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公开(公告)号:JPS63135367A
公开(公告)日:1988-06-07
申请号:JP28440387
申请日:1987-11-12
Applicant: HOECHST AG
Inventor: STUEHLER HERBERT , DULLINGER KLAUS
IPC: C07C303/22 , C07C67/00 , C07C301/00 , C07C303/24 , C07C305/10
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公开(公告)号:DE3767445D1
公开(公告)日:1991-02-21
申请号:DE3767445
申请日:1987-11-03
Applicant: HOECHST AG
Inventor: STUEHLER HERBERT , DULLINGER KLAUS
IPC: C07B45/02 , C07C303/30 , C07C305/02 , C07C305/10
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公开(公告)号:AT60053T
公开(公告)日:1991-02-15
申请号:AT87116132
申请日:1987-11-03
Applicant: HOECHST AG
Inventor: STUEHLER HERBERT , DULLINGER KLAUS
IPC: C07B45/02 , C07C303/30 , C07C305/02 , C07C305/10
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公开(公告)号:NO165394C
公开(公告)日:1991-02-06
申请号:NO874853
申请日:1987-11-20
Applicant: HOECHST AG
Inventor: STUEHLER HERBERT , FISCHER KURT
IPC: C07C29/00 , C07B61/00 , C07C27/00 , C07C31/22 , C07C67/00 , C07C253/00 , C07C253/22 , C07C255/00 , C07C255/03 , C07C255/17
Abstract: Glycerides are reacted with ammonia in an amount of at least 200 liters per kilogram of glyceride per hour, at a temperature of 220 DEG to 300 DEG C., and in the presence of special catalysts. Of the product mixture which is formed and removed from the reaction with the excess ammonia, and which is composed essentially of the components water, the desired glycerol and fatty acid nitrile containing fatty acid and fatty acid amide, the latter component is returned to the reaction during the glyceride reaction. After completion of the glyceride reaction, which is indicated when the product mixture contains virtually no more glycerol, all the fatty acid nitrile containing fatty acid and fatty acid amide is further treated, in an after-reaction with a reduced amount of ammonia and at higher temperature, in order to convert the fatty acid and fatty acid amide impurities into fatty acid nitrile.
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公开(公告)号:DD262859A5
公开(公告)日:1988-12-14
申请号:DD30921487
申请日:1987-11-19
Applicant: HOECHST AG
Inventor: STUEHLER HERBERT , FISCHER KURT
IPC: C07C29/00 , C07B61/00 , C07C27/00 , C07C31/22 , C07C67/00 , C07C253/00 , C07C253/22 , C07C255/00 , C07C255/03 , C07C255/17 , C07C120/00
Abstract: Glycerides are reacted with ammonia in an amount of at least 200 liters per kilogram of glyceride per hour, at a temperature of 220 DEG to 300 DEG C., and in the presence of special catalysts. Of the product mixture which is formed and removed from the reaction with the excess ammonia, and which is composed essentially of the components water, the desired glycerol and fatty acid nitrile containing fatty acid and fatty acid amide, the latter component is returned to the reaction during the glyceride reaction. After completion of the glyceride reaction, which is indicated when the product mixture contains virtually no more glycerol, all the fatty acid nitrile containing fatty acid and fatty acid amide is further treated, in an after-reaction with a reduced amount of ammonia and at higher temperature, in order to convert the fatty acid and fatty acid amide impurities into fatty acid nitrile.
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公开(公告)号:NO874853A
公开(公告)日:1988-05-24
申请号:NO874853
申请日:1987-11-20
Applicant: HOECHST AG
Inventor: STUEHLER HERBERT , FISCHER KURT
IPC: C07C29/00 , C07B61/00 , C07C27/00 , C07C31/22 , C07C67/00 , C07C253/00 , C07C255/00 , C07C255/03 , C07C255/17 , C07C121/16
CPC classification number: C07C31/225 , C07C253/22 , C07C255/03 , C07C255/07
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公开(公告)号:DK610687A
公开(公告)日:1988-05-22
申请号:DK610687
申请日:1987-11-20
Applicant: HOECHST AG
Inventor: STUEHLER HERBERT , FISCHER KURT
IPC: C07C29/00 , C07B61/00 , C07C27/00 , C07C31/22 , C07C67/00 , C07C253/00 , C07C253/22 , C07C255/00 , C07C255/03 , C07C255/17 , C07C121/00
Abstract: Glycerides are reacted with ammonia in an amount of at least 200 liters per kilogram of glyceride per hour, at a temperature of 220 DEG to 300 DEG C., and in the presence of special catalysts. Of the product mixture which is formed and removed from the reaction with the excess ammonia, and which is composed essentially of the components water, the desired glycerol and fatty acid nitrile containing fatty acid and fatty acid amide, the latter component is returned to the reaction during the glyceride reaction. After completion of the glyceride reaction, which is indicated when the product mixture contains virtually no more glycerol, all the fatty acid nitrile containing fatty acid and fatty acid amide is further treated, in an after-reaction with a reduced amount of ammonia and at higher temperature, in order to convert the fatty acid and fatty acid amide impurities into fatty acid nitrile.
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公开(公告)号:FI881405A0
公开(公告)日:1988-03-24
申请号:FI881405
申请日:1988-03-24
Applicant: HOECHST AG
Inventor: HOFINGER MANFRED , STUEHLER HERBERT , BILLENSTEIN SIEGFRIED , BERENBOLD HELMUT , QUACK JOCHEN MEINHARD
IPC: A61K8/00 , A61K8/40 , A61K8/45 , A61Q5/02 , A61Q5/12 , C07B61/00 , C07C67/00 , C07C213/00 , C07C219/06 , C11D1/62 , C11D3/30 , D06M13/02 , D06M13/322 , D06M13/46 , C07C
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公开(公告)号:DD232913A5
公开(公告)日:1986-02-12
申请号:DD27705485
申请日:1985-06-05
Applicant: HOECHST AG
Inventor: BILLENSTEIN SIEGFRIED , KUKLA BRUNO , STUEHLER HERBERT
IPC: C11C3/10 , C07C67/03 , C07C69/003 , C11C3/04 , C07C62/24
Abstract: A process for the preparation of fatty acid esters of short-chain primary and secondary alcohols with 1 to 5 carbon atoms by transesterification of glycerides with the said short-chain alcohols is described. In this process, a stream of the gaseous alcohol is passed through the liquid glyceride at temperatures of at least 210 DEG C. and the product mixture of gylcerol and fatty acid alkyl ester is discharged from the reaction zone with this stream and is then subjected to phase separation.
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公开(公告)号:DD138311A5
公开(公告)日:1979-10-24
申请号:DD20732178
申请日:1978-08-16
Applicant: HOECHST AG
Inventor: BILLENSTEIN SIEGFRIED , KUKLA BRUNO , STUEHLER HERBERT
IPC: C07C29/00 , B01J31/00 , B01J31/02 , B01J31/04 , C07B61/00 , C07C20060101 , C07C27/00 , C07C31/22 , C07C67/00 , C07C253/00 , C07C253/22 , C07C255/03 , C07C255/06 , C07C255/11 , C07C255/15 , C11B3/00 , C11C20060101 , C11C1/00
Abstract: Glycerol and aliphatic nitriles are simultaneously produced by treating liquid glycerides with gaseous ammonia at a rate of at least 200 liters of ammonia per kilogram of glyceride per hour at temperatures of from 220 DEG to 300 DEG C. in the presence of metal salts of carboxylic or sulfonic acids as catalysts and subjecting the product mixture to a phase separation into a nitrile phase and a glycerol/water phase. Preferred starting materials are vegetable and animal fats and oils.
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