GB427967A - Improvements in the manufacture of hydrogen - Google Patents
Improvements in the manufacture of hydrogenInfo
- 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
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
- C01B3/06—Production 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
- C01B3/061—Production 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
-
- 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
- C01B3/06—Production 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
- C01B3/10—Production 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
-
- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen 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.
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)
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 |
-
1933
- 1933-10-30 GB GB30139/33A patent/GB427967A/en not_active Expired
Cited By (4)
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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