GB659315A - Improvements in or relating to catalytic conversion of carbon monoxide with hydrogen - Google Patents
Improvements in or relating to catalytic conversion of carbon monoxide with hydrogenInfo
- Publication number
- GB659315A GB659315A GB1881/49A GB188149A GB659315A GB 659315 A GB659315 A GB 659315A GB 1881/49 A GB1881/49 A GB 1881/49A GB 188149 A GB188149 A GB 188149A GB 659315 A GB659315 A GB 659315A
- Authority
- GB
- United Kingdom
- Prior art keywords
- reduced
- reduction
- catalysts
- per cent
- 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
- B01J23/76—Catalysts 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
- B01J23/78—Catalysts 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
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Catalysts (AREA)
Abstract
The synthesis of hydrocarbons and oxygenated compounds from CO and H2 is effected with a catalyst comprising an iron oxide reduced to between 5 and 50, preferably 10-25, per cent of complete reduction and containing between 0.5 and 5 per cent of an alkali metal promoter. This reduction corresponds to an oxygen content of the catalyst of about 26-14, preferably 25-21 per cent. Fluidized operation is preferred, using catalysts of about 20-200, preferably 30-100 microns particle size. Iron oxide may be ground to about 30 microns or less, reduced with hydrogen, and then sintered to form particles of desired size or the oxide may be graded into different sizes which are separately reduced. Data are given showing that the catalysts have an activity equivalent to that of conventional catalysts of a higher degree of reduction while carbonization is less. In examples, pyrites ash or a fused mixture of natural and synthetic magnetite, promoted with potassium carbonate or nitrate, is reduced with hydrogen at 850-930 DEG F. for different times to yield catalysts of the desired degree of reduction.ALSO:A catalyst for the synthesis of hydrocarbons and oxygenated compounds from CO and H2 comprises an iron oxide reduced to between 5 and 50, preferably 10-25 per cent, of complete reduction and containing between 0.5 and 5 per cent of an alkali metal promoter. This reduction corresponds to an oxygen content of the catalyst of about 26-14, preferably 25-21 per cent. Fluidized operation is preferred, using catalysts of about 20-200, preferably 30-100 microns particle size. Iron oxide may be ground to about 30 microns or less, reduced with hydrogen, and then sintered to form particles of desired size or the oxide may be graded into different sizes which are separately reduced. Data are given showing that the catalyst have an activity equivalent to that of conventional catalysts of a higher degree of reduction while carbonization is less. In examples, pyrities ash or a fused mixture of natural and synthetic magnetite, promoted with potassium carbonate or nitrate, is reduced with hydrogen at 850-930 DEG F. for different times to yield catalysts of the desired degree of reduction.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US659315XA | 1948-05-12 | 1948-05-12 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB659315A true GB659315A (en) | 1951-10-24 |
Family
ID=22066108
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB1881/49A Expired GB659315A (en) | 1948-05-12 | 1949-01-24 | Improvements in or relating to catalytic conversion of carbon monoxide with hydrogen |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB659315A (en) |
-
1949
- 1949-01-24 GB GB1881/49A patent/GB659315A/en not_active Expired
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US2686195A (en) | Hydrocarbon synthesis | |
GB1472118A (en) | Molybdenum and ferromolybdenum production | |
CA2294091C (en) | Process for the preparation of high activity carbon monoxide hydrogenation catalysts; the catalyst compositions, and their use | |
GB1437750A (en) | Hot metal gasification of coal | |
US4607055A (en) | Aliphatic alcohol production | |
GB649464A (en) | Hydrogenation catalysts | |
US2476920A (en) | Catalyst for reduction of oxides of carbon with hydrogen | |
US2601121A (en) | Preconditioning hydrocarbon synthesis catalyst and removing fines therefrom | |
GB659315A (en) | Improvements in or relating to catalytic conversion of carbon monoxide with hydrogen | |
US2707706A (en) | Method of reducing catalyst | |
US2541657A (en) | Method of making commercial mixtures of hydrogen and carbon monoxide | |
US2509869A (en) | Hydrocarbon synthesis | |
US2636011A (en) | Fischer-tropsch catalyst preparation and regeneration | |
GB584790A (en) | Improved process for the production of chlorine | |
GB1461287A (en) | Fuel gas production | |
US2565977A (en) | Process for the preparation of catalysts for the conversion of carbon oxides with hydrogen | |
US2682552A (en) | Hydrocarbon synthesis process | |
GB678941A (en) | Improvements in or relating to hydrocarbon synthesis | |
US2513994A (en) | Production of synthesis gas | |
US2762828A (en) | Method for treatment of hydrocarbon synthesis catalyst | |
US2567295A (en) | Method for the synthesis of hydrocarbons with a reduced gamma iron oxide catalyst | |
GB647489A (en) | Improvements in or relating to the production of hydrocarbons and oxygenated organiccompounds | |
GB652477A (en) | Improvements in or relating to hydrocarbon synthesis | |
US2580116A (en) | Synthesis of organic compounds | |
US1866246A (en) | Process of producing hydrogen |