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 hydrogen

Info

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
Application number
GB1881/49A
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.)
Standard Oil Development Co
Original Assignee
Standard Oil Development Co
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Standard Oil Development Co filed Critical Standard Oil Development Co
Publication of GB659315A publication Critical patent/GB659315A/en
Expired legal-status Critical Current

Links

Classifications

    • 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

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.
GB1881/49A 1948-05-12 1949-01-24 Improvements in or relating to catalytic conversion of carbon monoxide with hydrogen Expired GB659315A (en)

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)

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