GB894592A - Process for the recovery of tungstic acid catalyst - Google Patents

Process for the recovery of tungstic acid catalyst

Info

Publication number
GB894592A
GB894592A GB31432/58A GB3143258A GB894592A GB 894592 A GB894592 A GB 894592A GB 31432/58 A GB31432/58 A GB 31432/58A GB 3143258 A GB3143258 A GB 3143258A GB 894592 A GB894592 A GB 894592A
Authority
GB
United Kingdom
Prior art keywords
solution
tungstic acid
acid
hydrogen peroxide
aqueous
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
GB31432/58A
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.)
Columbia Southern Chemical Corp
Original Assignee
Columbia Southern Chemical Corp
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 Columbia Southern Chemical Corp filed Critical Columbia Southern Chemical Corp
Publication of GB894592A publication Critical patent/GB894592A/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07BGENERAL METHODS OF ORGANIC CHEMISTRY; APPARATUS THEREFOR
    • C07B35/00Reactions without formation or introduction of functional groups containing hetero atoms, involving a change in the type of bonding between two carbon atoms already directly linked
    • C07B35/04Dehydrogenation
    • 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
    • C07C29/48Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by oxidation reactions with formation of hydroxy groups

Landscapes

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

Abstract

Tungsten values are recovered from tungstic acid catalyst used in the oxidation of olefinically unsaturated compounds by bringing aqueous solutions of tungstic acid, generally rendered alkaline by the addition of sodium hydroxide and containing from 0,05 to 5% by weight of tungstic acid, into contact with an ion-exchange resin and thereafter eluting tungstic acid values with an aqueous solution of alkali metal chloride and finally precipitating the tungstic acid catalyst values from the eluted solution. The elution is preferably effected with 2-30% strength sodium chloride at temperatures preferably between 15 DEG and 60 DEG C. The sodium tungstate solutions so obtained are then rendered acidic, to a pH preferably between 2-6,5, by the addition of an inorganic or organic acid, thereby precipitating the tungstic acid, which may be separated by filtration or other means. If the organic oxidation reaction involves the use of aqueous hydrogen peroxide, the initial tungstic acid is in the form of pertungstic acid. Specified ion-exchange resins are those obtained by the sulphonation of polystyrene and co-polymers thereof with vinyl benzene, sulphonated phenol formaldehyde resins, amino nitrogenous resins derived from styrene and its co-polymers and cross linked polymers of a glycidol ester of acrylic acid or an alpha-substituted acrylic acid, which cross-linked polymers have been treated with ammonia or a primary or secondary amine. The resins are preferably used in their hydroxyl form. The aqueous medium contacted with the ion exchange resin may contain unreacted olefinically unsaturated material, the oxidized reaction products, hydrogen peroxide and reaction by-products. According to an example, "Amberlite" (Registered Trade Mark) was converted to the hydroxyl form by passing sodium hydroxide solution therethrough and thereafter an aqueous tungstic acid catalyst solution, which had been adjusted to a pH between 9 and 10 by the addition of sodium hydroxide, was passed through at 25 DEG C. Elution with a 4% sodium chloride solution produced a sodium tungstate solution which was treated with concentrated hydrochloric acid to precipitate the tungstic acid, followed by heating at 80 DEG -100 DEG C. After washing with water and dilute hydrochloric acid, tungstic acid values were dissolved in hydrogen peroxide solution to form a catalyst for oxidation of olefinically unsaturated organic compounds. Reference is made to Specification 626,882 which describes the process for recovering chromium, molybdenum, tungsten or uranium in the form of oxygen-containing complex anions from a solution by contacting it with an ion-exchange resin and eluting with a solution of an acid, salt or base.ALSO:Allyl alcohol is oxidised to glycerol in the presence of a tungstic acid solution in hydrogen peroxide. A hydrogen peroxide solution containing 2.14 milimoles of H2WO4 was mixed with allyl alcohol at 70 DEG C. and further hydrogen peroxide added. Sodium hydroxide was added, the unreacted allyl alcohol distilled off and the glycerol recovered by fractional distillation. Specification 626,882 [Group III] is referred to.
GB31432/58A 1957-10-03 1958-10-02 Process for the recovery of tungstic acid catalyst Expired GB894592A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US894592XA 1957-10-03 1957-10-03

Publications (1)

Publication Number Publication Date
GB894592A true GB894592A (en) 1962-04-26

Family

ID=22217762

Family Applications (1)

Application Number Title Priority Date Filing Date
GB31432/58A Expired GB894592A (en) 1957-10-03 1958-10-02 Process for the recovery of tungstic acid catalyst

Country Status (1)

Country Link
GB (1) GB894592A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007111691A (en) * 2005-09-21 2007-05-10 Sumitomo Chemical Co Ltd Method for recovering tungsten
EP1942094A1 (en) * 2005-09-21 2008-07-09 Sumitomo Chemical Company, Limited Method for recovering tungsten
RU2484900C2 (en) * 2007-12-13 2013-06-20 Бп П.Л.К. Method of extracting catalyst
EP3263557A1 (en) * 2016-06-30 2018-01-03 Evonik Degussa GmbH Method for reactivation of a homogeneous oxidation catalyst

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007111691A (en) * 2005-09-21 2007-05-10 Sumitomo Chemical Co Ltd Method for recovering tungsten
EP1942094A1 (en) * 2005-09-21 2008-07-09 Sumitomo Chemical Company, Limited Method for recovering tungsten
EP1942094A4 (en) * 2005-09-21 2010-11-24 Sumitomo Chemical Co Method for recovering tungsten
US7993614B2 (en) 2005-09-21 2011-08-09 Sumitomo Chemical Company, Limited Method for recovering tungsten
RU2484900C2 (en) * 2007-12-13 2013-06-20 Бп П.Л.К. Method of extracting catalyst
EP3263557A1 (en) * 2016-06-30 2018-01-03 Evonik Degussa GmbH Method for reactivation of a homogeneous oxidation catalyst
WO2018002114A1 (en) * 2016-06-30 2018-01-04 Evonik Degussa Gmbh Method for reactivating a homogeneous oxidation catalyst
US10994270B2 (en) 2016-06-30 2021-05-04 Evonik Operations Gmbh Method for reactivation of a homogeneous oxidation catalyst

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