GB678941A - Improvements in or relating to hydrocarbon synthesis - Google Patents

Improvements in or relating to hydrocarbon synthesis

Info

Publication number
GB678941A
GB678941A GB29231/49A GB2923149A GB678941A GB 678941 A GB678941 A GB 678941A GB 29231/49 A GB29231/49 A GB 29231/49A GB 2923149 A GB2923149 A GB 2923149A GB 678941 A GB678941 A GB 678941A
Authority
GB
United Kingdom
Prior art keywords
iron
reduction
per cent
prepared
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
GB29231/49A
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 GB678941A publication Critical patent/GB678941A/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
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/16Reducing
    • B01J37/18Reducing with gases containing free hydrogen
    • 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
    • B01J27/22Carbides
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C1/00Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
    • C07C1/02Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of a carbon
    • C07C1/04Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon from oxides of a carbon from carbon monoxide with hydrogen
    • C07C1/0425Catalysts; their physical properties
    • C07C1/0445Preparation; Activation
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2523/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
    • C07C2523/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of the iron group metals or copper
    • C07C2523/74Iron group metals
    • C07C2523/745Iron
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2527/00Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • C07C2527/20Carbon compounds
    • C07C2527/22Carbides

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Catalysts (AREA)

Abstract

Hydrocarbons and oxygenated derivatives are prepared by contacting a gas mixture containing H2 and CO in a ratio of less than 2 : 1, under synthesis conditions, with a fluidized iron catalyst prepared by subjecting fresh iron oxide to reduction with hydrogen at 900-1500 DEG F., and subjecting the reduced product, before use in the synthesis, to an activating or precarbiding treatment with a mixture containing H2 and CO in a ratio of 2-8 : 1 at 500-700 DEG F. The final activating treatment may be continued until 50-55 per cent by weight of iron is converted to iron carbide. The reduction with hydrogen at 900-1500 DEG F. may be followed by a further reduction at 500-700 DEG F. Powdered iron oxide of particle size 0-200m with 50 per cent or more particles greater than 80m may be impregnated with alkali halide or carbonate and reduced at 1000-1100 DEG F. till the oxygen content of the iron is 3-10 per cent by weight. It is then activated at 500-700 DEG F. for several hours. Results of tests showing the increased resistance to oxidation and carbide retention, and reduction in carbon deposition and disintegration with catalyst prepared from pyrites ash containing sodium carbonate or potassium chloride, ammonia synthesis catalyst (fused magnetite), and mill scale are given. Specification 620,775 is referred to.ALSO:Hydrocarbons and oxygenated derivatives are prepared by contacting a gas mixture containing H2 and CO in a ratio of less than 2 : 1, under synthesis conditions, with a fluidized iron catalyst prepared by subjecting fresh iron oxide to reduction with hydrogen at 900-1500 DEG F, and subjecting the reduced product, before use in the synthesis, to an activating or precarbiding treatment with a mixture containing H2 and CO in a ratio of 2-8 : 1 at 500-700 DEG F. The final activating treatment may be continued until 50-55 per cent by weight of iron is converted to iron carbide. The reduction with hydrogen at 900-1500 DEG F may be followed by a further reduction at 500-700 DEG F. Powdered iron oxide of particle size 0-200m with 50 per cent or more particles greater than 80m may be impregnated with alkali halide or carbonate and reduced at 1000-1100 DEG F till the oxygen content of the iron is 3-10 per cent by weight. It is then activated at 500-700 DEG F for several hours. Results of tests showing the increased resistance to oxidation and carbide retention, and reduction in carbon deposition and disintegration with catalysts prepared from pyrites ash containing sodium carbonate or potassium chloride, ammonia synthesis catalyst (fused magnetite), and mill scale are given. Specification 620,775 is referred to.
GB29231/49A 1949-01-05 1949-11-15 Improvements in or relating to hydrocarbon synthesis Expired GB678941A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US678941XA 1949-01-05 1949-01-05

Publications (1)

Publication Number Publication Date
GB678941A true GB678941A (en) 1952-09-10

Family

ID=22079111

Family Applications (1)

Application Number Title Priority Date Filing Date
GB29231/49A Expired GB678941A (en) 1949-01-05 1949-11-15 Improvements in or relating to hydrocarbon synthesis

Country Status (1)

Country Link
GB (1) GB678941A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0170408A1 (en) * 1984-06-29 1986-02-05 Exxon Research And Engineering Company Iron carbide on titania surface modified with group VA oxides as Fischer-Tropsch catalysts
CN110627067A (en) * 2019-09-12 2019-12-31 大连理工大学 High-purity Fe5C2Preparation method of nano particles and application of nano particles in Fischer-Tropsch synthesis reaction

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0170408A1 (en) * 1984-06-29 1986-02-05 Exxon Research And Engineering Company Iron carbide on titania surface modified with group VA oxides as Fischer-Tropsch catalysts
CN110627067A (en) * 2019-09-12 2019-12-31 大连理工大学 High-purity Fe5C2Preparation method of nano particles and application of nano particles in Fischer-Tropsch synthesis reaction

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