GB940960A - Process for the catalytic conversion of carbon monoxide with steam to form hydrogen and carbon dioxide - Google Patents
Process for the catalytic conversion of carbon monoxide with steam to form hydrogen and carbon dioxideInfo
- Publication number
- GB940960A GB940960A GB4039660A GB4039660A GB940960A GB 940960 A GB940960 A GB 940960A GB 4039660 A GB4039660 A GB 4039660A GB 4039660 A GB4039660 A GB 4039660A GB 940960 A GB940960 A GB 940960A
- Authority
- GB
- United Kingdom
- Prior art keywords
- sulphide
- catalyst
- steam
- carbon dioxide
- cobalt
- 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
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
- C10K3/00—Modifying the chemical composition of combustible gases containing carbon monoxide to produce an improved fuel, e.g. one of different calorific value, which may be free from carbon monoxide
- C10K3/02—Modifying the chemical composition of combustible gases containing carbon monoxide to produce an improved fuel, e.g. one of different calorific value, which may be free from carbon monoxide by catalytic treatment
- C10K3/04—Modifying the chemical composition of combustible gases containing carbon monoxide to produce an improved fuel, e.g. one of different calorific value, which may be free from carbon monoxide by catalytic treatment reducing the carbon monoxide content, e.g. water-gas shift [WGS]
-
- 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
- C01B3/12—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 carbon monoxide
- C01B3/16—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 carbon monoxide using catalysts
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Inorganic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Catalysts (AREA)
Abstract
Hydrogen and carbon dioxide are produced from steam and carbon monoxide using as catalyst a mixture of a sulphide of cobalt and/or nickel together with one or more sulphides of the transition groups VA, VIA, and VIIA of the Periodic System of Leverenz, used either alone or on a carrier. The catalyst may also contain iron or copper sulphide. The reaction may be at superatmospheric pressure, e.g. 7 to 35 atmospheres and in at least two stages, the mean temperature in each successive stage being 50 DEG to 100 DEG C. lower than that in the preceding stage. The gas to be converted may contain hydrogen sulphide and organic sulphur compounds. The catalyst is re-activated by oxidation and re-sulphurization in situ. Catalyst carriers used may be alumina, synthetic and natural silicates, oxides of magnesium, calcium, zirconium, chromium, titanium.ALSO:In the conversion of steam and carbon monoxide to hydrogen and carbon dioxide a catalyst is used comprising a sulphide of cobalt and/or nickel together with a sulphide of a metal of Group VA, VIA, and VIIA of the Leverenz Periodic system. Examples use 9,8% by weight of molybdenum sulphide, and 4,7% by weight of cobalt sulphide using active alumina as carrier, the catalyst used as cylindrical pellets 3 mm. high and 3 mm. diameter.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DER0055664 | 1959-11-25 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB940960A true GB940960A (en) | 1963-11-06 |
Family
ID=7410033
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB4039660A Expired GB940960A (en) | 1959-11-25 | 1960-11-24 | Process for the catalytic conversion of carbon monoxide with steam to form hydrogen and carbon dioxide |
Country Status (2)
Country | Link |
---|---|
DE (1) | DE1250792B (en) |
GB (1) | GB940960A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2011055132A1 (en) | 2009-11-05 | 2011-05-12 | Johnson Matthey Plc | Water gas shift reaction process |
US10099922B2 (en) | 2014-01-17 | 2018-10-16 | Johnson Matthey Public Limited Company | Method of loading a vessel |
US10494255B2 (en) | 2015-10-29 | 2019-12-03 | Johnson Matthey Public Limited Company | Water gas shift process |
US10807866B2 (en) | 2015-10-29 | 2020-10-20 | Johnson Matthey Public Limited Company | Water-gas shift catalyst |
US11014811B2 (en) | 2015-10-29 | 2021-05-25 | Johnson Matthey Public Limited Company | Water gas shift process |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1281051A (en) * | 1968-06-18 | 1972-07-12 | Exxon Research Engineering Co | Low temperature shift reaction involving an alkali metal compound and a hydrogenation dehydrogenation component |
BE758677A (en) * | 1969-11-10 | 1971-05-10 | Exxon Research Engineering Co | NEW CATALYST FOR THE PRODUCTION OF HYDROGEN BY DISPLACING GAS TO WATER |
US3793081A (en) * | 1971-04-28 | 1974-02-19 | Exxon Research Engineering Co | Sulfided transition metal fuel cell cathode catalysts |
NL175835B (en) * | 1973-04-17 | 1984-08-01 | Shell Int Research | Process for preparing a hydrogen-rich gas from a carbon monoxide-containing gas using a nickel and / or cobalt and molybdenum-containing catalyst. |
US4389335A (en) * | 1981-04-14 | 1983-06-21 | United Catalysts Inc. | Catalyst for carbon monoxide conversion in sour gas |
US4452854A (en) * | 1981-04-14 | 1984-06-05 | United Catalysts, Inc. | Catalyst and process for carbon monoxide conversion in sour gas |
-
0
- DE DENDAT1250792D patent/DE1250792B/en active Pending
-
1960
- 1960-11-24 GB GB4039660A patent/GB940960A/en not_active Expired
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2011055132A1 (en) | 2009-11-05 | 2011-05-12 | Johnson Matthey Plc | Water gas shift reaction process |
US8821833B2 (en) | 2009-11-05 | 2014-09-02 | Johnson Matthey Public Limited Company | Water gas shift reaction process |
US9365421B2 (en) | 2009-11-05 | 2016-06-14 | Johnson Matthey Plc | Water gas shift reaction process |
US10099922B2 (en) | 2014-01-17 | 2018-10-16 | Johnson Matthey Public Limited Company | Method of loading a vessel |
US10494255B2 (en) | 2015-10-29 | 2019-12-03 | Johnson Matthey Public Limited Company | Water gas shift process |
US10807866B2 (en) | 2015-10-29 | 2020-10-20 | Johnson Matthey Public Limited Company | Water-gas shift catalyst |
US11014811B2 (en) | 2015-10-29 | 2021-05-25 | Johnson Matthey Public Limited Company | Water gas shift process |
Also Published As
Publication number | Publication date |
---|---|
DE1250792B (en) | 1967-09-28 |
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