GB1017871A - Improvements in and relating to the manufacture of combustible gases - Google Patents
Improvements in and relating to the manufacture of combustible gasesInfo
- Publication number
- GB1017871A GB1017871A GB6222/62A GB622262A GB1017871A GB 1017871 A GB1017871 A GB 1017871A GB 6222/62 A GB6222/62 A GB 6222/62A GB 622262 A GB622262 A GB 622262A GB 1017871 A GB1017871 A GB 1017871A
- Authority
- GB
- United Kingdom
- Prior art keywords
- gas
- zone
- steam
- oil
- water 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
Links
- 239000007789 gas Substances 0.000 title abstract 20
- 238000004519 manufacturing process Methods 0.000 title 1
- 239000003921 oil Substances 0.000 abstract 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 7
- 239000000571 coke Substances 0.000 abstract 3
- 238000006243 chemical reaction Methods 0.000 abstract 2
- 238000010438 heat treatment Methods 0.000 abstract 2
- 238000000034 method Methods 0.000 abstract 2
- 238000010926 purge Methods 0.000 abstract 2
- 239000004215 Carbon black (E152) Substances 0.000 abstract 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 abstract 1
- 230000003197 catalytic effect Effects 0.000 abstract 1
- 125000004122 cyclic group Chemical group 0.000 abstract 1
- 239000000295 fuel oil Substances 0.000 abstract 1
- 229930195733 hydrocarbon Natural products 0.000 abstract 1
- 150000002430 hydrocarbons Chemical class 0.000 abstract 1
- 239000001257 hydrogen Substances 0.000 abstract 1
- 229910052739 hydrogen Inorganic materials 0.000 abstract 1
- 239000004449 solid propellant Substances 0.000 abstract 1
- 238000005406 washing Methods 0.000 abstract 1
- 239000002918 waste heat Substances 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
- C10J1/00—Production of fuel gases by carburetting air or other gases without pyrolysis
- C10J1/213—Carburetting by pyrolysis of solid carbonaceous material in a carburettor
-
- 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)
- Detergent Compositions (AREA)
Abstract
<PICT:1017871/C4-C5/1> A combustible gas is made by a cyclic process which includes a plant-heating and gas-making periods, the process comprising gasifying a hydrocarbon oil with a hydrogen-containing gas (steam) in a zone 27, gasifying solid fuel (coke) with steam in a second zone 1, washing the oil gas and the water gas separately at 88, 65 respectively, passing the washed water gas through a heated, catalytic co-conversion apparatus 78, mixing the washed oil gas and the converted water gas, e.g. at 100, and generating blow gases from the coke in the zone 1 to heat that zone, and combusting the blow gases, e.g. at 16, to heat the zone 27. The apparatus operates as follows:-(a) During plant-heating, valves 9, 15, 60 are open and the rest shut, air being supplied through a pipe 8 to the coke 6 to form blow gases which are combusted at 16 by admitting secondary air through a pipe 17. Fuel oil may be burnt at 31, and hot gases pass via fixing chamber 41 and riser conduit 44 to a waste heat boiler 57 and atmosphere at 60. Free CO may be combusted in 44 by admitting tertiary air at 49, (b) steam purging of zones 1, 27 and 42, 44 from pipes 11, 28 follows, (c) up-run gas-making is started by opening valves 21, 104, and closing 15, 60. Steam is admitted by pipe 11 to the zone 1, water gas passing to the wash box 65, scrubber 68, and a holder 73. Simultaneously, oil gas is made at 27, by steam entering at 28 and oil at 39, the gas being "fixed" at 42, washed at 88 and cooled and scrubbed at 93, (d) water gas is made during a back-run, where steam is passed from 54 through the chamber 42 and zones 27, 1, water gas passing via pipe 25 or (e) during a down-run, where steam is admitted to the zone 1 at 62, valve 15 being closed. Oil gas may be made during the down-run, (f) steam purging from 11 via zone 1 to the wash box 65 completes the cycle. The water gas is boosted at 76 and after CO-conversion at 78, passes via a cooler 82 to join the oil gas in holder 100. Two specific examples are described.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB6222/62A GB1017871A (en) | 1962-02-17 | 1962-02-17 | Improvements in and relating to the manufacture of combustible gases |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB6222/62A GB1017871A (en) | 1962-02-17 | 1962-02-17 | Improvements in and relating to the manufacture of combustible gases |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB1017871A true GB1017871A (en) | 1966-01-19 |
Family
ID=9810628
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB6222/62A Expired GB1017871A (en) | 1962-02-17 | 1962-02-17 | Improvements in and relating to the manufacture of combustible gases |
Country Status (1)
| Country | Link |
|---|---|
| GB (1) | GB1017871A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2163449A (en) * | 1984-07-18 | 1986-02-26 | Shell Int Research | Production of gas mixtures containing hydrogen and carbon monoxide |
| CN109777448A (en) * | 2019-03-28 | 2019-05-21 | 陕西驭腾实业有限公司 | A kind of coke oven coke oven uprising tube raw coke oven gas waste heat is used to that tube furnace to be replaced to take off benzene device |
-
1962
- 1962-02-17 GB GB6222/62A patent/GB1017871A/en not_active Expired
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2163449A (en) * | 1984-07-18 | 1986-02-26 | Shell Int Research | Production of gas mixtures containing hydrogen and carbon monoxide |
| CN109777448A (en) * | 2019-03-28 | 2019-05-21 | 陕西驭腾实业有限公司 | A kind of coke oven coke oven uprising tube raw coke oven gas waste heat is used to that tube furnace to be replaced to take off benzene device |
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