GB894592A - Process for the recovery of tungstic acid catalyst - Google Patents
Process for the recovery of tungstic acid catalystInfo
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07B—GENERAL METHODS OF ORGANIC CHEMISTRY; APPARATUS THEREFOR
- C07B35/00—Reactions 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
- C07B35/04—Dehydrogenation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/16—Catalysts 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
- B01J23/24—Chromium, molybdenum or tungsten
- B01J23/30—Tungsten
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/48—Preparation 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.
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)
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 |
-
1958
- 1958-10-02 GB GB31432/58A patent/GB894592A/en not_active Expired
Cited By (8)
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 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CA2236126C (en) | Process for producing alkylene glycol | |
GB954435A (en) | Anion exchange resins for the recovery of gold and silver from gold and silver bearing aqueous cyanide liquors | |
ES2040141T3 (en) | PROCEDURE FOR PREPARING 1,3-PROPANODIOL. | |
GB1506534A (en) | Process for preparing mannitol from glucose | |
GB894592A (en) | Process for the recovery of tungstic acid catalyst | |
GB406345A (en) | Improvements in or relating to the production of formic acid | |
GB1068888A (en) | Method of making di- and tri methylolalkanoic acids | |
CA1147897A (en) | Process for the chloromethylation of polymers for the production of anionic exchange resins | |
GB897226A (en) | Production of unsaturated aliphatic nitriles | |
US3514490A (en) | Process for the production of diphenols | |
US4401631A (en) | Process for the recovery of molybdenum from mixtures of molybdenum compounds with other metallic compounds | |
GB1018144A (en) | A process for the recovery of tungstic catalysts | |
GB1463050A (en) | Process for the manufacture of bromine | |
GB2031906A (en) | Oxidation-resistant ion exchange resins | |
CA1181951A (en) | Recovery of molybdenum from spent catalyst solutions from hydroperoxide epoxidations | |
US4992600A (en) | Process for the oxidation of benzene to phenol | |
GB1339788A (en) | Method for converting anion exchange resins from the monovalent anion to the hydroxide form | |
US3422148A (en) | Process for the continuous manufacture of methyl isopropenyl ketone in the liquid phase | |
GB1572316A (en) | Process for preparing 5-(4-hydroxyphenyl)hydantion | |
US3600447A (en) | Preparation of hydroxylated aromatic compounds | |
US3243462A (en) | Process for preparing dimethylhydroxylamine | |
US2709710A (en) | Method for recovering para-hydroxybenzaldehyde | |
CA1141364A (en) | Oxidation of organic substances using a ruthenate catalyst | |
GB1002269A (en) | Process for the manufacture of methylal | |
GB956403A (en) | Recovery of copper and vanadium from aqueous streams by ion-exchange |