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GB454948A - Method of increasing yield in the catalytic synthesis of aliphatic hydrocarbons - Google Patents

Method of increasing yield in the catalytic synthesis of aliphatic hydrocarbons

Info

Publication number
GB454948A
GB454948A GB11038/35A GB1103835A GB454948A GB 454948 A GB454948 A GB 454948A GB 11038/35 A GB11038/35 A GB 11038/35A GB 1103835 A GB1103835 A GB 1103835A GB 454948 A GB454948 A GB 454948A
Authority
GB
United Kingdom
Prior art keywords
stage
reaction products
oil
hydrogen
stages
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
GB11038/35A
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.)
STUDIEN und VERWERTUNGSGESELLS
Original Assignee
STUDIEN und VERWERTUNGSGESELLS
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 STUDIEN und VERWERTUNGSGESELLS filed Critical STUDIEN und VERWERTUNGSGESELLS
Publication of GB454948A publication Critical patent/GB454948A/en
Expired legal-status Critical Current

Links

Classifications

    • AHUMAN NECESSITIES
    • A46BRUSHWARE
    • A46DMANUFACTURE OF BRUSHES
    • A46D3/00Preparing, i.e. Manufacturing brush bodies
    • A46D3/04Machines for inserting or fixing bristles in bodies
    • 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
    • C07C1/0485Set-up of reactors or accessories; Multi-step processes

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Manufacturing & Machinery (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

Aliphatic hydrocarbons containing more than one carbon atom, particularly liquid hydrocarbons, are produced by reacting mixtures of carbon monoxide with at least an equal volume of hydrogen in the presence of catalysts, at ordinary or slightly increased or reduced pressure, and at temperatures of 180--200 DEG C., the reaction being effected in at least two stages with intermediate removal of all or part of the condensible reaction products, and in the early stages conditions being so chosen that the gases are only partly converted, for example by operating at low temperatures within the range, or by using a deficiency of hydrogen or high velocities. The gas mixture may traverse a cycle with one or more contact stages and then, after removal of reaction products, be completely converted in a further stage. In examples: (1) a mixture of 2 parts H2 and 1 part CO is passed over three layers of cobalt in succession, the reaction products, oil, benzine, and water, being removed after passing each layer. The temperature is selected so that no more than one third of the CO is converted in each stage, for example, 182 DEG C. in the first stage, 187 DEG C. in the second, and 193 DEG C. in the third. Alternatively, two layers may be disposed in parallel and, after removal of reaction products, the gases passed over a third layer. Temperatures may be 184 DEG C. in the first stage and 195 DEG C. in the second; (2) two stages at 180 and 200 DEG C. are employed, light benzine and lower boiling hydrocarbons being removed intermediately as by washing with cold oil or the use of active carbon; (3) as in (2) all the reaction products being removed, the oil by washing with an oil at above 100 DEG C., the water with water, unsaturated gaseous hydrocarbons with H2SO4, and saturated gaseous hydrocarbons with active carbon; (4) insufficient hydrogen is used in the first stage and after each stage only so much hydrogen is added as will limit the conversion.
GB11038/35A 1934-04-25 1935-04-10 Method of increasing yield in the catalytic synthesis of aliphatic hydrocarbons Expired GB454948A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE454948X 1912-03-25

Publications (1)

Publication Number Publication Date
GB454948A true GB454948A (en) 1936-10-12

Family

ID=6538990

Family Applications (1)

Application Number Title Priority Date Filing Date
GB11038/35A Expired GB454948A (en) 1934-04-25 1935-04-10 Method of increasing yield in the catalytic synthesis of aliphatic hydrocarbons

Country Status (2)

Country Link
FR (1) FR454948A (en)
GB (1) GB454948A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE911609C (en) * 1938-06-08 1954-05-17 Basf Ag Process for converting carbon monoxide with hydrogen into hydrocarbons
WO2001064607A2 (en) * 2000-02-29 2001-09-07 Chevron U.S.A. Inc. Increased liquid sensitivity during fischer-tropsch synthesis by olefin incorporation
WO2004026994A1 (en) * 2002-09-19 2004-04-01 Sasol Technology (Proprietary) Limited Hydrocarbon synthesis

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE911609C (en) * 1938-06-08 1954-05-17 Basf Ag Process for converting carbon monoxide with hydrogen into hydrocarbons
WO2001064607A2 (en) * 2000-02-29 2001-09-07 Chevron U.S.A. Inc. Increased liquid sensitivity during fischer-tropsch synthesis by olefin incorporation
NL1017458C2 (en) * 2000-02-29 2002-02-19 Chevron Usa Inc Increased fluid sensitivity during Fisher-Tropsch synthesis by incorporating olefins.
WO2001064607A3 (en) * 2000-02-29 2002-03-07 Chevron Usa Inc Increased liquid sensitivity during fischer-tropsch synthesis by olefin incorporation
WO2004026994A1 (en) * 2002-09-19 2004-04-01 Sasol Technology (Proprietary) Limited Hydrocarbon synthesis

Also Published As

Publication number Publication date
FR454948A (en) 1913-07-18

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