GB427967A - Improvements in the manufacture of hydrogen - Google Patents

Improvements in the manufacture of hydrogen

Info

Publication number
GB427967A
GB427967A GB30139/33A GB3013933A GB427967A GB 427967 A GB427967 A GB 427967A GB 30139/33 A GB30139/33 A GB 30139/33A GB 3013933 A GB3013933 A GB 3013933A GB 427967 A GB427967 A GB 427967A
Authority
GB
United Kingdom
Prior art keywords
reaction
silicon
pipe
vessel
caustic soda
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
GB30139/33A
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Publication of GB427967A publication Critical patent/GB427967A/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
    • C01B3/06Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
    • C01B3/061Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents by reaction of metal oxides with water
    • 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
    • C01B3/06Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
    • C01B3/10Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents by reaction of water vapour with metals
    • 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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/36Hydrogen production from non-carbon containing sources, e.g. by water electrolysis

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Inorganic Chemistry (AREA)
  • Silicon Compounds (AREA)
  • Hydrogen, Water And Hydrids (AREA)

Abstract

<PICT:0427967/III/1> <PICT:0427967/III/2> In manufacture of hydrogen from silicon and a caustic alkali as described in Specification 399,110, wherein the acid silicate is produced, means are provided whereby the hot solution formed is removed from the reaction vessel so that the hydrogen may be withdrawn in a relatively cool condition. A pressure vessel 2, Fig. 3, is provided with a flange 4 to which is bolted a cover 5, a gasket 6 serving to render the cover gas tight. Carried in the interior is a series of perforated containers 11, 12, 13, the lowest of which contains a mixture of powdered silicon and caustic soda, the others being filled with granulated silicon. Water is added through a tube 9 in the cover, the reaction taking place in a few minutes and being of very short duration. After the completion of the reaction, a valve 17 in a pipe 15 is opened, the pipe dipping down to the bottom of the basket 11 and removing therefrom under the pressure of the hydrogen, the liquid contents of the vessel 2. One or more generators 2 may be mounted on a vehicle provided with a crane for operating the vessels 2, the gas produced being withdrawn by valved pipes 18 and conducted to a purifying vessel. In a modified form, the reaction may be rendered partially or wholly continuous, the vessel 2 being adapted to receive a metallic holder 24, Fig. 5, provided with perforated shelves 25, the lowest compartment serving to contain a mixture of caustic soda and silicon which functions as the starting charge, the other compartments being filled with granulated silicon. Water to start the reaction is introduced in the manner described with reference to Fig. 3, gas being withdrawn by a pipe 18 and the liquid contents by a pipe 5. To render the process continuous, a solution of caustic soda is pumped on to bubble trays 32 by a pipe 26, the solution being raised to the necessary temperature by the steam and gas generated by the starting reaction. Additional supplies of silicon may be added by a device consisting of a chamber having entrance and exit valves. In a second modification, an oil reservoir is provided so that the pump does not deal directly with the caustic soda solution.
GB30139/33A 1932-10-29 1933-10-30 Improvements in the manufacture of hydrogen Expired GB427967A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
FR427967X 1932-10-29

Publications (1)

Publication Number Publication Date
GB427967A true GB427967A (en) 1935-04-30

Family

ID=8899084

Family Applications (1)

Application Number Title Priority Date Filing Date
GB30139/33A Expired GB427967A (en) 1932-10-29 1933-10-30 Improvements in the manufacture of hydrogen

Country Status (1)

Country Link
GB (1) GB427967A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004052774A2 (en) * 2002-12-11 2004-06-24 Wacker-Chemie Gmbh Method for producing hydrogen
CN109650331A (en) * 2019-02-15 2019-04-19 嘉兴尚能光伏材料科技有限公司 Hydrogen production process and hydrogen generating system based on silicon powder and silicon material
WO2019158941A1 (en) * 2018-02-16 2019-08-22 Silicon Fuel Limited Hydrogen generation

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004052774A2 (en) * 2002-12-11 2004-06-24 Wacker-Chemie Gmbh Method for producing hydrogen
WO2004052774A3 (en) * 2002-12-11 2004-10-07 Wacker Chemie Gmbh Method for producing hydrogen
WO2019158941A1 (en) * 2018-02-16 2019-08-22 Silicon Fuel Limited Hydrogen generation
CN109650331A (en) * 2019-02-15 2019-04-19 嘉兴尚能光伏材料科技有限公司 Hydrogen production process and hydrogen generating system based on silicon powder and silicon material

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