GB947164A - Improvements in or relating to the production of combustible gas - Google Patents
Improvements in or relating to the production of combustible gasInfo
- Publication number
- GB947164A GB947164A GB12975/60A GB1297560A GB947164A GB 947164 A GB947164 A GB 947164A GB 12975/60 A GB12975/60 A GB 12975/60A GB 1297560 A GB1297560 A GB 1297560A GB 947164 A GB947164 A GB 947164A
- Authority
- GB
- United Kingdom
- Prior art keywords
- air
- plant
- products
- catalyst
- mixture
- 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
- 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
- C01B3/46—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 discontinuously preheated non-moving solid materials, e.g. blast and run
-
- 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)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Inorganic Chemistry (AREA)
- Hydrogen, Water And Hydrids (AREA)
- Furnace Details (AREA)
Abstract
<PICT:0947164/C3/1> A cyclic process for producing combustible gas from fluid hydrocarbons by a catalytic process includes in each cycle a plant-heating period which comprises passing through the plant and catalyst bed 41 a hot mixture of inert gases, e.g. nitrogen or carbon dioxide or products of combustion, with or without air, see Fig. 1 (not shown), the mixture having a temperature in the range 900 DEG to 1200 DEG C. and a free oxygen content of between 3% and 8% of the total gases, including water vapour. The plant may be of the uniflow, non-regenerative type, Fig. 1, or of the regenerative type shown in Fig. 2. During a gas-making period, steam is introduced at 55 and, after passing over pre-heated chequer bricks 43, is mixed with oil to be reformed which is sprayed at 56 into a chamber 42. The mixture passes over the catalyst 41 and chequer bricks 47 in an air pre-heater 46 to an outlet 49. During a plant-heating period, air is delivered by conduits 58 . . . 60 to the pre-heater 46 and fuel (oil) and air entering respectively at 61, 62 are burnt in a chamber 45, the products of combustion passing over catalyst 41 and bricks 43 to an outlet 54. Some of these products are recycled via conduits 63, 65, 60 and additional air and fuel may be burnt at 68 in the chamber 42. Control of the various proportions of fuel, air and products of combustion employed during the plant-heating period enable the temperature and oxygen content of the gas mixture passing over the catalyst 41 to be controlled.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB12975/60A GB947164A (en) | 1960-04-12 | 1960-04-12 | Improvements in or relating to the production of combustible gas |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB12975/60A GB947164A (en) | 1960-04-12 | 1960-04-12 | Improvements in or relating to the production of combustible gas |
Publications (1)
Publication Number | Publication Date |
---|---|
GB947164A true GB947164A (en) | 1964-01-22 |
Family
ID=10014535
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB12975/60A Expired GB947164A (en) | 1960-04-12 | 1960-04-12 | Improvements in or relating to the production of combustible gas |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB947164A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2020206145A1 (en) * | 2019-04-05 | 2020-10-08 | Exxonmobil Research And Engineering Company | Oxycombustion with co2 capture in reverse flow reactors |
-
1960
- 1960-04-12 GB GB12975/60A patent/GB947164A/en not_active Expired
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2020206145A1 (en) * | 2019-04-05 | 2020-10-08 | Exxonmobil Research And Engineering Company | Oxycombustion with co2 capture in reverse flow reactors |
CN113646259A (en) * | 2019-04-05 | 2021-11-12 | 埃克森美孚研究工程公司 | Utilization of CO in a countercurrent reactor2Trapped oxygen combustion |
US11465903B2 (en) | 2019-04-05 | 2022-10-11 | ExxonMobil Technology and Engineering Company | Oxycombustion with CO2 capture in reverse flow reactors |
CN113646259B (en) * | 2019-04-05 | 2023-12-29 | 埃克森美孚技术与工程公司 | Utilization of CO in a countercurrent reactor 2 Captured oxygen combustion |
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