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公开(公告)号:ID16044A
公开(公告)日:1997-08-28
申请号:ID970559
申请日:1997-02-24
Applicant: BASF AG
Inventor: MACHHAMMER OTTO , DAMS ALBRECHT , ECK BERND , PROLL THEO
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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公开(公告)号:MX9700316A
公开(公告)日:1997-07-31
申请号:MX9700316
申请日:1997-01-10
Applicant: BASF AG
Inventor: MACHHAMMER OTTO , DOCKNER TONI , ENGERT GERD-JUERGEN , PROLL THEO
IPC: B01D9/02 , B01D3/00 , C07B61/00 , C07C51/235 , C07C51/25 , C07C51/43 , C07C51/48 , C07C57/04 , C07C57/05 , C07C57/055 , C07C57/07 , C07C69/54 , C07C69/653
Abstract: Un proceso para preparar ácido acrílico y/o ésteres comprende los pasos de: (a) oxidacion de fase de gas catalítica de propeno y/o acroleina de ácido acrílico a fin de obtener un producto de reaccion gaseoso que comprende ácido acrílico, (b) absorcion con solvente del producto de reaccion, (c) destilacion del solvente cargado con el ácido acrílico para obtener un ácido acrílico crudo y el solvente, (d) purificacion del ácido acrílico crudo mediante cristalizacion, y (e) opcionalmente esterificacion del ácido acrílico cristalino.
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公开(公告)号:DE19600955A1
公开(公告)日:1997-07-17
申请号:DE19600955
申请日:1996-01-12
Applicant: BASF AG
Inventor: MACHHAMMER OTTO , DOCKNER TONI , ENGERT GERD-JUERGEN , PROLL THEO
IPC: B01D9/02 , B01D3/00 , C07B61/00 , C07C51/235 , C07C51/25 , C07C51/43 , C07C51/48 , C07C57/04 , C07C57/05 , C07C57/055 , C07C57/07 , C07C69/54
Abstract: The production of acrylic acid (I) and/or its esters comprises; (a) catalytic gas-phase oxidation of propene and/or acrolein to give a gaseous product containing (I), (b) absorption of the reaction product with a solvent, (c) distillation in a column to give crude (I) and solvent, (d) purification of (I) by crystallisation and optionally (e) esterification of crystallised (I). Also claimed is an apparatus for the process, comprising reactor(s) for stage (a), an absorption column, a distillation column, dynamic crystalliser(s) and static crystalliser(s), and container(s) for intermediate storage.
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公开(公告)号:AU588664B2
公开(公告)日:1989-09-21
申请号:AU6828087
申请日:1987-02-04
Applicant: BASF AG
Inventor: KROENER MICHAEL , SCHMIDT WILLI , OFTRING ALFRED , PROLL THEO , HARTMANN HEINRICH
IPC: C07C231/24 , C07C67/00 , C07C231/00 , C07C233/00 , C07C233/03 , C07C233/15 , C08F26/00 , C08F126/02 , C07C102/00 , C07C103/127 , C07C103/365
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公开(公告)号:CZ298792B6
公开(公告)日:2008-01-30
申请号:CZ2000885
申请日:1998-09-09
Applicant: BASF AG
Inventor: ECK BERND , MACHHAMMER OTTO , PROLL THEO , SCHLIEPHAKE VOLKER , THIEL JOACHIM , BROELLOS KLAUS
Abstract: Zpusob výroby kyseliny akrylové nebo metakrylové výrobou plynné smesi produktu, která má v podstatesložení reakcní smesi z katalytické oxidace v plynné fázi alkanu, alkenu, alkanolu a/nebo alkanalu se 3 nebo 4 uhlíkovými atomy a/nebo jejich predstupnu na kyselinu akrylovou, prípadne kyselinu metakrylovou. Oddelení kyseliny akrylové nebo metakrylové z plynné smesi produktu se pritom provádí zpusobem, který obsahuje následující kroky: a) kondenzace plynné smesi produktu, b) krystalizace kyseliny akrylové nebo kyseliny metakrylové z roztoku získaného ve stupni a), c) oddelení získaných krystalu z matecného louhu stupne b) a d) zpetné uvedení nejméne cásti matecného louhu ze stupne c) do stupne a).
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公开(公告)号:AU2002355627A1
公开(公告)日:2003-02-17
申请号:AU2002355627
申请日:2002-06-21
Applicant: BASF AG
Inventor: PROLL THEO , SCHINDLER GOTZ-PETER , MACHHAMMER OTTO , MULLER-ENGEL KLAUS JOACHIM
IPC: C07C45/34 , B01J27/199 , C07B61/00 , C07C45/33 , C07C45/35 , C07C47/22 , C07C51/235 , C07C57/055 , C07C253/26 , C07C255/08 , C07C5/333
Abstract: Partial oxidation products and/or ammoxidation products of an olefinic hydrocarbon A' are prepared by a process in which said olefinic hydrocarbon is produced during normal operation by partial dehydrogenation and/or oxydehydrogenation of hydrocarbon A and fed in from another source during partial or complete nonoperation of the dehydrogenation and/or oxydehydrogenation.
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公开(公告)号:ES2175794T3
公开(公告)日:2002-11-16
申请号:ES98948948
申请日:1998-09-09
Applicant: BASF AG
Inventor: ECK BERND , MACHHAMMER OTTO , PROLL THEO , SCHLIEPHAKE VOLKER , THIEL JOACHIM , BROLLOS KLAUS
Abstract: A process for preparing acrylic acid or methacrylic acid comprises preparing a gaseous product mixture having essentially the composition of a reaction mixture of the catalytic gas phase oxidation of C3-/C4-alkanes, -alkenes, -alkanols and/or -alkanals and/or precursors thereof to form acrylic acid or methacrylic acid. The product is removed from the gaseous product mixture by a process comprising the following steps:(a) condensing said gaseous product mixture,(b) crystallizing acrylic acid or methacrylic acid from the solution obtained in step (a),(c) removing the resulting crystals from the mother liquor, and(d) recycling at least a portion of said mother liquor from step (c) into step (a).
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公开(公告)号:DK0784046T3
公开(公告)日:2001-04-30
申请号:DK97100374
申请日:1997-01-10
Applicant: BASF AG
Inventor: MACHHAMMER OTTO , DOCKNER TONI , ENGERT GERD-JUERGEN , PROLL THEO
IPC: B01D9/02 , B01D3/00 , C07B61/00 , C07C51/235 , C07C51/25 , C07C51/43 , C07C51/48 , C07C57/04 , C07C57/05 , C07C57/055 , C07C57/07 , C07C69/54
Abstract: The production of acrylic acid (I) and/or its esters comprises; (a) catalytic gas-phase oxidation of propene and/or acrolein to give a gaseous product containing (I), (b) absorption of the reaction product with a solvent, (c) distillation in a column to give crude (I) and solvent, (d) purification of (I) by crystallisation and optionally (e) esterification of crystallised (I). Also claimed is an apparatus for the process, comprising reactor(s) for stage (a), an absorption column, a distillation column, dynamic crystalliser(s) and static crystalliser(s), and container(s) for intermediate storage.
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公开(公告)号:ID27390A
公开(公告)日:2001-04-05
申请号:ID20010163
申请日:1999-07-21
Applicant: BASF AG
Inventor: ECK BERND , HEILEK JORG , SCHLEIPHAKE VOLKER , PROLL THEO , BROLLOS KLAUS , THIEL JOACHIM , MACHHAMMER OTTO
IPC: C07C51/225 , C07C51/43 , C07C57/05 , C07C57/07
Abstract: A process for the preparation of acrylic acid by:(a) preparation of a gaseous product mixture which essentially has the composition of a reaction mixture of catalytic gas-phase oxidation of C3-alkanes, C3-alkenes, C3-alkanols and/or C3-alkanals and/or intermediates thereof to acrylic acid, which comprises(b) condensation of the gaseous product mixture,(c) crystallization of the acrylic acid from the solution obtained in stage (b), with partial evaporation of the solution under reduced pressure,(d) isolation of the resulting crystals from the mother liquor,(e) recycling of at least a part of the mother liquor from stage (d) to stage (b) and(f) recycling of at least a part of the evaporated solution from stage (c) to stage (b).
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公开(公告)号:CZ2000898A3
公开(公告)日:2000-06-14
申请号:CZ2000898
申请日:1998-09-10
Applicant: BASF AG
Inventor: ECK BERND , MACHHAMMER OTTO , PROLL THEO , SCHLIEPHAKE VOLKER , THIEL JOACHIM , BROELLOS KLAUS
Abstract: A process for the fractional condensation of a gas mixture which, in addition to acrylic acid or methacrylic acid, also contains at least one further condensable component and additionally a high proportion of one or more noncondensable components, wherein the gas mixture is passed through a column having separatory internals and the condensable components are condensed by cooling.
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