GB672500A - Improvements in or relating to the desulfurization of gaseous mixtures particularly synthesis gases - Google Patents
Improvements in or relating to the desulfurization of gaseous mixtures particularly synthesis gasesInfo
- Publication number
- GB672500A GB672500A GB16946/50A GB1694650A GB672500A GB 672500 A GB672500 A GB 672500A GB 16946/50 A GB16946/50 A GB 16946/50A GB 1694650 A GB1694650 A GB 1694650A GB 672500 A GB672500 A GB 672500A
- Authority
- GB
- United Kingdom
- Prior art keywords
- char
- line
- gas
- generator
- steam
- 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
- C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
- C10K1/00—Purifying combustible gases containing carbon monoxide
- C10K1/32—Purifying combustible gases containing carbon monoxide with selectively adsorptive solids, e.g. active 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
- 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
- C10J3/482—Gasifiers with stationary fluidised bed
-
- 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
Abstract
672,500. Gas-purifying process. STANDARD OIL DEVELOPMENT CO. July 6, 1950 [March 23, 1950], No. 16946/50. Class 55 (ii). Sulphur compounds in water gas produced by gasifying solid carbonaceous materials with steam, are removed by bringing the gas into contact with a highly absorptive char of high surface area which has been withdrawn from the gasification zone. In the apparatus shown, finely-divided coal is fed from a hopper 1 into a first stage generator 5 and formed into a dense bed fluidized by a mixture of steam and oxygen admitted through lines 3 and 4. Water gas discharges through lines 10 and 11. The coke or char remains in generator 5 until its carbon content is between 45 and 75 per cent, when.its surface area is found to be a maximum, usually exceeding 500 square metres per gram. It is then withdrawn through lines 12 and 20 and is carried forward by the made water-gas from line 11, through a heat-exchanger 21, where the temperature of the suspension is lowered to between 75‹ and 400‹ F., to a desulphurizer 23, 1 to 2 per cent of air being added to the suspension through a line 22. A fluidized bed of the char is maintained in chamber 23, the organic sulphur compounds in the gas being adsorbed by the char and the H 2 S being oxidized by the air with the formation of free sulphur which deposits on the char. A cooling coil 34 maintains the bed at the correct temperature. Purified gas is led off through a line 24 and the sulphurized char through line 25, an air current from line 27 fluidizing the char in a regenerator vessel 28, so that the sulphur burns to SO 2 which discharges through line 29. The cleaned char leaves vessel 28 by line 30 and is taken up by a steam-oxygen mixture and fluidized in a second stage generator 16, the water-gas produced being added to that from generator 5, whilst ash is discharged through a line 19. If more char is produced in generator 5 than is required for desulphurization, it can be fed direct to generator 16 via line 14.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US672500XA | 1950-03-23 | 1950-03-23 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB672500A true GB672500A (en) | 1952-05-21 |
Family
ID=22074734
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB16946/50A Expired GB672500A (en) | 1950-03-23 | 1950-07-06 | Improvements in or relating to the desulfurization of gaseous mixtures particularly synthesis gases |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB672500A (en) |
-
1950
- 1950-07-06 GB GB16946/50A patent/GB672500A/en not_active Expired
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