GB635913A - Improvements in or relating to the production of synthesis gas mixtures containing carbon monoxide and hydrogen - Google Patents
Improvements in or relating to the production of synthesis gas mixtures containing carbon monoxide and hydrogenInfo
- Publication number
- GB635913A GB635913A GB13595/47A GB1359547A GB635913A GB 635913 A GB635913 A GB 635913A GB 13595/47 A GB13595/47 A GB 13595/47A GB 1359547 A GB1359547 A GB 1359547A GB 635913 A GB635913 A GB 635913A
- Authority
- GB
- United Kingdom
- Prior art keywords
- steam
- refractory material
- oxygen
- gas
- carbon monoxide
- 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
-
- 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
- C10K1/02—Dust removal
- C10K1/026—Dust removal by centrifugal forces
-
- 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
- C10K3/00—Modifying the chemical composition of combustible gases containing carbon monoxide to produce an improved fuel, e.g. one of different calorific value, which may be free from carbon monoxide
- C10K3/001—Modifying the chemical composition of combustible gases containing carbon monoxide to produce an improved fuel, e.g. one of different calorific value, which may be free from carbon monoxide by thermal treatment
-
- 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
- C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
- C10J2300/0913—Carbonaceous raw material
- C10J2300/093—Coal
- C10J2300/0933—Coal fines for producing water 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
- C10J2300/00—Details of gasification processes
- C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
- C10J2300/0983—Additives
- C10J2300/0993—Inert particles, e.g. as heat exchange medium in a fluidized or moving bed, heat carriers, sand
-
- 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
- C10J2300/16—Integration of gasification processes with another plant or parts within the plant
- C10J2300/164—Integration of gasification processes with another plant or parts within the plant with conversion of synthesis gas
- C10J2300/1656—Conversion of synthesis gas to chemicals
-
- 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
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)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
635,913. Oil gas ; water gas generation. STANDARD OIL DEVELOPMENT CO. May 20, 1947, No. 13595. Convention date, Sept. 27, 1946. [Classes 55 (i) and 55 (ii)] Gas mixtures containing mainly hydrogen and carbon monoxide are produced by charging liquified bituminous carbonaceous material into a fluidized bed of refractory material into which oxygen and steam are also introduced, the gaseous products being discharged into an upper part of the reaction zone to which further oxygen is supplied. A dense suspension of powdered refractory material, e.g. silica, alumina or magnesia is maintained in a fluidized state in a reaction chamber 1 by an oxygen-steam mixture admitted through a line 3 and a heavy oil tar or pitch, such as a vacuum distillation residue of the bottoms of a Venezuelan crude, heated to 200- 450‹ F. is sprayed with steam through a nozzle 7 within or above the dense phase. Carbon dioxide may be added with the steam. Partial combustion occurs at 1,500-2,000‹ F. and preferably 115-300 lb. per sq. in. pressure. Secondary oxygen supplied through a line 10 effects oxidation of lighter hydrocarbons and soot in a zone extending to the top of an enlargement la of the chamber, at temperatures up to 3,000‹ F. The ,gases pass through a waste heat boiler 17 and dust separator 22 to hydrocarbon synthesis apparatus. Refractory material is desirably supplied continuously from a hopper 40 and removed by a pipe 45 in order to remove salts and other metallic compounds present in the pitch. Gas and steam may be injected through pipes 43, 44. The Specification as open to inspection under Sect. 91 describes the use of low grade coals, shales and less readily liquifiable material such as asphalt which may be ground and mixed with the refractory material. This may be dispensed with in the case of high ash containing fuels. This subject-matter does not appear in the Specification as accepted.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US635913XA | 1946-09-27 | 1946-09-27 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB635913A true GB635913A (en) | 1950-04-19 |
Family
ID=22050215
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB13595/47A Expired GB635913A (en) | 1946-09-27 | 1947-05-20 | Improvements in or relating to the production of synthesis gas mixtures containing carbon monoxide and hydrogen |
Country Status (1)
| Country | Link |
|---|---|
| GB (1) | GB635913A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE1160829B (en) * | 1956-08-20 | 1964-01-09 | Phillips Petroleum Co | Method of activating a solid catalyst |
-
1947
- 1947-05-20 GB GB13595/47A patent/GB635913A/en not_active Expired
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE1160829B (en) * | 1956-08-20 | 1964-01-09 | Phillips Petroleum Co | Method of activating a solid catalyst |
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