GB465157A - Improvements in or relating to the manufacture of methane - Google Patents
Improvements in or relating to the manufacture of methaneInfo
- Publication number
- GB465157A GB465157A GB2982135A GB2982135A GB465157A GB 465157 A GB465157 A GB 465157A GB 2982135 A GB2982135 A GB 2982135A GB 2982135 A GB2982135 A GB 2982135A GB 465157 A GB465157 A GB 465157A
- Authority
- GB
- United Kingdom
- Prior art keywords
- methane
- oxide
- alumina
- catalyst
- hydrogen
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/74—Iron group metals
- B01J23/755—Nickel
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Catalysts (AREA)
Abstract
For the production of methane from carbon monoxide and hydrogen a catalyst is prepared by co-precipitating in the cold nickel oxide and alumina, shaping the precipitate, and reducing the nickel oxide. The alumina may be partly or wholly replaced by another dehydrating or dehydrogenating oxide such as thoria, blue oxide of tungsten, titania, magnesia. The catalyst may be prepared at low temperatures as described in Specification 354,351. The methane reaction is preferably effected at 330--400 DEG C., and at atmospheric or slightly increased pressure. As reaction mixture may be used either pure gases, or mixtures such as water-gas, or coal gas enriched in carbon monoxide. The hydrogen is preferably in excess.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB2982135A GB465157A (en) | 1935-10-29 | 1935-10-29 | Improvements in or relating to the manufacture of methane |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB2982135A GB465157A (en) | 1935-10-29 | 1935-10-29 | Improvements in or relating to the manufacture of methane |
Publications (1)
Publication Number | Publication Date |
---|---|
GB465157A true GB465157A (en) | 1937-04-29 |
Family
ID=10297719
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB2982135A Expired GB465157A (en) | 1935-10-29 | 1935-10-29 | Improvements in or relating to the manufacture of methane |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB465157A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4208191A (en) * | 1978-05-30 | 1980-06-17 | The Lummus Company | Production of pipeline gas from coal |
US4273724A (en) * | 1979-07-09 | 1981-06-16 | Exxon Research & Engineering Co. | Hydrocarbon synthesis from CO and H2 using titanium promoted bulk nickel catalysts |
-
1935
- 1935-10-29 GB GB2982135A patent/GB465157A/en not_active Expired
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4208191A (en) * | 1978-05-30 | 1980-06-17 | The Lummus Company | Production of pipeline gas from coal |
US4273724A (en) * | 1979-07-09 | 1981-06-16 | Exxon Research & Engineering Co. | Hydrocarbon synthesis from CO and H2 using titanium promoted bulk nickel catalysts |
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