GB282573A - Improvements in the production of water gas and hydrogen - Google Patents

Improvements in the production of water gas and hydrogen

Info

Publication number
GB282573A
GB282573A GB4943/27A GB494327A GB282573A GB 282573 A GB282573 A GB 282573A GB 4943/27 A GB4943/27 A GB 4943/27A GB 494327 A GB494327 A GB 494327A GB 282573 A GB282573 A GB 282573A
Authority
GB
United Kingdom
Prior art keywords
water gas
methane
hydrogen
temperature
catalyst
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
GB4943/27A
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.)
Synthetic Ammonia & Nitrates
Original Assignee
Synthetic Ammonia & Nitrates
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 Synthetic Ammonia & Nitrates filed Critical Synthetic Ammonia & Nitrates
Priority to GB4943/27A priority Critical patent/GB282573A/en
Publication of GB282573A publication Critical patent/GB282573A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • 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
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Catalysts (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

282,573. Synthetic Ammonia & Nitrates, Ltd., and Humphrey, H. A. Feb. 22, 1927. Coking processes.-Coal is dried at a temperature of 200 to 300‹ C. by hot combustion gases to which air is added to effect partial oxidation so as to control the coking properties of the material, and is then subjected to low temperature carbonization at net exceeding 600‹ C. to give a semi-coke, in the form of lumps which are suitable for use in a water gas generator. Tho water gas may be treated with steam at high temperatures to convert the methane into carbon monoxide and hydrogen. The semi-coke may, however, be heated to a higher temperature before use for the generation of water gas free from methane. The gas mixture, is then passed over a catalyst containing finely divided iron or metals at a temperature of 200-300‹ C. to generate higher paraffin hydrocarbons. The residue from this treatment or the origrnal gas mixture is compressed and passed, after separation of the paraffins and methane if present, over a catalyst such as basic zinc chromate for the production of methanol or may be treated with steam in the presence of an iron oxide catalyst at about 500‹ C. converting the carbon monoxide into carbon dioxide which is then removed, leaving hydrogen which is mixed with the proportion of nitrogen required for the synthesis of ammonia. Specification 292,060 is referred to.
GB4943/27A 1927-02-22 1927-02-22 Improvements in the production of water gas and hydrogen Expired GB282573A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB4943/27A GB282573A (en) 1927-02-22 1927-02-22 Improvements in the production of water gas and hydrogen

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB4943/27A GB282573A (en) 1927-02-22 1927-02-22 Improvements in the production of water gas and hydrogen

Publications (1)

Publication Number Publication Date
GB282573A true GB282573A (en) 1927-12-29

Family

ID=9786769

Family Applications (1)

Application Number Title Priority Date Filing Date
GB4943/27A Expired GB282573A (en) 1927-02-22 1927-02-22 Improvements in the production of water gas and hydrogen

Country Status (1)

Country Link
GB (1) GB282573A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106544058A (en) * 2017-01-24 2017-03-29 北京金泰瑞和工程科技有限公司 Fixed bed pressured gasification system

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106544058A (en) * 2017-01-24 2017-03-29 北京金泰瑞和工程科技有限公司 Fixed bed pressured gasification system

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