GB947164A - Improvements in or relating to the production of combustible gas - Google Patents

Improvements in or relating to the production of combustible gas

Info

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
Application number
GB12975/60A
Inventor
Geoffrey Milner
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Power Gas Corp Ltd
Original Assignee
Power Gas Corp Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Power Gas Corp Ltd filed Critical Power Gas Corp Ltd
Priority to GB12975/60A priority Critical patent/GB947164A/en
Publication of GB947164A publication Critical patent/GB947164A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32Production 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
    • C01B3/34Production 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
    • C01B3/46Production 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
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency
    • Y02P20/129Energy 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.
GB12975/60A 1960-04-12 1960-04-12 Improvements in or relating to the production of combustible gas Expired GB947164A (en)

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)

* Cited by examiner, † Cited by third party
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

Cited By (4)

* Cited by examiner, † Cited by third party
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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