GB767409A - Improvements in or relating to the production of ketones - Google Patents

Improvements in or relating to the production of ketones

Info

Publication number
GB767409A
GB767409A GB3570553A GB3570553A GB767409A GB 767409 A GB767409 A GB 767409A GB 3570553 A GB3570553 A GB 3570553A GB 3570553 A GB3570553 A GB 3570553A GB 767409 A GB767409 A GB 767409A
Authority
GB
United Kingdom
Prior art keywords
alumina
water
catalyst
per cent
platinum
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
GB3570553A
Inventor
Warran Wills Elliott
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.)
Imperial Chemical Industries Ltd
Original Assignee
Imperial Chemical Industries Ltd
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 Imperial Chemical Industries Ltd filed Critical Imperial Chemical Industries Ltd
Priority to GB3570553A priority Critical patent/GB767409A/en
Publication of GB767409A publication Critical patent/GB767409A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C49/00Ketones; Ketenes; Dimeric ketenes; Ketonic chelates
    • C07C49/04Saturated compounds containing keto groups bound to acyclic carbon atoms
    • C07C49/08Acetone

Abstract

Olefines containing at least 3 carbon atoms are converted into ketones containing the corresponding number of carbon atoms by reacting the olefines with water wholly or partly in the vapour phase under a pressure of 5 to 1000 atmos. gauge and at 200 DEG to 400 DEG C., in the presence of a solid catalyst comprising at most 10 per cent by weight of a hydrogenating metal from Group IB or VIII of the Periodic Table, supported on a substantially water-insoluble solid hydration catalyst comprising an electronic insulator or semi-conductor material, the terms "insulator" and "semi-conductor" being used in the senses given in the Journal of the Chemical Society, 1950, at page 242 et seq. Preferred hydrogenating metals are platinum and palladium; nickel and copper are also mentioned. The supports for the metal catalysts may be gamma - alumina, alumina - silica, alumina-zirconia, thoria, cadmium and zinc phosphates and the crystalline phosphates of the alkaline earth metals, all of which are best suited for use in the absence of liquid water, and tungsta, molybdena and titania. In general, water : olefine ratios of 1 : 2 to 20 : 1 are employed. Temperatures preferably do not exceed 350 DEG C. In an example, propylene is reacted with water at 270 DEG C. under 250 atmos. gauge pressure using a pelleted catalyst of 5 per cent platinum on tungstic acid yielding acetone together with some isopropanol which is recycled with unchanged propylene. Another catalyst mentioned is 2 per cent Pt on gammaalumina or tungstic acid. Other starting materials mentioned are aliphatic olefines having up to 6 carbon atoms, e.g. butene-1, and cycloaliphatic ketones such as cyclopentene and cyclohexene. Specification 335,551, [Class 2 (iii)], is referred to. According to the Provisional Specification, elevated temperatures and pressures generally may be used.ALSO:Solid catalysts for use in converting olefines into ketones of the same carbon content by reaction with water (see Group IV(b)) comprise at most 10 per cent by weight of a hydrogenating metal from Group I(b) or VIII of the Periodic Table supported on a substantially water-insoluble solid hydration catalyst comprising an electronic insulator or semi-conductor material, the terms "insulator" and "semi-conductor" being used in the senses given in the Journal of the Chemical Society, 1950, at page 242 et seq. Specified hydrogenating metals are platinum, palladium, nickel and copper. The supports for the metals may be gamma-alumina, aluminasilica, alumina-zirconia, thoria, cadmium and zinc phosphates, the crystalline phosphates of the alkaline earth metals, tungsta, molybdena and titania. Specified catalysts are platinum (2 or 5 per cent) on tungstic acid as gamma-alumina. A suitable catalyst may be prepared by impregnating tungstic acid powder with chloroplatinic acid solution, pelleting at 40 or more tons/sq. in. pressure and then igniting in air or hydrogen at 300-400 DEG C. Specification 335,551 [Class 1(i)] is referred to.
GB3570553A 1953-12-23 1953-12-23 Improvements in or relating to the production of ketones Expired GB767409A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB3570553A GB767409A (en) 1953-12-23 1953-12-23 Improvements in or relating to the production of ketones

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB3570553A GB767409A (en) 1953-12-23 1953-12-23 Improvements in or relating to the production of ketones

Publications (1)

Publication Number Publication Date
GB767409A true GB767409A (en) 1957-02-06

Family

ID=10380660

Family Applications (1)

Application Number Title Priority Date Filing Date
GB3570553A Expired GB767409A (en) 1953-12-23 1953-12-23 Improvements in or relating to the production of ketones

Country Status (1)

Country Link
GB (1) GB767409A (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3080426A (en) * 1959-01-29 1963-03-05 Exxon Research Engineering Co Oxidation of alcohols
US3080425A (en) * 1957-06-28 1963-03-05 Consortium Elektrochem Ind Process for the production of aldehydes and ketones compounds
US3086994A (en) * 1957-08-01 1963-04-23 Consortium Elektrochem Ind Process for the production of aldehydes and ketones
US3119875A (en) * 1957-10-31 1964-01-28 Hoechst Ag Process for oxidizing olefins to aldehydes and ketones
US3121673A (en) * 1957-07-10 1964-02-18 Hoechst Ag Process of regenerating a liquid catalyst
US3122586A (en) * 1957-08-01 1964-02-25 Consortium Elektrochem Ind Process for oxidizing olefins to aldehydes and ketones
US3131223A (en) * 1957-01-04 1964-04-28 Consortium Elektrochem Ind Process for the production of aldehydes and ketones
US3153083A (en) * 1957-09-06 1964-10-13 Consortium Elektrochem Ind Process for the production of carbonyl groups in organic compounds
US3154586A (en) * 1957-07-10 1964-10-27 Hoechst Ag Process for oxidizing olefins to aldehydes and ketones

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3131223A (en) * 1957-01-04 1964-04-28 Consortium Elektrochem Ind Process for the production of aldehydes and ketones
US3080425A (en) * 1957-06-28 1963-03-05 Consortium Elektrochem Ind Process for the production of aldehydes and ketones compounds
US3121673A (en) * 1957-07-10 1964-02-18 Hoechst Ag Process of regenerating a liquid catalyst
US3154586A (en) * 1957-07-10 1964-10-27 Hoechst Ag Process for oxidizing olefins to aldehydes and ketones
US3086994A (en) * 1957-08-01 1963-04-23 Consortium Elektrochem Ind Process for the production of aldehydes and ketones
US3122586A (en) * 1957-08-01 1964-02-25 Consortium Elektrochem Ind Process for oxidizing olefins to aldehydes and ketones
US3153083A (en) * 1957-09-06 1964-10-13 Consortium Elektrochem Ind Process for the production of carbonyl groups in organic compounds
US3119875A (en) * 1957-10-31 1964-01-28 Hoechst Ag Process for oxidizing olefins to aldehydes and ketones
US3080426A (en) * 1959-01-29 1963-03-05 Exxon Research Engineering Co Oxidation of alcohols

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