1.
    发明专利
    未知

    公开(公告)号:MX9306515A

    公开(公告)日:1994-04-29

    申请号:MX9306515

    申请日:1993-10-20

    Applicant: DEGUSSA

    Abstract: PCT No. PCT/EP93/02838 Sec. 371 Date May 23, 1995 Sec. 102(e) Date May 23, 1995 PCT Filed Oct. 14, 1993 PCT Pub. No. WO94/08957 PCT Pub. Date Apr. 28, 1994The direct saponification of methionine nitrile obtained from methylmercaptopropionaldehyde, prussic acid and ammonia gives low yields, catalyst and educt losses and unwanted side-products. The aim of the invention is therefore to provide a method which can be carried out without isolating the intermediate products, in particular continuously, and with low losses. The ketone used is recovered in high yields after amide saponification since this liberates the ketone from side-products. In order to recover the ammonia, it is necessary for the ammonia to be substantially freed of ketone, the mixture of ammonia, ketone and water obtained being separated under pressure in a separation column. When the amide is saponified at >/=160 DEG C., amide concentrations of less than 25% by wt. are preferred. Methionine nitrile is produced by treatment with at least 4 equivalents of >/=50% by wt. ammonia at between 40 DEG and 80 DEG C./or between 5 and 60 min. Cyanide residues are destroyed by heating to over 150 DEG C. Methionine is of particular use as a feedstuff, in particular in aqueous solution.

    Continuous process for the production of methionine or methionine derivatives

    公开(公告)号:SG47910A1

    公开(公告)日:1998-04-17

    申请号:SG1996005199

    申请日:1993-10-14

    Applicant: DEGUSSA

    Abstract: PCT No. PCT/EP93/02838 Sec. 371 Date May 23, 1995 Sec. 102(e) Date May 23, 1995 PCT Filed Oct. 14, 1993 PCT Pub. No. WO94/08957 PCT Pub. Date Apr. 28, 1994The direct saponification of methionine nitrile obtained from methylmercaptopropionaldehyde, prussic acid and ammonia gives low yields, catalyst and educt losses and unwanted side-products. The aim of the invention is therefore to provide a method which can be carried out without isolating the intermediate products, in particular continuously, and with low losses. The ketone used is recovered in high yields after amide saponification since this liberates the ketone from side-products. In order to recover the ammonia, it is necessary for the ammonia to be substantially freed of ketone, the mixture of ammonia, ketone and water obtained being separated under pressure in a separation column. When the amide is saponified at >/=160 DEG C., amide concentrations of less than 25% by wt. are preferred. Methionine nitrile is produced by treatment with at least 4 equivalents of >/=50% by wt. ammonia at between 40 DEG and 80 DEG C./or between 5 and 60 min. Cyanide residues are destroyed by heating to over 150 DEG C. Methionine is of particular use as a feedstuff, in particular in aqueous solution.

    Method for the continuous preparation of methionine or methionine derivatives

    公开(公告)号:AU675989B2

    公开(公告)日:1997-02-27

    申请号:AU5333994

    申请日:1993-10-14

    Applicant: DEGUSSA

    Abstract: PCT No. PCT/EP93/02838 Sec. 371 Date May 23, 1995 Sec. 102(e) Date May 23, 1995 PCT Filed Oct. 14, 1993 PCT Pub. No. WO94/08957 PCT Pub. Date Apr. 28, 1994The direct saponification of methionine nitrile obtained from methylmercaptopropionaldehyde, prussic acid and ammonia gives low yields, catalyst and educt losses and unwanted side-products. The aim of the invention is therefore to provide a method which can be carried out without isolating the intermediate products, in particular continuously, and with low losses. The ketone used is recovered in high yields after amide saponification since this liberates the ketone from side-products. In order to recover the ammonia, it is necessary for the ammonia to be substantially freed of ketone, the mixture of ammonia, ketone and water obtained being separated under pressure in a separation column. When the amide is saponified at >/=160 DEG C., amide concentrations of less than 25% by wt. are preferred. Methionine nitrile is produced by treatment with at least 4 equivalents of >/=50% by wt. ammonia at between 40 DEG and 80 DEG C./or between 5 and 60 min. Cyanide residues are destroyed by heating to over 150 DEG C. Methionine is of particular use as a feedstuff, in particular in aqueous solution.

    5.
    发明专利
    未知

    公开(公告)号:DE4235295A1

    公开(公告)日:1994-04-21

    申请号:DE4235295

    申请日:1992-10-20

    Applicant: DEGUSSA

    Abstract: The direct saponification of methionine nitrile obtained from methylmercaptopropionaldehyde, prussic acid and ammonia gives low yields, catalyst and educt losses and unwanted side-products. The aim of the invention is therefore to provide a method which can be carried out without isolating the intermediate products, in particular continuously, and with low losses. The ketone used is recovered in high yields after amide saponification since this liberates the ketone from side-products. In order to recover the ammonia, it is necessary for the ammonia to be substantially freed of ketone, the mixture of ammonia, ketone and water obtained being separated under pressure in a separation column. When the amide is saponified at >/= 160 DEG C, amide concentrations of less than 25 % by wt. are preferred. Methionine nitrile is produced by treatment with at least 4 equivalents of >/= 50 % by wt. ammonia at between 40 and 80 DEG C for between 5 and 60 min. Cyanide residues are destroyed by heating to over 150 DEG C. Methionine is of particular use as a feedstuff, in particular in aqueous solution.

    CONTINUOUS PROCESS OF PREPARING METHIONINE OR METHIONINE DERIVATIVES

    公开(公告)号:CZ94795A3

    公开(公告)日:1995-09-13

    申请号:CZ94795

    申请日:1993-10-14

    Applicant: DEGUSSA

    Abstract: PCT No. PCT/EP93/02838 Sec. 371 Date May 23, 1995 Sec. 102(e) Date May 23, 1995 PCT Filed Oct. 14, 1993 PCT Pub. No. WO94/08957 PCT Pub. Date Apr. 28, 1994The direct saponification of methionine nitrile obtained from methylmercaptopropionaldehyde, prussic acid and ammonia gives low yields, catalyst and educt losses and unwanted side-products. The aim of the invention is therefore to provide a method which can be carried out without isolating the intermediate products, in particular continuously, and with low losses. The ketone used is recovered in high yields after amide saponification since this liberates the ketone from side-products. In order to recover the ammonia, it is necessary for the ammonia to be substantially freed of ketone, the mixture of ammonia, ketone and water obtained being separated under pressure in a separation column. When the amide is saponified at >/=160 DEG C., amide concentrations of less than 25% by wt. are preferred. Methionine nitrile is produced by treatment with at least 4 equivalents of >/=50% by wt. ammonia at between 40 DEG and 80 DEG C./or between 5 and 60 min. Cyanide residues are destroyed by heating to over 150 DEG C. Methionine is of particular use as a feedstuff, in particular in aqueous solution.

    Method for the continuous preparation of methionine or methionine derivatives

    公开(公告)号:AU5333994A

    公开(公告)日:1994-05-09

    申请号:AU5333994

    申请日:1993-10-14

    Applicant: DEGUSSA

    Abstract: PCT No. PCT/EP93/02838 Sec. 371 Date May 23, 1995 Sec. 102(e) Date May 23, 1995 PCT Filed Oct. 14, 1993 PCT Pub. No. WO94/08957 PCT Pub. Date Apr. 28, 1994The direct saponification of methionine nitrile obtained from methylmercaptopropionaldehyde, prussic acid and ammonia gives low yields, catalyst and educt losses and unwanted side-products. The aim of the invention is therefore to provide a method which can be carried out without isolating the intermediate products, in particular continuously, and with low losses. The ketone used is recovered in high yields after amide saponification since this liberates the ketone from side-products. In order to recover the ammonia, it is necessary for the ammonia to be substantially freed of ketone, the mixture of ammonia, ketone and water obtained being separated under pressure in a separation column. When the amide is saponified at >/=160 DEG C., amide concentrations of less than 25% by wt. are preferred. Methionine nitrile is produced by treatment with at least 4 equivalents of >/=50% by wt. ammonia at between 40 DEG and 80 DEG C./or between 5 and 60 min. Cyanide residues are destroyed by heating to over 150 DEG C. Methionine is of particular use as a feedstuff, in particular in aqueous solution.

    10.
    发明专利
    未知

    公开(公告)号:ES2102686T3

    公开(公告)日:1997-08-01

    申请号:ES93923467

    申请日:1993-10-14

    Applicant: DEGUSSA

    Abstract: PCT No. PCT/EP93/02838 Sec. 371 Date May 23, 1995 Sec. 102(e) Date May 23, 1995 PCT Filed Oct. 14, 1993 PCT Pub. No. WO94/08957 PCT Pub. Date Apr. 28, 1994The direct saponification of methionine nitrile obtained from methylmercaptopropionaldehyde, prussic acid and ammonia gives low yields, catalyst and educt losses and unwanted side-products. The aim of the invention is therefore to provide a method which can be carried out without isolating the intermediate products, in particular continuously, and with low losses. The ketone used is recovered in high yields after amide saponification since this liberates the ketone from side-products. In order to recover the ammonia, it is necessary for the ammonia to be substantially freed of ketone, the mixture of ammonia, ketone and water obtained being separated under pressure in a separation column. When the amide is saponified at >/=160 DEG C., amide concentrations of less than 25% by wt. are preferred. Methionine nitrile is produced by treatment with at least 4 equivalents of >/=50% by wt. ammonia at between 40 DEG and 80 DEG C./or between 5 and 60 min. Cyanide residues are destroyed by heating to over 150 DEG C. Methionine is of particular use as a feedstuff, in particular in aqueous solution.

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