US2147780A - Production of hydrogen - Google Patents

Production of hydrogen Download PDF

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Publication number
US2147780A
US2147780A US104061A US10406136A US2147780A US 2147780 A US2147780 A US 2147780A US 104061 A US104061 A US 104061A US 10406136 A US10406136 A US 10406136A US 2147780 A US2147780 A US 2147780A
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US
United States
Prior art keywords
iron
catalyst
oxide
iron oxide
steam
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 - Lifetime
Application number
US104061A
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English (en)
Inventor
Kahler Friedrich Von
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.)
American Magnesium Metals Corp
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American Magnesium Metals Corp
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Filing date
Publication date
Application filed by American Magnesium Metals Corp filed Critical American Magnesium Metals Corp
Application granted granted Critical
Publication of US2147780A publication Critical patent/US2147780A/en
Anticipated expiration legal-status Critical
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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
    • C01B3/12Production 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 carbon monoxide
    • C01B3/16Production 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 carbon monoxide using catalysts
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/76Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/78Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with alkali- or alkaline earth metals
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J27/00Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/20Carbon compounds
    • 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

Definitions

  • Thisinvention relates to the production of hydrogen by reacting a mixture of carbon monoxide and steam, and more particularly to such a process involving the useof an improved catalyst.
  • the conversion of carbon monoxide with steam is carried out with the aid of catalysts which contain, apart from magnesium oxide and alkali carbonate (preferably potassium carbonate) and carbonaceous substances, as a further constituent iron oxide in the form of native iron ores.
  • Red iron ore micaceous iron-ore, haematite, bloodstone, and the like
  • ferric oxide FeezOz
  • Iron in the form of ferric hydroxides occur in nature in brown iron ores (limonite containing FB403(OH)6, bog iron ores containing FezO(Ol-I) 4, gothite containing FeO(OH), and the like).
  • iron ores which yield ferric oxide or ferric hydroxide-under heat, examples of such ores being sideritecontainingFeCOz and magnetite containing Fes04.
  • these fourcomponent catalysts also retain undiminished the poison-resisting properties of the known three-component catalysts, more particularly in respect of the commonestcatalyst poison, name-- 1y sulphur, in inorganic ,or organic combination. This state of things shows that the components combine, within the range of proportions here concerned,'to form a new unity having decisive- 1y altered properties.
  • the quantity of iron oxides in the mixture required to obtain marked enhancement of the catalytical activity of the three-component catalysts in question depends on the proportions of the other constituents'of the catalyst mass.
  • the proportion of iron oxides to-thetotal quantity of MgO +K2CO3 contained in the catalyst should be between 1:30 and 1:2.
  • the iron oxide content should preferably amount to at the most of the entire catalyst mass.
  • the magnesium oxide used may be in the state of caustic burned or calcined magnesia, or of precipitated magnesia.
  • native iron oxide or ferric hydroxide instead of adding native iron oxide or ferric hydroxide to the magnesia it is also possible to start with magnesite rich in iron or its transition states to breunerite (MgCOaFeCOa) without any further addition of iron.
  • the catalyst may for example have the following composition:-
  • iron oxide in the following claims to include not only oxides but also hydroxides of iron and combinations yielding iron oxide or bydroxide under heat, while the numerical indications refer to ferric oxide (F8203).
  • the process of producing hydrogen which comprises causing steam to react with carbon monoxide according to the reaction in the presence of a catalyst consisting principally of a mixture of magnesium oxide, alkali carbonate and carbonaceous substance, and containing a considerably smaller amount of iron oxide in the form of native iron ore, the ratio of the quantity of iron oxide to the total quantity of magnesium oxide and alkali'carbonate in the catalyst being between 1:30 and 1:2.
  • the process of producing hydrogen which comprises causing steam to react with carbon monoxide according to the reaction in the presence of a catalyst consisting principally of a mixture of calcined magnesite, potassium carbonate and carbonaceous substance, and containing as an activator a considerably smaller amount of iron oxide in the form of native iron ore, the ratio of the quantity of iron oxide to the total quantity of magnesium oxide and alkali carbonate in the catalyst being between 1:30 and 1:2.
  • the process of producing hydrogen which comprises causing steam to react with carbon monoxide according to the reaction in the presence of a catalyst consisting principally of a mixture of calcined magnesite, alkali carbonate and carbonaceous substance, and containing as an activator a considerably smaller amount of iron oxide in the form of native iron ore, the ratio of the quantity of iron oxide to the total quantity of magnesium oxide and alkali carbonate in the catalyst being between 1:30 and 1:2 and the iron oxide content amounting at the most to 10 per cent of the Whole of the catalyst mass.
  • a process of producing hydrogen including reacting a mixture of carbon monoxide and steam in the presence of a catalyst prepared from magnesitic material rich in iron by the addition of alkali carbonate and carbonaceous matter, the ratio of the quantity of iron oxide to the total quantity of magnesium oxide and alkali carbonate in the catalyst being between 1:30 and 1:2 and the iron oxide content amounting at the most to 10 per cent of the whole of the catalyst mass.
  • the process of producing hydrogen which comprises reacting a carbon monoxide-containing gaseous mixture rich in hydrogen, and steam in the presence of a catalyst consisting principally of a mixture of magnesium oxide, alkali carbonate and carbonaceous matter, and containing as an activator a considerably smaller amount of iron oxide in the form of native iron ore, the ratio of the quantity of iron oxide to the total quantity of magnesium oxide and alkali carbonate in the catalyst being between 1:30 and 1:2.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Inorganic Chemistry (AREA)
  • Catalysts (AREA)
  • Hydrogen, Water And Hydrids (AREA)
US104061A 1935-10-23 1936-10-05 Production of hydrogen Expired - Lifetime US2147780A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
AT464667X 1935-10-23

Publications (1)

Publication Number Publication Date
US2147780A true US2147780A (en) 1939-02-21

Family

ID=3674638

Family Applications (1)

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US104061A Expired - Lifetime US2147780A (en) 1935-10-23 1936-10-05 Production of hydrogen

Country Status (6)

Country Link
US (1) US2147780A (xx)
BE (1) BE417743A (xx)
DE (1) DE706868C (xx)
FR (1) FR811736A (xx)
GB (1) GB464667A (xx)
NL (1) NL44648C (xx)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2517177A (en) * 1945-08-28 1950-08-01 American Magnesium Metals Corp Method of producing hydrogen by converting carbon monoxide with steam
US2950258A (en) * 1956-08-29 1960-08-23 Phillips Petroleum Co Dehydrogenation catalyst
US3539297A (en) * 1968-04-08 1970-11-10 Exxon Research Engineering Co Preventing catalyst poisoning by sulfur
DE2054869A1 (de) * 1969-11-10 1971-05-19 Esso Research and Engineering Co , Linden, NJ (V St A ) Verfahren zur Frzeugung von Wasser stoff
US3932599A (en) * 1974-03-01 1976-01-13 Rheinische Braunkohlenwerke Aktiengesellschaft Method of obtaining hydrogen from steam
EP0532078A2 (en) * 1991-08-30 1993-03-17 Shell Internationale Researchmaatschappij B.V. Process for the preparation of a dehydrogenation catalyst and the use thereof
US20060177639A1 (en) * 2005-02-04 2006-08-10 Elzen Kerstin T Process for the production of primer surfacer-free multi-layer coatings

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3512831A (en) * 1964-08-24 1970-05-19 Hyland C Flint Spring seat
US4054644A (en) * 1972-03-16 1977-10-18 Exxon Research & Engineering Co. Water gas shift process
US4595787A (en) * 1985-06-24 1986-06-17 Phillips Petroleum Company Potassium carbonate supports, catalysts and olefin dimerization processes therewith

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2517177A (en) * 1945-08-28 1950-08-01 American Magnesium Metals Corp Method of producing hydrogen by converting carbon monoxide with steam
US2950258A (en) * 1956-08-29 1960-08-23 Phillips Petroleum Co Dehydrogenation catalyst
US3539297A (en) * 1968-04-08 1970-11-10 Exxon Research Engineering Co Preventing catalyst poisoning by sulfur
DE2054869A1 (de) * 1969-11-10 1971-05-19 Esso Research and Engineering Co , Linden, NJ (V St A ) Verfahren zur Frzeugung von Wasser stoff
US3932599A (en) * 1974-03-01 1976-01-13 Rheinische Braunkohlenwerke Aktiengesellschaft Method of obtaining hydrogen from steam
EP0532078A2 (en) * 1991-08-30 1993-03-17 Shell Internationale Researchmaatschappij B.V. Process for the preparation of a dehydrogenation catalyst and the use thereof
EP0532078A3 (en) * 1991-08-30 1993-05-12 Shell Internationale Research Maatschappij B.V. Process for the preparation of a dehydrogenation catalyst and the use thereof
AU649869B2 (en) * 1991-08-30 1994-06-02 Shell Internationale Research Maatschappij B.V. Process for the preparation of a dehydrogenation catalyst and the use thereof
US20060177639A1 (en) * 2005-02-04 2006-08-10 Elzen Kerstin T Process for the production of primer surfacer-free multi-layer coatings

Also Published As

Publication number Publication date
BE417743A (xx)
DE706868C (de) 1941-06-07
NL44648C (xx)
FR811736A (fr) 1937-04-21
GB464667A (en) 1937-04-22

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