EP0616022A1 - Procédé pour la gazéification sous pression de combustibles finement divisés - Google Patents
Procédé pour la gazéification sous pression de combustibles finement divisés Download PDFInfo
- Publication number
- EP0616022A1 EP0616022A1 EP93104291A EP93104291A EP0616022A1 EP 0616022 A1 EP0616022 A1 EP 0616022A1 EP 93104291 A EP93104291 A EP 93104291A EP 93104291 A EP93104291 A EP 93104291A EP 0616022 A1 EP0616022 A1 EP 0616022A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- raw gas
- quench
- gas
- convection
- boiler
- Prior art date
- Legal status (The legal status 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 status listed.)
- Granted
Links
- 238000002309 gasification Methods 0.000 title claims abstract description 54
- 238000000034 method Methods 0.000 title claims abstract description 26
- 239000000446 fuel Substances 0.000 title claims abstract description 10
- 238000010791 quenching Methods 0.000 claims abstract description 81
- 239000002893 slag Substances 0.000 claims abstract description 19
- 238000000605 extraction Methods 0.000 claims abstract description 14
- 239000002245 particle Substances 0.000 claims abstract description 14
- 238000010438 heat treatment Methods 0.000 claims description 15
- 238000009827 uniform distribution Methods 0.000 claims description 4
- 239000010419 fine particle Substances 0.000 claims description 2
- 230000000171 quenching effect Effects 0.000 abstract description 5
- 239000007789 gas Substances 0.000 description 80
- 238000001816 cooling Methods 0.000 description 5
- 238000009835 boiling Methods 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000000265 homogenisation Methods 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 230000000295 complement effect Effects 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 238000005242 forging Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000010079 rubber tapping Methods 0.000 description 1
- 238000001228 spectrum Methods 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/72—Other features
- C10J3/82—Gas withdrawal means
- C10J3/84—Gas withdrawal means with means for removing dust or tar from the gas
- C10J3/845—Quench rings
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/46—Gasification of granular or pulverulent flues in suspension
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/72—Other features
- C10J3/78—High-pressure apparatus
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/72—Other features
- C10J3/82—Gas withdrawal means
- C10J3/84—Gas withdrawal means with means for removing dust or tar from the gas
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/72—Other features
- C10J3/86—Other features combined with waste-heat boilers
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
- C10K1/00—Purifying combustible gases containing carbon monoxide
- C10K1/04—Purifying combustible gases containing carbon monoxide by cooling to condense non-gaseous materials
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2300/00—Details of gasification processes
- C10J2300/12—Heating the gasifier
- C10J2300/1246—Heating the gasifier by external or indirect heating
Definitions
- the invention relates to a method for the pressure gasification of finely divided fuels in the course of the production of process gas.
- a gasification reactor, a boiler, in particular a convection boiler, and a quenching device are used.
- Fine-particle fuels mean fine-grained to dust-like fuels. In particular, it may be coal.
- the energy is fed to the gasification reactor via burners, which usually also carry the finely divided fuel.
- the gasification reaction is controlled or regulated as required for the production of a service gas of a predetermined composition. Quenching or quenching the raw gas freezes disturbing reactions.
- a quench gas is supplied for this purpose.
- the term gas here also means vapors.
- the prevailing teaching is also used within the scope of the invention.
- the walls of the gasification reactor and the convection boiler and other components for the purpose of hot cooling e.g. B. in the form of boiling water cooling, tube walls made of different parallel tubes or provided with such tube walls.
- the convection boiler is equipped with convection heating surfaces. It goes without saying that the heat absorbed via the tube walls and in the convection boiler is used.
- the invention has for its object to provide a method for pressure gasification, which is characterized by simple procedure and high operational reliability and can be implemented in a simple and compact gasification apparatus.
- the advantages and effects described are particularly pronounced if the deflected raw gas stream is guided past concentric convection heating surfaces in the convection boiler and to a temperature of 400 ° to 200 ° C. upon entry into the raw gas extraction device is cooled.
- the supply of the quench gas can also have an effect on the thermodynamics in the process according to the invention for homogenization and homogenization and thus for suppressing streak formation and disadvantageous influences, namely in that the quench gas is distributed in a uniform distribution between the gasification reactor and the quench tube with the aid of a rotating quench gas supply gap the entire circumference and in cross flow to the raw gas is introduced into the quench tube.
- the quench gas is preferably introduced into the quench tube via a built-in quench gas supply gap.
- the concentric convection heating surfaces surround the quench tube.
- the convection heating surfaces there is therefore an annular space with an annular disk-shaped plan, in which a large convection heating surface can be accommodated without difficulty.
- tower-like boilers with concentric convection heating surfaces have a thermodynamically ineffective area in the center, in the method according to the invention this area is used to hold the quench tube.
- the systems or apparatuses that result from the teaching of the method according to the invention when introduced into practice are surprisingly compact with high performance and high throughput.
- the heat transfer and thus the cooling of the raw gas take place very intensively according to the invention, because both the wall of the quench tube and the convection heating surfaces are flowed around and acted upon on both sides by the gas to be cooled.
- the invention teaches that a swirl flow is impressed on the raw gas stream as it exits the convection boiler in the flue gas extraction device and the flow rate and swirl in the raw gas extraction device are set up in such a way that entrained slag and ash particles are discharged.
- the gasification apparatus shown in the figures is intended for the pressure gasification of finely divided fuels in the course of the production of process gas and is set up in such a way that it results from the method according to the invention.
- a middle part has not been shown, the length of which corresponds approximately to the length of the lower part.
- the basic structure of the gasification apparatus includes a gasification reactor 1, a quench tube 2 for the raw gas emerging from the gasification reactor 1 and a convection boiler 3 with convection heating surfaces 4 for receiving the waste heat of the raw gas.
- the convection heating surfaces 4 are expediently arranged in the form of concentric cylinders.
- the apparatuses described are constructed from tube walls, which in turn consist of tubes which are guided in parallel and welded to one another.
- the gasification reactor 1, the quench tube 2 and the convection boiler 3 are arranged with a boiler housing 5 in a pressure vessel 6.
- the convection boiler 3 surrounds the quench tube 2 concentrically.
- the gasification reactor 1 is arranged coaxially under the quench tube 2.
- the boiler housing 5 also suitably consists of tube walls.
- a deflection device 7 is arranged or formed in the boiler housing 5 for the raw gas emerging from the quench tube 2 and to be introduced into the convection boiler 3.
- a raw gas outlet device 8 is arranged in a region between the gasification reactor 1 and convection boiler 3, with which the raw gas from the boiler housing 5 and the pressure vessel 6 is carried out.
- a swirl-producing deflection of the raw gas emerging from the convection boiler takes place with the aid of guide vanes 8a indicated in FIG. 3.
- the design is such that the escaping raw gas entrains slag and ash particles so that there are no disturbing deposits in this area. The cooling of the raw gas and thus the Schiackeparticle was carried out so far that baking is not possible.
- the gasification reactor 1 is fixed in the lower part of the pressure vessel 6 in this.
- the fixed points 9 indicate this.
- the convection heating surfaces 4 are carried by the quench tube 2 and the Kesseie housing 5.
- the quench tube 2 and the boiler housing 5 are placed in their lower area, above the raw gas outlet device 8, on load discharge elements 10, which have raw gas passages 11 and are fixed to the pressure vessel 6 are. In this regard, reference is made in particular to FIGS. 3, 5 and 6 with the fixed points 12.
- a circumferential quench gas introduction gap 13 is arranged between the gasification reactor 1 and the quench tube 2. This separates the quench tube 2 and the gasification reactor 1.
- the arrangement is such that between the quench tube area below the load transfer elements 10, on the one hand, and the gasification reactor 1 above its fixed point bearing 9, on the other hand, different, also pressure-vessel-related, thermal expansions are permitted.
- the quench gas introduction gap 13 is additionally dimensioned as a thermal expansion compensation gap.
- the pressure vessel 6 is at the same time set up as a supporting structure for the gasification reactor 1, the quench tube 2 and the convection boiler 3 with boiler housing 5 and statically and in terms of stability.
- the already mentioned deflection device 7 is designed in the exemplary embodiment as a hood-shaped impact deflection device.
- the raw gas outlet device 8 has a device 14 for the discharge of slag and / or ash particles, which is described in detail below.
- the convection heating surfaces 4 are fastened on one side to supporting cross members 16.
- the cross members 16 are connected to the boiler housing 5 and the quench tube 2 without tension in order to avoid constraints from different thermal expansion of the boiler housing or the quench tube.
- the traverses 16 are statically supported as beams on two supports.
- the details of the load transfer elements 10 can be seen in particular from FIGS. 5 and 6. These are designed as rigid, metallic components with an inner ring 17, outer ring 18 and spokes 19. The intermediate spaces form the raw gas passages 11. The components 17, 18, 19 described are made in one piece, for. B. as forgings.
- the load transfer elements 10 are connected to the load-bearing elements in the pressure vessel 6 via heated supports or a heated frame 20 on the boiler housing 5. It was indicated in FIG. 5 that the load transfer elements 10 are at the same time designed as a feed device for the boiling water of a boiling water cooling of the quench tube-forming pipelines of the tube wall of the quench tube 2. For this purpose, reference is made to the pipes or channels 21.
- the boiling water is discharged via heat expansion deformable discharge pipes 22 connected to the top of the quench pipe 2 or its pipes.
- heat expansion deformable discharge pipes 22 connected to the top of the quench pipe 2 or its pipes.
- all pipe connections between the quench pipe 2 and the boiler housing 5 are designed and arranged to be elastically deformable .
- the gasification reactor 1 forms an annular space 23 opposite the wall of the pressure vessel 6.
- the quench gases to be supplied become via this annular space 23 to the quench gas introduction gap 13.
- the annular space 23 is also connected to a pressure compensation space 24 which has remained free between the boiler housing 5 and the pressure vessel 6.
- the quench gas introduction gap 13 is particularly advantageous in the exemplary embodiment. It is formed between a conically drawn-in output component 25 of the gasification reactor 1 and a skirt 26 of the quench tube 2 which is complementary thereto.
- the output component 25 is designed on the gasification reactor chamber side free of a refractory lining with a metallic blank.
- the cone angle is approximately 60 °. All surfaces located downstream of the output component 25 are also free of a refractory lining.
- the output member 25 of the gasification reactor 1 is provided with a cleaning ring 27 and this periodically, for. B. is movable by means of tapping.
- the annular space between the peripheral wall of the gasification reactor 1 and the pressure vessel 6 is closed by a membrane 28.
- the pressure compensation in the area below the membrane is established via the slag discharge opening in the bottom of the gasification reactor 1.
- a gasification reactor 1 In the pressure vessel 6, which is designed for the pressure of the pressure gasification, a gasification reactor 1, a quench tube 2 and a convection boiler 3 are arranged concentrically.
- the raw gas emerging axially upward from the gasification reactor 1 is introduced into the quench tube 2 connected upward.
- a quench gas is supplied.
- the mixed gas stream of raw gas and quench gas which is referred to again below as raw gas, is deflected above the quench tube 2 by means of a deflection device 7 which is rotationally symmetrical with respect to the axis of the quench tube 2 in the form of a deflecting screen and is converted into a hollow cylindrical raw gas stream.
- the hollow-cylindrical raw gas flow is introduced into the hollow-cylindrical convection boiler 3, which concentrically surrounds the quench tube 2.
- the raw gas stream is withdrawn from the convection boiler 3 when it leaves the convection boiler 3 with the aid of a raw gas outlet device 8.
- the flow rate of the raw gas is first set up in such a way that slag and ash parts entrained by the raw gas are carried via the 180 ° deflection into the hollow cylindrical convection boiler 3, in which they cool down until they lose their adhesiveness.
- the flow in the raw gas outlet device 8 is set up so that the entrained slag and ash parts are discharged.
- the exemplary embodiment shows that the deflected raw gas stream is guided past concentric convection heating surfaces 4 in the convection boiler 3 and is cooled to a temperature of 400 to 200 ° C. upon entry into the raw gas outlet device 8.
- the quench gas is in a circulating quench gas introduction gap 13 between the gasification reactor 1 and the quench tube 2 in uniform distribution over the entire circumference and introduced into the quench tube 2 in cross flow to the raw gas.
- a swirl flow is impressed on the raw gas flow when it leaves the convection boiler 3 in the raw gas outlet device 8.
- the flow rate and the swirl in the raw gas outlet device 8 are set up so that entrained slag and ash particles are discharged.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Gasification And Melting Of Waste (AREA)
- Processing Of Solid Wastes (AREA)
- Industrial Gases (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
Priority Applications (10)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
ES93104291T ES2078078T3 (es) | 1993-03-16 | 1993-03-16 | Procedimiento para la gasificacion bajo presion de combustibles finamente divididos. |
DK93104291.5T DK0616022T3 (da) | 1993-03-16 | 1993-03-16 | Fremgangsmåde til trykforgasning af partikelformige brændstoffer |
DE59300598T DE59300598D1 (de) | 1993-03-16 | 1993-03-16 | Verfahren für die Druckvergasung von feinteiligen Brennstoffen. |
EP93104291A EP0616022B1 (fr) | 1993-03-16 | 1993-03-16 | Procédé pour la gazéification sous pression de combustibles finement divisés |
ZA939354A ZA939354B (en) | 1993-03-16 | 1993-12-14 | Process for elevated-pressure gasification of finely particulate fuels |
US08/201,364 US5441547A (en) | 1993-03-16 | 1994-02-24 | Method for gasification of a finely divided combustible material |
CN94102284A CN1041107C (zh) | 1993-03-16 | 1994-03-10 | 对细小燃料高压制取的煤气进行冷却的方法 |
PL94302608A PL173329B1 (pl) | 1993-03-16 | 1994-03-14 | Sposób zgazowywania ciśnieniowego drobnocząstkowych paliw |
RU94008855A RU2122565C1 (ru) | 1993-03-16 | 1994-03-15 | Способ газификации под давлением высокодисперсных горючих |
GR950403163T GR3018065T3 (en) | 1993-03-16 | 1995-11-10 | Process for pressure gasification of fine particulate fuels. |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP93104291A EP0616022B1 (fr) | 1993-03-16 | 1993-03-16 | Procédé pour la gazéification sous pression de combustibles finement divisés |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0616022A1 true EP0616022A1 (fr) | 1994-09-21 |
EP0616022B1 EP0616022B1 (fr) | 1995-09-13 |
Family
ID=8212704
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP93104291A Expired - Lifetime EP0616022B1 (fr) | 1993-03-16 | 1993-03-16 | Procédé pour la gazéification sous pression de combustibles finement divisés |
Country Status (10)
Country | Link |
---|---|
US (1) | US5441547A (fr) |
EP (1) | EP0616022B1 (fr) |
CN (1) | CN1041107C (fr) |
DE (1) | DE59300598D1 (fr) |
DK (1) | DK0616022T3 (fr) |
ES (1) | ES2078078T3 (fr) |
GR (1) | GR3018065T3 (fr) |
PL (1) | PL173329B1 (fr) |
RU (1) | RU2122565C1 (fr) |
ZA (1) | ZA939354B (fr) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8562698B2 (en) | 2008-03-27 | 2013-10-22 | Thyssenkrupp Uhde Gmbh | Device for production of synthesis gas with a gasification reactor with a subsequent quenching space |
RU2534081C2 (ru) * | 2009-07-27 | 2014-11-27 | Тиссенкрупп Уде Гмбх | Реактор газификации |
DE102008057410B4 (de) | 2008-11-14 | 2019-07-04 | Thyssenkrupp Industrial Solutions Ag | Vorrichtung zur Herstelllung von Synthesegas mit einem Vergasungsreaktor mit anschließendem Quenchraum |
Families Citing this family (13)
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 (de) | 2007-06-12 | 2008-12-18 | Uhde Gmbh | Herstellung und Kühlung von gasförmigen Kohlevergasungsprodukten |
DE102007044726A1 (de) | 2007-09-18 | 2009-03-19 | Uhde Gmbh | Vergasungsreaktor und Verfahren zur Flugstromvergasung |
CN101842467B (zh) | 2007-09-18 | 2013-09-25 | 犹德有限公司 | 气化反应器和用于气流床气化的方法 |
DE102008012734A1 (de) | 2008-03-05 | 2009-09-10 | Uhde Gmbh | Vergasungsreaktor und Verfahren zur Flugstromvergasung |
DE102008012732A1 (de) | 2008-03-05 | 2009-09-10 | Uhde Gmbh | Vergasungsvorrichtung mit Schlackeabzug |
DE102009005464A1 (de) | 2009-01-21 | 2010-08-05 | Uhde Gmbh | Vorrichtung zur Herstellung von Synthesegas mit einem Vergasungreaktor mit anschließendem Quenchraum |
DE102008015801B4 (de) | 2008-03-27 | 2019-02-28 | Thyssenkrupp Industrial Solutions Ag | Vorrichtung zur Herstellung von Synthesegas mit einem Vergasungsreaktor mit anschließendem Quenchraum |
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 |
DE102011107726B4 (de) | 2011-07-14 | 2016-06-30 | Thyssenkrupp Industrial Solutions Ag | Vorrichtung und Verfahren zum Einleiten von nachwachsenden Brennstoffen in den Bereich der Strahlungskesselwand von Vergasungsreaktoren |
DE102011110213A1 (de) | 2011-08-16 | 2013-02-21 | Thyssenkrupp Uhde Gmbh | Verfahren und Vorrichtung zur Rückführung von Abgas aus einer Gasturbine mit nachfolgendem Abhitzekessel |
JP5518161B2 (ja) * | 2012-10-16 | 2014-06-11 | 三菱重工業株式会社 | ガス化装置 |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR1070615A (fr) * | 1951-12-12 | 1954-08-03 | Babcock & Wilcox France | Générateur de vapeur combiné à un appareil de production de gaz de synthèse |
DE1596323A1 (de) * | 1967-06-06 | 1970-04-02 | Walther & Cie Ag | Synthesegaserzeuger mit Gaskuehler,die in einem Druckzylinder angeordnet sind |
FR2500470A1 (fr) * | 1981-02-26 | 1982-08-27 | Steinmueller Gmbh L & C | Installation pour obtenir des produits sous forme gazeuse |
EP0099833A1 (fr) * | 1982-07-21 | 1984-02-01 | Creusot-Loire | Dispositif de conversion et de récupération d'énergie thermique |
EP0115094A2 (fr) | 1982-12-29 | 1984-08-08 | Shell Internationale Researchmaatschappij B.V. | Procédé et appareil pour la production de gaz de synthèse |
DE3809313A1 (de) * | 1988-03-19 | 1989-10-05 | Krupp Koppers Gmbh | Verfahren und vorrichtung zum kuehlen von partialoxidationsgas |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
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CH656637A5 (de) * | 1981-10-26 | 1986-07-15 | Sulzer Ag | Gaskuehler-anordnung zu kohlevergasungsanlage. |
GB2164951A (en) * | 1984-09-26 | 1986-04-03 | Shell Int Research | Method and apparatus for producing synthesis gas |
DE3711314A1 (de) * | 1987-04-03 | 1988-10-13 | Babcock Werke Ag | Vorrichtung zum kuehlen eines synthesegases in einem quenchkuehler |
DE3816340A1 (de) * | 1988-05-13 | 1989-11-23 | Krupp Koppers Gmbh | Verfahren und vorrichtung zum kuehlen eines heissen produktgases, das klebrige bzw. schmelzfluessige partikel enthaelt |
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 (de) * | 1988-07-16 | 1990-01-18 | Krupp Koppers Gmbh | Anlage fuer die erzeugung eines produktgases aus einem feinteiligen kohlenstofftraeger |
DD280975B3 (de) * | 1989-03-31 | 1993-03-04 | Noell Dbi Energie Entsorgung | Verfahren und vorrichtung zur kuehlung und reinigung von mit schlacke bzw.staub beladenen druckvergasungsgasen |
JP2659849B2 (ja) * | 1990-05-30 | 1997-09-30 | 三菱重工業株式会社 | 加圧型ガス化装置 |
-
1993
- 1993-03-16 ES ES93104291T patent/ES2078078T3/es not_active Expired - Lifetime
- 1993-03-16 EP EP93104291A patent/EP0616022B1/fr not_active Expired - Lifetime
- 1993-03-16 DK DK93104291.5T patent/DK0616022T3/da active
- 1993-03-16 DE DE59300598T patent/DE59300598D1/de not_active Expired - Fee Related
- 1993-12-14 ZA ZA939354A patent/ZA939354B/xx unknown
-
1994
- 1994-02-24 US US08/201,364 patent/US5441547A/en not_active Expired - Fee Related
- 1994-03-10 CN CN94102284A patent/CN1041107C/zh not_active Expired - Fee Related
- 1994-03-14 PL PL94302608A patent/PL173329B1/pl unknown
- 1994-03-15 RU RU94008855A patent/RU2122565C1/ru active
-
1995
- 1995-11-10 GR GR950403163T patent/GR3018065T3/el unknown
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR1070615A (fr) * | 1951-12-12 | 1954-08-03 | Babcock & Wilcox France | Générateur de vapeur combiné à un appareil de production de gaz de synthèse |
DE1596323A1 (de) * | 1967-06-06 | 1970-04-02 | Walther & Cie Ag | Synthesegaserzeuger mit Gaskuehler,die in einem Druckzylinder angeordnet sind |
FR2500470A1 (fr) * | 1981-02-26 | 1982-08-27 | Steinmueller Gmbh L & C | Installation pour obtenir des produits sous forme gazeuse |
EP0099833A1 (fr) * | 1982-07-21 | 1984-02-01 | Creusot-Loire | Dispositif de conversion et de récupération d'énergie thermique |
EP0115094A2 (fr) | 1982-12-29 | 1984-08-08 | Shell Internationale Researchmaatschappij B.V. | Procédé et appareil pour la production de gaz de synthèse |
DE3809313A1 (de) * | 1988-03-19 | 1989-10-05 | Krupp Koppers Gmbh | Verfahren und vorrichtung zum kuehlen von partialoxidationsgas |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8562698B2 (en) | 2008-03-27 | 2013-10-22 | Thyssenkrupp Uhde Gmbh | Device for production of synthesis gas with a gasification reactor with a subsequent quenching space |
DE102008057410B4 (de) | 2008-11-14 | 2019-07-04 | Thyssenkrupp Industrial Solutions Ag | Vorrichtung zur Herstelllung von Synthesegas mit einem Vergasungsreaktor mit anschließendem Quenchraum |
RU2534081C2 (ru) * | 2009-07-27 | 2014-11-27 | Тиссенкрупп Уде Гмбх | Реактор газификации |
US9200222B2 (en) | 2009-07-27 | 2015-12-01 | Thyssenkrupp Uhde Gmbh | Gasification reactor having direct or indirect support at coolant inlet lines or mixture outlet lines |
Also Published As
Publication number | Publication date |
---|---|
US5441547A (en) | 1995-08-15 |
ZA939354B (en) | 1994-06-21 |
GR3018065T3 (en) | 1996-02-29 |
CN1041107C (zh) | 1998-12-09 |
DK0616022T3 (da) | 1996-01-15 |
RU2122565C1 (ru) | 1998-11-27 |
PL173329B1 (pl) | 1998-02-27 |
DE59300598D1 (de) | 1995-10-19 |
ES2078078T3 (es) | 1995-12-01 |
CN1093738A (zh) | 1994-10-19 |
EP0616022B1 (fr) | 1995-09-13 |
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