GB494236A - Improvements in or relating to the manufacture of adiponitrile - Google Patents
Improvements in or relating to the manufacture of adiponitrileInfo
- Publication number
- GB494236A GB494236A GB11448/37A GB1144837A GB494236A GB 494236 A GB494236 A GB 494236A GB 11448/37 A GB11448/37 A GB 11448/37A GB 1144837 A GB1144837 A GB 1144837A GB 494236 A GB494236 A GB 494236A
- Authority
- GB
- United Kingdom
- Prior art keywords
- ammonia
- acid
- catalyst
- adipic acid
- adipamide
- 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
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C255/00—Carboxylic acid nitriles
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Adiponitrile is obtained by passing a gaseous mixture of ammonia and adipic acid, or a derivative thereof which will react with ammonia to form adipamide, over a dehydration catalyst at a temperature between 320-400 DEG C. and at such a rate that the time of contact of the reactants with the catalyst is between 1 and 10 seconds, preferably 5 seconds. For example, a stream of ammonia is passed at a measured rate through a preheater 2 at about 500 DEG C. and into a vaporizing chamber 5 maintained at about 325-350 DEG C. Adipic acid, molten, powdered or in solution, is fed in through inlet 6 and evaporated by the ammonia stream. The mixture is then swept over into the catalyst chamber 10 through a heated transfer line 8. This chamber is maintained at 325-350 DEG C. The <PICT:0494236/IV/1> products are passed through cooling coil 13 and into separators 14. The oil layers are removed through outlets 15 and distilled to obtain pure adiponitrile. The aqueous layers are extracted to recover dissolved nitrile. Ammonia-acid molecular ratios of 4 : 1 to 24 : 1, preferably 6 : 1 to 16 : 1, are employed. Suitable catalysts are selected from the oxides and salts of elements of the 4th, 5th, 6th, 7th, and 8th groups, e.g. the dehydrating oxides of aluminium, silicon, tungsten, titanium, or molybdenum, preferably in the form of hard non-porous gels. Phosphoric, phosphotungstic and phosphomolybdic acids may also be used, preferably on supports, e.g. pumice, silica gel or kieselguhr. Other catalysts or promoters may be added, and spent catalysts may be revived by treatment with oxygen-containing gases. The preferred catalyst is silica gel. The apparatus should preferably be made of or lined with nickel, aluminium or its alloys, stainless steel containing molybdenum or copper-silicon-manganese alloys. A thin layer of carbonaceous material deposited on the metallic surface minimizes corrosion and adverse effects on the reaction. Other derivatives of adipic acid which may be used include adipamide, adipimide, adipic esters, o -cyanovaleric acid, adipamic acid and o -cyanovaleramide. Ordinary, increased or reduced pressure may be used. Examples describe the reaction between ammonia and adipic acid or adipamide, using ammonia-acid ratios of 16 : 1 and 8 : 1 and a silica gel catalyst and contact times of 5, 3,2, and 5,9 seconds. The product contains also cyclopentanone and tarry residue.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US494236XA | 1936-04-21 | 1936-04-21 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB494236A true GB494236A (en) | 1938-10-21 |
Family
ID=21959753
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB11448/37A Expired GB494236A (en) | 1936-04-21 | 1937-04-21 | Improvements in or relating to the manufacture of adiponitrile |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB494236A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109265367A (en) * | 2018-10-30 | 2019-01-25 | 重庆中平紫光科技发展有限公司 | A kind of method of stably catalyzed system and Adiponitrile |
US10429427B2 (en) | 2010-08-11 | 2019-10-01 | Danfoss Power Solutions Gmbh & Co. Ohg | Method and device for determining the state of an electrically controlled valve |
CN111054436A (en) * | 2019-12-16 | 2020-04-24 | 中国科学院大连化学物理研究所 | Application of plasma modified phosphotungstic heteropoly acid in synthesis of adiponitrile from adipic acid |
US11149001B2 (en) * | 2016-12-06 | 2021-10-19 | Toray Industries, Inc. | Method for producing ϵ-caprolactam |
-
1937
- 1937-04-21 GB GB11448/37A patent/GB494236A/en not_active Expired
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US10429427B2 (en) | 2010-08-11 | 2019-10-01 | Danfoss Power Solutions Gmbh & Co. Ohg | Method and device for determining the state of an electrically controlled valve |
US11149001B2 (en) * | 2016-12-06 | 2021-10-19 | Toray Industries, Inc. | Method for producing ϵ-caprolactam |
CN109265367A (en) * | 2018-10-30 | 2019-01-25 | 重庆中平紫光科技发展有限公司 | A kind of method of stably catalyzed system and Adiponitrile |
CN109265367B (en) * | 2018-10-30 | 2021-09-24 | 河南中平紫光科技有限公司 | Method for stabilizing catalytic system and synthesizing adiponitrile |
CN111054436A (en) * | 2019-12-16 | 2020-04-24 | 中国科学院大连化学物理研究所 | Application of plasma modified phosphotungstic heteropoly acid in synthesis of adiponitrile from adipic acid |
CN111054436B (en) * | 2019-12-16 | 2021-04-23 | 中国科学院大连化学物理研究所 | Application of plasma modified phosphotungstic heteropoly acid in synthesis of adiponitrile from adipic acid |
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