113.
    发明专利
    未知

    公开(公告)号:DE50003261D1

    公开(公告)日:2003-09-18

    申请号:DE50003261

    申请日:2000-02-28

    Applicant: BASF AG

    Abstract: The present invention relates to a process for the continuous preparation of methoxyamine hydrochloride by cleavage of acetone oxime methyl ether by means of hydrogen chloride and water, wherein the cleavage is carried out in a reaction column having less than 20 theoretical plates and the amount taken off at the top is set to at least 30% of the amount of feed.

    114.
    发明专利
    未知

    公开(公告)号:PT994112E

    公开(公告)日:2002-12-31

    申请号:PT99117240

    申请日:1999-09-02

    Applicant: BASF AG

    Abstract: Separation of impurities from 3-(2'-acetoxyethyl)-dihydro-2(3H)-furanone (I) obtained by acetylation of 3-(2'-hydroxyethyl)-dihydro-2(3H)-furanone comprises first separating high boiling impurities and subjecting the recovered distillation head product to a further step in which light and medium boiling components are taken off at the head and recovering pure (I) as the sump product.

    115.
    发明专利
    未知

    公开(公告)号:AT221060T

    公开(公告)日:2002-08-15

    申请号:AT99117240

    申请日:1999-09-02

    Applicant: BASF AG

    Abstract: Separation of impurities from 3-(2'-acetoxyethyl)-dihydro-2(3H)-furanone (I) obtained by acetylation of 3-(2'-hydroxyethyl)-dihydro-2(3H)-furanone comprises first separating high boiling impurities and subjecting the recovered distillation head product to a further step in which light and medium boiling components are taken off at the head and recovering pure (I) as the sump product.

    119.
    发明专利
    未知

    公开(公告)号:DE19911234A1

    公开(公告)日:2000-09-28

    申请号:DE19911234

    申请日:1999-03-15

    Applicant: BASF AG

    Abstract: The invention relates to a method for the continuous production of methoxyamine hydrochloride by dissociating acetone oxime dimethyl ether with hydrogen chloride and water. The inventive method is characterized by carrying out the dissociation step in a reactor column of less than 20 theoretical steps of separation and adjusting the overhead removal amount to at least 30 % of the quantity supplied.

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