GB693407A - Improvements in and relating to the partial hydrogenation of polyunsaturated organiccompounds - Google Patents

Improvements in and relating to the partial hydrogenation of polyunsaturated organiccompounds

Info

Publication number
GB693407A
GB693407A GB18446/51A GB1844651A GB693407A GB 693407 A GB693407 A GB 693407A GB 18446/51 A GB18446/51 A GB 18446/51A GB 1844651 A GB1844651 A GB 1844651A GB 693407 A GB693407 A GB 693407A
Authority
GB
United Kingdom
Prior art keywords
alumina
hydrogen
catalyst
compounds
silica
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
GB18446/51A
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.)
Bataafsche Petroleum Maatschappij NV
Original Assignee
Bataafsche Petroleum Maatschappij NV
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 Bataafsche Petroleum Maatschappij NV filed Critical Bataafsche Petroleum Maatschappij NV
Publication of GB693407A publication Critical patent/GB693407A/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
    • B01J27/00Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/02Sulfur, selenium or tellurium; Compounds thereof
    • B01J27/04Sulfides
    • B01J27/047Sulfides with chromium, molybdenum, tungsten or polonium
    • B01J27/051Molybdenum
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C5/00Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
    • C07C5/02Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation
    • C07C5/03Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by hydrogenation of non-aromatic carbon-to-carbon double bonds
    • C07C5/05Partial hydrogenation
    • 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
    • C07C2527/02Sulfur, selenium or tellurium; Compounds thereof
    • C07C2527/04Sulfides
    • C07C2527/047Sulfides with chromium, molybdenum, tungsten or polonium
    • C07C2527/051Molybdenum

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Catalysts (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

Unsaturated organic compounds are produced by reacting a polyunsaturated organic compound, i.e. an organic compound with a plurality of double or triple bonds between carbon atoms, at least one such double or triple bond being other than a double bond in an aromatic ring and in which none of the carbon atoms between the said double or triple bonds is attached to four carbon atoms, with hydrogen at elevated temperature in the presence of a molybdenum sulphide catalyst formed by reduction of a higher molybdenum sulphide. Preferably a support or carrier for the molybdenum sulphide catalyst is used, e.g. alumina, silica gel, pumice, diatomite, activated charcoal, activated clays and silica alumina complexes. Promoters for the alumina, e.g. silica, may be used and the alumina may be treated with an acid or acid salt. Preferably the selective hydrogenation of the unsaturated compounds is carried out in the liquid phase and may be carried out at atmospheric or superatmospheric pressure. The process may be performed at 100-200 DEG C. and preferably excess hydrogen is used. In the examples: (a) limonene, (b) 1,5-hexadiene, (c) myrcene, (d) 1,3-cyclohexadiene are hydrogenated to give unsaturated products containing only one double bond. Other polyolefinic hydrocarbons which may be reduced to the mono-olefins are, for example, the hexadienes, isoprene, piperylene, cyclohexadiene, methyl cyclohexadiene, dipentene and terpinene. Compounds having an acetylenic and an olefinic group, e.g. vinyl acetylene, may also be reduced to the mono-olefin. Polyolefinic acids, alcohols, esters, ethers, ketones, aldehydes, amines, nitro compounds, halides, sulphides and mercaptans may also be reduced to the corresponding mono-olefinic compounds, e.g. sorbic acid may be converted to 3-hexenoic acid, geraniol to the corresponding decylenol and phorone to isobutenyl isobutyl ketone. Further examples of the process are the reduction of styrene to ethyl benzene, a -propenyl benzene to propyl benzene, indene to indane and vinyl thiophene to ethyl thiophene. Specification 589,915 is referred to.ALSO:A catalyst for use in the production of unsaturated organic compounds by reacting a poly-unsaturated compound with hydrogen consists of molybdenum sulphide formed by the reduction of a higher molybdenum sulphide. Preferably a support or carrier, e.g. alumina, for the catalyst is used. A promoter for the alumina, e.g. silica is advantageous. Other carriers which may be used are silica gel, pumice, diatomite, activated charcoal and activated acid-treated clays. The preferred catalysts are prepared by reducing the initially produced higher sulphides of molybdenum to the disulphide. The higher sulphide may be reduced with hydrogen or decomposed by heating an in inert atmosphere. In the examples the catalyst is prepared by impregnating an alumina carrier containing about 5 per cent of silica with ammonium molybdate solution. The mixture is dried and ground, treated with hydrogen sulphide and reduced with hydrogen in a fluidized fixed-bed treater. Specification 589,915 is referred to.
GB18446/51A 1950-08-05 1951-08-03 Improvements in and relating to the partial hydrogenation of polyunsaturated organiccompounds Expired GB693407A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US693407XA 1950-08-05 1950-08-05

Publications (1)

Publication Number Publication Date
GB693407A true GB693407A (en) 1953-07-01

Family

ID=22088314

Family Applications (1)

Application Number Title Priority Date Filing Date
GB18446/51A Expired GB693407A (en) 1950-08-05 1951-08-03 Improvements in and relating to the partial hydrogenation of polyunsaturated organiccompounds

Country Status (1)

Country Link
GB (1) GB693407A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20220154092A1 (en) * 2011-04-13 2022-05-19 Amyris, Inc. Olefins and methods for making the same

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20220154092A1 (en) * 2011-04-13 2022-05-19 Amyris, Inc. Olefins and methods for making the same
US11802100B2 (en) * 2011-04-13 2023-10-31 Amyris, Inc. Olefins and methods for making the same

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