ES2064455T3 - Procedimiento de gasificacion de carbon en dos etapas. - Google Patents
Procedimiento de gasificacion de carbon en dos etapas.Info
- Publication number
- ES2064455T3 ES2064455T3 ES89310629T ES89310629T ES2064455T3 ES 2064455 T3 ES2064455 T3 ES 2064455T3 ES 89310629 T ES89310629 T ES 89310629T ES 89310629 T ES89310629 T ES 89310629T ES 2064455 T3 ES2064455 T3 ES 2064455T3
- Authority
- ES
- Spain
- Prior art keywords
- reactor
- water
- carbon
- increase
- gas
- 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.)
- Expired - Lifetime
Links
- 239000003245 coal Substances 0.000 title abstract 4
- 238000002309 gasification Methods 0.000 title abstract 2
- 238000000034 method Methods 0.000 title abstract 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract 4
- 229910052799 carbon Inorganic materials 0.000 abstract 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract 2
- 230000015572 biosynthetic process Effects 0.000 abstract 2
- 238000002485 combustion reaction Methods 0.000 abstract 2
- 229910052760 oxygen Inorganic materials 0.000 abstract 2
- 239000001301 oxygen Substances 0.000 abstract 2
- 238000011084 recovery Methods 0.000 abstract 2
- 239000007787 solid Substances 0.000 abstract 2
- 238000004326 stimulated echo acquisition mode for imaging Methods 0.000 abstract 2
- 238000003786 synthesis reaction Methods 0.000 abstract 2
- WYTGDNHDOZPMIW-RCBQFDQVSA-N alstonine Natural products C1=CC2=C3C=CC=CC3=NC2=C2N1C[C@H]1[C@H](C)OC=C(C(=O)OC)[C@H]1C2 WYTGDNHDOZPMIW-RCBQFDQVSA-N 0.000 abstract 1
- 239000000446 fuel Substances 0.000 abstract 1
- 239000007789 gas Substances 0.000 abstract 1
- QEVHRUUCFGRFIF-MDEJGZGSSA-N reserpine Chemical compound O([C@H]1[C@@H]([C@H]([C@H]2C[C@@H]3C4=C(C5=CC=C(OC)C=C5N4)CCN3C[C@H]2C1)C(=O)OC)OC)C(=O)C1=CC(OC)=C(OC)C(OC)=C1 QEVHRUUCFGRFIF-MDEJGZGSSA-N 0.000 abstract 1
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
- C10J3/721—Multistage gasification, e.g. plural parallel or serial gasification stages
-
- 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
- C10J3/48—Apparatus; Plants
- C10J3/485—Entrained flow gasifiers
-
- 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
- C10J2200/00—Details of gasification apparatus
- C10J2200/15—Details of feeding means
- C10J2200/152—Nozzles or lances for introducing gas, liquids or suspensions
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
- Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S48/00—Gas: heating and illuminating
- Y10S48/07—Slurry
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Industrial Gases (AREA)
- Processing Of Solid Wastes (AREA)
- Air Supply (AREA)
Abstract
UN PROCESO DE FLUJO SUPERIOR DE DOS ETAPAS PARA GASIFICACION DE CARBON Y UN APARATO USADO PARA ELLO. UN GAS QUE CONTIENE OXIGENO Y UN PRIMER INCREMENTO DE UN LIMO DE CARBON EN AGUA SE QUEMAN EN UN REACTOR DE QUEMADO CON FUEGO HORIZONTAL POR MEDIO DE BOQUILLAS DE HORNO HORIZONTALES COAXIALES YUXTAPUESTAS MONTADAS EN EL REACTOR, CON LO QUE SE CONVIERTE EL OXIGENO, EL CARBON, Y EL AGUA EN VAPOR Y PRODUCTOS GASEOSOS DE COMBUSTION. LA DESCARGA DEL REACTOR DE QUEMADO SE PONE EN CONTACTO EN LA PARTE SUPERIOR CON UN SEGUNDO INCREMENTO DE LIMO DE CARBON Y AGUA EN UNA UNIDAD VERTICAL NO FOGUEADA DE RECUPERACION DE CALOR CONECTADA AL EXTREMO SUPERIOR DEL REACTOR. EL CALOR GENERADO EN EL REACTOR SE USA EN LA UNIDAD DE RECUPERACION DE CALOR PARA CONVERTIR EL SEGUNDO INCREMENTO DE LIMO DE CARBON Y AGUA EN MAS VAPOR, CARBON Y GAS DE SINTESIS. EL GAS EFLUENTE SE SEPARA DEL CARBON SOLIDO, Y EL GAS DE SINTESIS SE PASA DENTRO DE UNA CALDERA SERPENTIN PARA RECUPERAR CALOR Y EL PRODUCTO GASEOSO ENFRIADO SE RECUPERA COMO PRODUCTO DESEADO RICO EN COMBUSTIBLE. EL CARBON SOLIDO SE VUELVE A CONVERTIR EN LIMO Y SE RECICLA AL REACTOR DE QUEMADO (3) PARA COMBUSTION ADICIONAL.FIG 1.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US80303185A | 1985-11-29 | 1985-11-29 | |
| US07/178,035 US4872886A (en) | 1985-11-29 | 1988-04-05 | Two-stage coal gasification process |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| ES2064455T3 true ES2064455T3 (es) | 1995-02-01 |
Family
ID=26873886
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| ES89310629T Expired - Lifetime ES2064455T3 (es) | 1985-11-29 | 1989-10-17 | Procedimiento de gasificacion de carbon en dos etapas. |
Country Status (8)
| Country | Link |
|---|---|
| US (1) | US4872886A (es) |
| EP (1) | EP0423401B1 (es) |
| KR (1) | KR0140194B1 (es) |
| CA (1) | CA2000446A1 (es) |
| DE (1) | DE68919851T2 (es) |
| ES (1) | ES2064455T3 (es) |
| GR (1) | GR3015038T3 (es) |
| WO (1) | WO1991005835A1 (es) |
Families Citing this family (86)
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| SE470213B (sv) * | 1992-03-30 | 1993-12-06 | Nonox Eng Ab | Sätt och anordning för framställning av bränslen ur fasta kolhaltiga naturbränslen |
| US5327726A (en) * | 1992-05-22 | 1994-07-12 | Foster Wheeler Energy Corporation | Staged furnaces for firing coal pyrolysis gas and char |
| US5243922A (en) * | 1992-07-31 | 1993-09-14 | Institute Of Gas Technology | Advanced staged combustion system for power generation from coal |
| USH1325H (en) | 1992-10-13 | 1994-07-05 | Shell Oil Company | One stage coal gasification process |
| US5370715A (en) * | 1993-04-27 | 1994-12-06 | Kortzeborn; Robert N. | Waste destructor and method of converting wastes to fluid fuel |
| US5431703A (en) * | 1993-05-13 | 1995-07-11 | Shell Oil Company | Method of quenching synthesis gas |
| US5433760A (en) * | 1993-05-13 | 1995-07-18 | Shell Oil Company | Method of quenching synthesis gas |
| US6027540A (en) * | 1997-03-31 | 2000-02-22 | Destec Energy, Inc. | Apparatus for removal of particulate matter from gas streams |
| PL189837B1 (pl) * | 1997-06-06 | 2005-09-30 | Ge Energy Usa | Sposób regulacji przepływu tlenu w procesie gazyfikacji i układ do regulacji przepływu tlenu w procesie gazyfikacji |
| CN1118544C (zh) * | 2000-01-13 | 2003-08-20 | 华东理工大学 | 煤基两段组合式气化工艺及其装置 |
| US7070758B2 (en) | 2000-07-05 | 2006-07-04 | Peterson Oren V | Process and apparatus for generating hydrogen from oil shale |
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| US20060101715A1 (en) * | 2004-11-17 | 2006-05-18 | Karel Vlok | Apparatus and method for coal gasification |
| US20060165582A1 (en) * | 2005-01-27 | 2006-07-27 | Brooker Donald D | Production of synthesis gas |
| DE102005041931B4 (de) * | 2005-09-03 | 2018-07-05 | Siemens Aktiengesellschaft | Vorrichtung zur Erzeugung von Synthesegasen durch Partialoxidation von aschehaltigen Brennstoffen unter erhöhtem Druck mit Teilquenchung des Rohgases und Abhitzegewinnung |
| EP1978074A1 (en) * | 2007-04-06 | 2008-10-08 | Waterim Ltd | Apparatus for the purification of a synthesis gas flow obtained from the gasification of refuses and/or biomasses |
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| US3979188A (en) * | 1974-10-25 | 1976-09-07 | Foster Wheeler Energy Corporation | Partial oxidation carbon removal process |
| US3945809A (en) * | 1975-07-08 | 1976-03-23 | The United States Of America As Represented By The United States Energy Research And Development Administration | Method and apparatus for removing coarse unentrained char particles from the second stage of a two-stage coal gasifier |
| US3957460A (en) * | 1975-09-09 | 1976-05-18 | The United States Of America As Represented By The United States Energy Research And Development Administration | Oxidation of coal-water slurry feed to hydrogasifier |
| US4069024A (en) * | 1977-05-09 | 1978-01-17 | Combustion Engineering, Inc. | Two-stage gasification system |
| US4168956A (en) * | 1977-08-18 | 1979-09-25 | Combustion Engineering, Inc. | Method of operating a coal gasifier |
| DE2822862C2 (de) * | 1978-05-26 | 1984-01-05 | Ruhrchemie Ag, 4200 Oberhausen | Verfahren zur Gewinnung wasserstoff- und kohlenmonoxidhaltiger Gasgemische durch Vergasung kohlenstoffhaltiger, aschebildender Brennstoffe |
| US4278446A (en) * | 1979-05-31 | 1981-07-14 | Avco Everett Research Laboratory, Inc. | Very-high-velocity entrained-bed gasification of coal |
| US4278445A (en) * | 1979-05-31 | 1981-07-14 | Avco Everett Research Laboratory, Inc. | Subsonic-velocity entrained-bed gasification of coal |
| US4247302A (en) * | 1979-07-13 | 1981-01-27 | Texaco Inc. | Process for gasification and production of by-product superheated steam |
| US4244706A (en) * | 1979-09-10 | 1981-01-13 | The United States Of America As Represented By The United States Department Of Energy | Process for gasifying carbonaceous material from a recycled condensate slurry |
| EP0050863A1 (en) * | 1980-10-24 | 1982-05-05 | Hitachi, Ltd. | Process of and apparatus for gasifying coals |
| US4343627A (en) * | 1980-11-28 | 1982-08-10 | Combustion Engineering, Inc. | Method of operating a two-stage coal gasifier |
| US4319888A (en) * | 1980-12-12 | 1982-03-16 | Combustion Engineering, Inc. | Apparatus for mixing char-ash into coal stream |
| US4312639A (en) * | 1980-12-22 | 1982-01-26 | Atlantic Richfield Company | Process for heating solids for coal gasification |
| GB2106130B (en) * | 1981-09-04 | 1985-11-27 | Foster Wheeler Power Prod | Gasification |
| US4525175A (en) * | 1983-05-31 | 1985-06-25 | Texaco Inc. | High turn down burner for partial oxidation of slurries of solid fuel |
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| IN168599B (es) * | 1985-11-29 | 1991-05-04 | Dow Chemical Co | |
| US4705535A (en) * | 1986-03-13 | 1987-11-10 | The Dow Chemical Company | Nozzle for achieving constant mixing energy |
-
1988
- 1988-04-05 US US07/178,035 patent/US4872886A/en not_active Expired - Lifetime
-
1989
- 1989-10-10 WO PCT/US1989/004536 patent/WO1991005835A1/en not_active Ceased
- 1989-10-11 CA CA002000446A patent/CA2000446A1/en not_active Abandoned
- 1989-10-17 ES ES89310629T patent/ES2064455T3/es not_active Expired - Lifetime
- 1989-10-17 EP EP89310629A patent/EP0423401B1/en not_active Expired - Lifetime
- 1989-10-17 DE DE68919851T patent/DE68919851T2/de not_active Expired - Lifetime
-
1991
- 1991-06-08 KR KR91700575A patent/KR0140194B1/ko not_active Expired - Fee Related
-
1995
- 1995-02-09 GR GR950400270T patent/GR3015038T3/el unknown
Also Published As
| Publication number | Publication date |
|---|---|
| KR920702858A (ko) | 1992-10-28 |
| KR0140194B1 (en) | 1998-06-15 |
| DE68919851T2 (de) | 1995-07-06 |
| EP0423401A1 (en) | 1991-04-24 |
| GR3015038T3 (en) | 1995-05-31 |
| CA2000446A1 (en) | 1991-04-11 |
| EP0423401B1 (en) | 1994-12-07 |
| US4872886A (en) | 1989-10-10 |
| WO1991005835A1 (en) | 1991-05-02 |
| DE68919851D1 (de) | 1995-01-19 |
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