PURIFICATION OF ACRYLIC AND METHACRYLIC ACIDS

    公开(公告)号:CZ43697A3

    公开(公告)日:1997-09-17

    申请号:CZ43697

    申请日:1997-02-12

    Applicant: BASF AG

    Abstract: A process for purifying (meth)acrylic acid by phase separation techniques comprises the following steps: (a) a mixture containing (meth)acrylic acid is separated into distinct phases in the presence of an organic solvent, with the composition of the (meth)acrylic acid-rich phase remaining essentially unchanged, and this acid-rich phase is separated; (b) the remaining phase from step (a) is separated into indistinct phases; and (c) one of the phases from step (b) is returned to step (a). Also claimed is preparation of (meth)acrylic acid. Preferably in step (c) the acid-rich phase is returned to step (a). 1-100 (100) wt.% of the phase remaining from step (a) is used in step (b). Pure end product is added to steps (a) and (b). Step (a) involves crystallisation, freezing or sublimation, preferably static and/or dynamic crystallisation, and most preferably a combined static and dynamic crystallisation in which the residue from the dynamic crystallisation is added to the static crystallisation step and the crystallised product from the static crystallisation is returned to the dynamic crystallisation.

    Zpusob prípravy kyseliny (meth)akrylové

    公开(公告)号:CZ298267B6

    公开(公告)日:2007-08-08

    申请号:CZ43697

    申请日:1997-02-12

    Applicant: BASF AG

    Abstract: Postup prípravy kyseliny (meth)akrylové zahrnující následující stupne: (I) katalytickou oxidaci propenu nebo izobutenu a/nebo akroleinu nebo methakroleinu v plynné fázi na kyselinu (meth)akrylovou zavzniku plynného reakcního produktu obsahujícího kyselinu (meth)akrylovou; (II) absorpci tohoto reakcního produktu za použití vysokovroucího rozpouštedla; (III) rozdelení rozpouštedla s absorbovaným produktem ze stupne (I), které se získá ve stupni (II), na rozpouštedlo a surovou (meth)akrylovou kyselinu pomocí destilace; (IV) vycištení surové (meth)akrylové kyseliny ze stupne (III) krystalizací za vzniku (meth)akrylové kyseliny; a (V) recirkulaci prinejmenším cásti výsledného matecného louhu dostupne (II) a/nebo stupne (III).

    25.
    发明专利
    未知

    公开(公告)号:DE50206163D1

    公开(公告)日:2006-05-11

    申请号:DE50206163

    申请日:2002-05-28

    Applicant: BASF AG

    Abstract: The invention relates to a method for producing (meth)acrylic acid esters IV by means of transesterification of a (meth)acrylic acid ester I with an alcohol R 2 OH comprising at least one more carbon atom than the alcohol constituents (R 1 O-) in the (meth)acrylic acid ester I to be subjected to transesterification, in the presence of a catalyst or a catalyst mixture. Either essentially the (meth)acrylic acid ester I is separated and then the catalyst used is separated by distillation (catalyst separation), or the catalyst used is separated by distillation first (catalyst separation), and then essentially the (meth)acrylic acid ester I is separated, from the reaction product of the transesterification. Constituents from the mixture obtained, which have a lower boiling point than the (meth)acrylic acid ester IV, are essentially separated by distillation (separation of constituents at low boiling point), and the (meth)acrylic acid ester IV is then purified by distillation (purification by distillation).

    Purification of acrylic acid and methacrylic acid

    公开(公告)号:SG77590A1

    公开(公告)日:2001-01-16

    申请号:SG1997000382

    申请日:1997-02-21

    Applicant: BASF AG

    Abstract: A process for purifying (meth)acrylic acid by phase separation techniques comprises the following steps: (a) a mixture containing (meth)acrylic acid is separated into distinct phases in the presence of an organic solvent, with the composition of the (meth)acrylic acid-rich phase remaining essentially unchanged, and this acid-rich phase is separated; (b) the remaining phase from step (a) is separated into indistinct phases; and (c) one of the phases from step (b) is returned to step (a). Also claimed is preparation of (meth)acrylic acid. Preferably in step (c) the acid-rich phase is returned to step (a). 1-100 (100) wt.% of the phase remaining from step (a) is used in step (b). Pure end product is added to steps (a) and (b). Step (a) involves crystallisation, freezing or sublimation, preferably static and/or dynamic crystallisation, and most preferably a combined static and dynamic crystallisation in which the residue from the dynamic crystallisation is added to the static crystallisation step and the crystallised product from the static crystallisation is returned to the dynamic crystallisation.

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