GB1519090A - Production of clean synthesis or fuel gas - Google Patents
Production of clean synthesis or fuel gasInfo
- Publication number
- GB1519090A GB1519090A GB45428/76A GB4542876A GB1519090A GB 1519090 A GB1519090 A GB 1519090A GB 45428/76 A GB45428/76 A GB 45428/76A GB 4542876 A GB4542876 A GB 4542876A GB 1519090 A GB1519090 A GB 1519090A
- Authority
- GB
- United Kingdom
- Prior art keywords
- gas
- immersion fluid
- temperature
- particulate carbon
- stream
- 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
Links
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
- C10J3/46—Gasification of granular or pulverulent flues in suspension
- C10J3/48—Apparatus; Plants
- C10J3/485—Entrained flow gasifiers
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
- C01B3/32—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
- C01B3/34—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
- C01B3/36—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using oxygen or mixtures containing oxygen as gasifying agents
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/50—Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification
-
- 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
- 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
- C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
- C10K1/00—Purifying combustible gases containing carbon monoxide
- C10K1/08—Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors
-
- 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
- C10K1/08—Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors
- C10K1/10—Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors with aqueous liquids
- C10K1/101—Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors with aqueous liquids with water only
-
- 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
- C10K1/08—Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors
- C10K1/16—Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors with non-aqueous liquids
- C10K1/18—Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors with non-aqueous liquids hydrocarbon oils
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2203/00—Integrated processes for the production of hydrogen or synthesis gas
- C01B2203/04—Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
- C01B2203/0465—Composition of the impurity
- C01B2203/049—Composition of the impurity the impurity being carbon
-
- 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
- C10J2300/1223—Heating the gasifier by burners
-
- 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
Abstract
1519090 Synthesis gas generator TEXACO DEVELOPMENT CORP 2 Nov 1976 [22 Dec 1975 (3)] 45428/76 Heading C5E A process for the production of clean synthesis gas or fuel gas comprises (a) partial oxidation of a feed comprising a dispersion of particulate carbon in a liquid hydrocarbonaceous fuel with a freeoxygen-containing gas in a free flow, unpacked gas generator, at a temperature of from 1300 to 3000‹F., and a pressure of from 1 to 250 atmospheres, to produce an effluent gas stream comprising H 2 , CO, CO 2 , H 2 O and entrained particulate carbon; (b) cooling the effluent gas stream in a quench zone to a temperature of from 300 to 900‹F., but above the dew point of water in the effluent gas stream, and simultaneously removing the entrained particulate carbon, by discharging the effluent gas stream directly into a body of immersion fluid comprising a dispersion of particulate carbon in liquid hydrocarbonaceous fuel, and recovering a clean gaseous stream comprising H 2 , CO, CO 2 , and H 2 O; (c) cooling at least a portion of the thus heated immersion fluid to a temperature of from 300 to 850‹F. by indirect heat exchange, and recycling at least a portion of the resulting cooled immersion fluid to the quench zone; and (d) introducing a portion of the hot immersion fluid produced in step (b) or a portion of the cooled immersion fluid into the gas generator as a portion of the feed. The partial oxidation may be carried out in the presence of a temperature moderator such as H 2 O, CO 2 , flue gas or recycle gas. The clean gaseous stream may be further purified by scrubbing with liquid hydrocarbonaceous fuel or water, and the scrubbing liquid may be recycled into the gasifier.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US05/643,561 US4007019A (en) | 1975-12-22 | 1975-12-22 | Production of clean synthesis or fuel gas |
US05/643,458 US4007018A (en) | 1975-12-22 | 1975-12-22 | Production of clean synthesis or fuel gas |
US05/643,069 US4007017A (en) | 1975-12-22 | 1975-12-22 | Production of clean synthesis or fuel gas |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1519090A true GB1519090A (en) | 1978-07-26 |
Family
ID=27417700
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB45428/76A Expired GB1519090A (en) | 1975-12-22 | 1976-11-02 | Production of clean synthesis or fuel gas |
Country Status (11)
Country | Link |
---|---|
JP (1) | JPS5277106A (en) |
AU (1) | AU497294B2 (en) |
CA (1) | CA1080474A (en) |
DK (1) | DK574176A (en) |
ES (1) | ES453761A1 (en) |
FR (1) | FR2336470A1 (en) |
GB (1) | GB1519090A (en) |
GR (1) | GR62017B (en) |
IT (1) | IT1203052B (en) |
SE (1) | SE7613834L (en) |
YU (1) | YU302776A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2125429A (en) * | 1982-08-04 | 1984-03-07 | Humphreys & Glasgow Ltd | Tar removal process |
WO2017135811A1 (en) * | 2016-02-05 | 2017-08-10 | Black Bear Carbon B.V. | Method for treatment of a hot pyrolysis gas |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3219316A1 (en) * | 1982-05-22 | 1983-11-24 | Ruhrchemie Ag, 4200 Oberhausen | METHOD AND DEVICE FOR PRODUCING SYNTHESIS GAS BY PARTIAL OXIDATION OF COAL-WATER SUSPENSIONS |
JPS61127355A (en) * | 1984-11-26 | 1986-06-14 | Shigeyoshi Arai | Letter board for photographic typesetting machine |
JPS63145401U (en) * | 1987-03-16 | 1988-09-26 | ||
JPH06315301A (en) * | 1993-04-30 | 1994-11-15 | Keiji Ikeo | Hoe |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3232727A (en) * | 1961-12-13 | 1966-02-01 | Texaco Inc | Synthesis gas generation |
US3639261A (en) * | 1968-03-27 | 1972-02-01 | Texaco Inc | Process for the generation of synthesis gas from oil |
US3544291A (en) * | 1968-04-22 | 1970-12-01 | Texaco Inc | Coal gasification process |
US3816332A (en) * | 1971-04-07 | 1974-06-11 | Texaco Development Corp | Synthesis gas production |
FR2146530A5 (en) * | 1971-07-16 | 1973-03-02 | Texaco Development Corp | Synthesis gas from coke slurry withoutpreheating |
US3928000A (en) * | 1973-12-28 | 1975-12-23 | Texaco Inc | Production of a clean methane-rich fuel gas from high-sulfur containing hydrocarbonaceous materials |
US3929429A (en) * | 1974-09-26 | 1975-12-30 | Texaco Inc | Fuel gas from solid carbonaceous fuels |
-
1976
- 1976-11-02 GB GB45428/76A patent/GB1519090A/en not_active Expired
- 1976-11-19 AU AU19846/76A patent/AU497294B2/en not_active Expired
- 1976-11-29 ES ES453761A patent/ES453761A1/en not_active Expired
- 1976-11-29 CA CA266,740A patent/CA1080474A/en not_active Expired
- 1976-12-06 JP JP51145716A patent/JPS5277106A/en active Granted
- 1976-12-09 SE SE7613834A patent/SE7613834L/en not_active Application Discontinuation
- 1976-12-10 YU YU03027/76A patent/YU302776A/en unknown
- 1976-12-10 FR FR7637305A patent/FR2336470A1/en active Granted
- 1976-12-18 GR GR52432A patent/GR62017B/en unknown
- 1976-12-20 DK DK574176A patent/DK574176A/en not_active Application Discontinuation
- 1976-12-21 IT IT30737/76A patent/IT1203052B/en active
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2125429A (en) * | 1982-08-04 | 1984-03-07 | Humphreys & Glasgow Ltd | Tar removal process |
WO2017135811A1 (en) * | 2016-02-05 | 2017-08-10 | Black Bear Carbon B.V. | Method for treatment of a hot pyrolysis gas |
CN109072105A (en) * | 2016-02-05 | 2018-12-21 | 黑熊碳有限公司 | Method for handling hot pyrolysis gas |
Also Published As
Publication number | Publication date |
---|---|
FR2336470B1 (en) | 1981-07-24 |
JPS5277106A (en) | 1977-06-29 |
CA1080474A (en) | 1980-07-01 |
YU302776A (en) | 1982-05-31 |
AU497294B2 (en) | 1978-12-07 |
ES453761A1 (en) | 1978-01-01 |
IT1203052B (en) | 1989-02-15 |
AU1984676A (en) | 1978-05-25 |
JPS5333601B2 (en) | 1978-09-14 |
GR62017B (en) | 1979-02-16 |
DK574176A (en) | 1977-06-23 |
SE7613834L (en) | 1977-06-23 |
FR2336470A1 (en) | 1977-07-22 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PS | Patent sealed | ||
PCNP | Patent ceased through non-payment of renewal fee |