2, so that the reaching to the bottom 7 liquid slag is dammed up there to a flat slag bath 18. The upper edge of the annular body 9 is provided on one side with a recess 19. Thus, at this point, the slag can flow as a compact jet 2o through the slag discharge opening 8 together with the raw gas into the cooling and granulating part 3. The water discharge line 11 is connected to the supply line 14 to the water distribution device 13. Thus, the heat content of the effluent from the annular body 9 and heated there cooling water is used to increase the settling in the cooling and granulating 3 saturation temperature of the raw gas. At the same time it is thus - except for the pressure drop of the flowing cooling water between entry into the annular body 9 and water distribution device 13 - a pressure equalization between the pressure prevailing in the steel tube of the body 9 pressure and the pressure in the reaction chamber and cooling and Granulierteil »

Claims (4)

Brfindungsansprüch.
1. An apparatus for gasification of ash-containing fuels with a free oxygen-containing gasification agent as fflammenreaktion in the plug cloud at temperatures above the melting point of the ash, wherein the molten slag is transferred together with generated hot raw gas from a reaction space in a cooling and granulating, with a in the bottom of Reaktlonsraumes, formed by an annular, dam-like over the surrounding bottom of the reaction space protruding annular body slag drain opening (8), characterized in that the upper edge of the annular body (9) with one or more recesses (19) is provided.
2. Device according to item 1, characterized in that the slag outlet opening forming annular body (9) consists of a cast in several turns and cast in cast iron steel pipe (17), which with a water supply line (1o) and a water discharge line (11) is. ,
3. Device according to item 1 and 2, characterized in that the water supply line (1o) and the water discharge line (11) is connected to the cooling water supply of the cooling pipe screen (4) for the reaction space.
- · - · 208158
4 · Device according to items 1 and 2, characterized in that the Wasserabf uhrungsleitung (11) with a water distribution device (13) in the cooling and granulation part (3) is connected so that in the annular body
(9) heated and through the water drainage pipe
(11) draining water immediately for granulation
the slag, where appropriate, can serve for the direct cooling of the raw gas »
Hiercu ^^ pages drawings
DD20815878A 1978-09-28 1978-09-28 Device for gasification of absorbent fuels in flying cloud DD150313A3 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
DD20815878A DD150313A3 (en) 1978-09-28 1978-09-28 Device for gasification of absorbent fuels in flying cloud

Applications Claiming Priority (9)

Application Number Priority Date Filing Date Title
DD20815878A DD150313A3 (en) 1978-09-28 1978-09-28 Device for gasification of absorbent fuels in flying cloud
DE19792935752 DE2935752C2 (en) 1978-09-28 1979-09-05
CS609179A CS220582B1 (en) 1978-09-28 1979-09-07 Apparatus for gasifying ash containing fuel
AT604279A AT376694B (en) 1978-09-28 1979-09-13 Slag and gasabflussoeffnung for a reactor for gasification ash-containing fuels in flight cloud
AU51142/79A AU529627B2 (en) 1978-09-28 1979-09-25 Gasifying ash containing fuels
YU235679A YU40235B (en) 1978-09-28 1979-09-27 Device for the gasification of ash-containing fuels in a suspended cloud
GB7933488A GB2033563B (en) 1978-09-28 1979-09-27 Removing slag from a gasifier
HUBE001373 HU181855B (en) 1978-09-28 1979-09-27 Removing slag from a gasifier
FR7924329A FR2437436B1 (en) 1978-09-28 1979-09-28 Device for the gasification of suspended fuel at high ash content

Publications (1)

Publication Number Publication Date
DD150313A3 true DD150313A3 (en) 1981-08-26

Family

ID=5514630

Family Applications (1)

Application Number Title Priority Date Filing Date
DD20815878A DD150313A3 (en) 1978-09-28 1978-09-28 Device for gasification of absorbent fuels in flying cloud

Country Status (9)

Country Link
AT (1) AT376694B (en)
AU (1) AU529627B2 (en)
CS (1) CS220582B1 (en)
DD (1) DD150313A3 (en)
DE (1) DE2935752C2 (en)
FR (1) FR2437436B1 (en)
GB (1) GB2033563B (en)
HU (1) HU181855B (en)
YU (1) YU40235B (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3120238A1 (en) * 1981-05-21 1982-12-09 Babcock Anlagen Ag Reactor for flight stream gasification
DE3540304A1 (en) * 1984-11-15 1986-05-15 Shell Int Research Reactor and process for the manufacture of synthesis gas
DE19714376C1 (en) * 1997-04-08 1999-01-21 Gutehoffnungshuette Man Synthesis gas generator with combustion and quench

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CH661054A5 (en) * 1981-10-23 1987-06-30 Sulzer Ag Gaskuehler to synthesis gas generator.
US4605423A (en) * 1982-04-12 1986-08-12 Texaco Development Corporation Apparatus for generating and cooling synthesis gas
DE3220624A1 (en) * 1982-05-03 1983-11-10 Kloeckner Humboldt Deutz Ag Device for continuous granulation of slags by means of coolant fluid
US5851497A (en) * 1994-11-18 1998-12-22 Texaco Inc. Gasifier throat
US5464592A (en) * 1993-11-22 1995-11-07 Texaco Inc. Gasifier throat
US8888872B2 (en) 2010-07-06 2014-11-18 General Electric Company Gasifier cooling system

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE765992C (en) * 1941-03-01 1953-01-26 Koppers Gmbh Heinrich A process for the production of fuel gas from heizkraeftigem fuels staubfoermigen
FR1117216A (en) * 1953-12-07 1956-05-18 Babcock & Wilcox France Method and apparatus for the continuous production of synthesis gas from a carbonaceous fuel entrained by steam
US2931715A (en) * 1956-10-24 1960-04-05 Texaco Inc Apparatus for the gasification of solid fuels
GB1525191A (en) * 1976-05-28 1978-09-20 British Gas Corp Coal gasification plant
GB2029946B (en) * 1978-09-08 1982-12-01 British Gas Corp Slag removal from coal gasification plant

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3120238A1 (en) * 1981-05-21 1982-12-09 Babcock Anlagen Ag Reactor for flight stream gasification
DE3540304A1 (en) * 1984-11-15 1986-05-15 Shell Int Research Reactor and process for the manufacture of synthesis gas
DE19714376C1 (en) * 1997-04-08 1999-01-21 Gutehoffnungshuette Man Synthesis gas generator with combustion and quench

Also Published As

Publication number Publication date
GB2033563B (en) 1983-03-30
DE2935752C2 (en) 1985-10-31
DE2935752A1 (en) 1980-06-04
AU529627B2 (en) 1983-06-16
ATA604279A (en) 1984-05-15
GB2033563A (en) 1980-05-21
HU181855B (en) 1983-11-28
YU235679A (en) 1983-01-21
FR2437436B1 (en) 1986-03-21
FR2437436A1 (en) 1980-04-25
YU40235B (en) 1985-08-31
AU5114279A (en) 1980-04-03
AT376694B (en) 1984-12-27
CS220582B1 (en) 1983-04-29

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