GB646497A - Improvements in and relating to the production of alcohols - Google Patents

Improvements in and relating to the production of alcohols

Info

Publication number
GB646497A
GB646497A GB2445246A GB2445246A GB646497A GB 646497 A GB646497 A GB 646497A GB 2445246 A GB2445246 A GB 2445246A GB 2445246 A GB2445246 A GB 2445246A GB 646497 A GB646497 A GB 646497A
Authority
GB
United Kingdom
Prior art keywords
prepared
catalyst
water
temperature
per cent
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
GB2445246A
Inventor
Norman Levy
Robert Kay Greenhalgh
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 GB2445246A priority Critical patent/GB646497A/en
Publication of GB646497A publication Critical patent/GB646497A/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
    • B01J23/16Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J23/24Chromium, molybdenum or tungsten
    • B01J23/30Tungsten
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C29/00Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
    • C07C29/03Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by addition of hydroxy groups to unsaturated carbon-to-carbon bonds, e.g. with the aid of H2O2
    • C07C29/04Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by addition of hydroxy groups to unsaturated carbon-to-carbon bonds, e.g. with the aid of H2O2 by hydration of carbon-to-carbon double bonds

Landscapes

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

Abstract

Tertiary butanol is prepared by reacting isobutene and water at elevated pressure and at a temperature within the range of from 160 DEG to 220 DEG C. in the presence of an unsupported pelleted catalyst consisting of the blue oxide of tungsten having a formula approximating to W2O5 and prepared by reducing a hydrated tungsten trioxide or ammonium paratungstate at elevated temperatures. Secondary butanol is prepared in the same manner from butene-1 and/or butene-2 but at a temperature in the range of from 230 DEG to 270 DEG C. Water-to-olefine molecular ratios may vary from 1 : 1 up to as high as 20 : 1, the higher ratios being preferred. The process may be operated continuously, any unreacted olefine being recycled. A mixture of isobutene and either or both n-butenes and water may be passed over the catalyst at a temperature within the range of from 160 DEG to 220 DEG C., the resulting t-butanol separated from the reaction mixture and the residue, with more water, if necessary or desired, then passed over a second blue oxide of tungsten catalyst at a temperature in the higher range to form secondary butanol. Suitable catalysts are prepared by pelleting a mixture of powdered tungstic acid and 2 per cent graphite which is then reduced, for example, by treatment at an elevated temperature with hydrogen, carbon monoxide, mixtures containing these gases, or with a lower aliphatic alcohol, or it may be placed in the reaction vessel and treated at elevated temperature with the reactants; the tungstic acid may be replaced by ammonium para-tungstate. Examples describe the conversion of isobutene and butene-2 into the corresponding alcohols at 250 atmospheres pressure, the catalyst used being prepared by pelleting tungstic acid containing 2 per cent graphite and treating with ethanol for 3 hours at 250 DEG C., and then similarly treating with water. Specification 622,937 is referred to. According to the Provisional Specification the catalyst may be prepared by the reduction of WO3 containing 2 per cent of graphite.ALSO:Blue oxide of tungsten, for use as catalyst in the hydration of butenes to sec.- and tertiary-butanols, is prepared in unsupported pelleted form by reducing ammonium paratungstate or a hydrated tungsten trioxide, or WO3 according to the Provisional Specification, at elevated temperature. Hydrogen, carbon monoxide, or mixtures containing these gases, or lower aliphatic alcohols, may be used for the reduction; alternatively the pellets may be reduced in the reaction vessel by means of the reactants themselves. In an example, hydrated tungsten trioxide containing 2 per cent graphite is pelleted and then treated at 250 DEG C. with ethanol for 3 hours and then with water for three hours.
GB2445246A 1946-08-16 1946-08-16 Improvements in and relating to the production of alcohols Expired GB646497A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB2445246A GB646497A (en) 1946-08-16 1946-08-16 Improvements in and relating to the production of alcohols

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB2445246A GB646497A (en) 1946-08-16 1946-08-16 Improvements in and relating to the production of alcohols

Publications (1)

Publication Number Publication Date
GB646497A true GB646497A (en) 1950-11-22

Family

ID=10211928

Family Applications (1)

Application Number Title Priority Date Filing Date
GB2445246A Expired GB646497A (en) 1946-08-16 1946-08-16 Improvements in and relating to the production of alcohols

Country Status (1)

Country Link
GB (1) GB646497A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8558036B2 (en) 2010-11-15 2013-10-15 Saudi Arabian Oil Company Dual phase catalysts system for mixed olefin hydrations

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8558036B2 (en) 2010-11-15 2013-10-15 Saudi Arabian Oil Company Dual phase catalysts system for mixed olefin hydrations
US8865951B2 (en) 2010-11-15 2014-10-21 Saudi Arabian Oil Company Dual phase catalysts system for mixed olefin hydrations
US9056315B2 (en) 2010-11-15 2015-06-16 Saudi Arabian Oil Company Dual phase catalysts system for mixed olefin hydrations

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