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公开(公告)号:ES2241833T3
公开(公告)日:2005-11-01
申请号:ES01942361
申请日:2001-01-12
Applicant: BASF AG
Inventor: TELES JOAQUIM HENRIQUE , REHFINGER ALWIN , BASSLER PETER , RIEBER NORBERT , HEFNER WERNER , BERG ANNE
IPC: B01D3/00 , C07B61/00 , C07C5/42 , C07C11/06 , C07D301/12 , C07D301/32 , C07D303/04
Abstract: Un procedimiento para tratar una mezcla (M1), que comprende un alqueno y oxígeno, en el que (i) el oxígeno se retira de la mezcla (M1) mediante la combustión del oxígeno para dar una mezcla (M2) y (ii)el alqueno se separa de la mezcla (M2) mediante destilación, en donde la combustión del oxígeno contenido en la mezcla (M1) se efectúa catalíticamente, los catalizadores usados para dicho propósito se seleccionan del grupo que consiste en metales nobles y cromito de cobre y la combustión catalítica se lleva a cabo a una temperatura de 280 a 580ºC.
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公开(公告)号:DE60111015D1
公开(公告)日:2005-06-30
申请号:DE60111015
申请日:2001-01-12
Applicant: BASF AG
Inventor: TELES HENRIQUE , REHFINGER ALWIN , BASSLER PETER , RIEBER NORBERT , HEFNER WERNER , BERG ANNE , RUDOLF PETER
IPC: B01D3/00 , C07B61/00 , C07C5/42 , C07C11/06 , C07D301/12 , C07D301/32 , C07D303/04
Abstract: A mixture (M1) comprising an alkene and oxygen is worked up by a process in which (i) oxygen is removed from the mixture (M1) by a nondistillative method to give a mixture (M2) and (ii) the alkene is separated off from the mixture (M2) by distillation.
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公开(公告)号:AT296297T
公开(公告)日:2005-06-15
申请号:AT01942361
申请日:2001-01-12
Applicant: BASF AG
Inventor: TELES JOAQUIM HENRIQUE , REHFINGER ALWIN , BASSLER PETER , RIEBER NORBERT , HEFNER WERNER , BERG ANNE , RUDOLF PETER
IPC: B01D3/00 , C07B61/00 , C07C5/42 , C07C11/06 , C07D301/12 , C07D301/32 , C07D303/04
Abstract: A mixture (M1) comprising an alkene and oxygen is worked up by a process in which (i) oxygen is removed from the mixture (M1) by a nondistillative method to give a mixture (M2) and (ii) the alkene is separated off from the mixture (M2) by distillation.
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公开(公告)号:AU2003219096A1
公开(公告)日:2003-10-13
申请号:AU2003219096
申请日:2003-03-25
Applicant: BASF AG
Inventor: ASPRION NORBERT , GROSSMANN CHRISTOPH , HOLEMANN KARL , THEIS GERHARD , WAHL PETER , HEFNER WERNER , BORCHERT HOLGER
IPC: C07D301/32
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公开(公告)号:SG42369A1
公开(公告)日:1997-08-15
申请号:SG1996006836
申请日:1996-03-09
Applicant: BASF AG
Inventor: TENTEN ANDREAS , NEUMANN HANS-PETER , VOGEL HERBERT , MACHHAMMER OTTO , HEFNER WERNER , RUPPEL WILHELM
Abstract: In continuous gas phase oxidn. of C3H6 to acrolein (I) and/or acrylic acid (II) with heterogeneous catalyst in an oxidn. reactor, the charge gas mixt. (III) contains only inert diluent gas(es) (IIIA) in addn. to C3H6 and O2 and (pt. of) (IIIA) is sepd. from the prodn. gas mixt. and recycled to the oxidn. reactor. The novelty is that (IIIA) consists of over 85 vol. % 1-5C satd. hydrocarbon(s).
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公开(公告)号:DE19525504A1
公开(公告)日:1997-01-16
申请号:DE19525504
申请日:1995-07-13
Applicant: BASF AG
Inventor: HEFNER WERNER , MACHHAMMER OTTO , NEUMANN HANS-PETER , TENTEN ANDREAS , RUPPEL WILHELM , VOGEL HERBERT
Abstract: Prodn. of acrolein (I) and/or acrylic acid (II) from C3H8 involves (A) gas phase partial dehydrogenation of C3H8 to C3H6, using heterogeneous catalyst; (B) using the prod. gas mixt. of C3H6 and unreacted C3H8 for charging an oxidn. reactor, in which C3H6 is converted to (I) and/or (II) by gas phase selective partial oxidn. with pure O2 using heterogeneous catalyst; and (C) separating the prod. from the prod. gas stream and recycling at least the unreacted C3H8 from stage (B) to stage (A). The novelty is that, before entering stage (B), constituents other than C3H8 and C3H6, at least H2 and steam, are removed from the prod. gas mixt. from stage (A). Pref. all constituents except C3H8 and C3H6 are removed after stage (A). Stage (B) is carried out in 2 consecutive reactors charged with multi-metal oxide catalysts, the first of Mo-Bi-Fe and the second of Mo-V. The prod. gas mixt. from the first oxidn. reactor is passed directly into the second; and the vol. ratio of organic cpd. for partial oxidn. (C3H6 or (II)) to O2 is 1:(1-3) in both reactors.
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公开(公告)号:DE19508558A1
公开(公告)日:1996-09-12
申请号:DE19508558
申请日:1995-03-10
Applicant: BASF AG
Inventor: HEFNER WERNER , MACHHAMMER OTTO , NEUMANN HANS-PETER , TENTEN ANDREAS , RUPPEL WILHELM , VOGEL HERBERT
Abstract: Prodn. of acrolein (I) and/or acrylic acid (II) from C3H8 involves (A) gas phase partial dehydrogenation of C3H8 to C3H6, using heterogeneous catalyst; (B) using the prod. gas mixt. of C3H6 and unreacted C3H8 for charging an oxidn. reactor, in which C3H6 is converted to (I) and/or (II) by gas phase selective partial oxidn. with pure O2 using heterogeneous catalyst; and (C) separating the prod. from the prod. gas stream and recycling at least the unreacted C3H8 from stage (B) to stage (A). The novelty is that, before entering stage (B), constituents other than C3H8 and C3H6, at least H2 and steam, are removed from the prod. gas mixt. from stage (A). Pref. all constituents except C3H8 and C3H6 are removed after stage (A). Stage (B) is carried out in 2 consecutive reactors charged with multi-metal oxide catalysts, the first of Mo-Bi-Fe and the second of Mo-V. The prod. gas mixt. from the first oxidn. reactor is passed directly into the second; and the vol. ratio of organic cpd. for partial oxidn. (C3H6 or (II)) to O2 is 1:(1-3) in both reactors.
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公开(公告)号:NO172477C
公开(公告)日:1993-07-28
申请号:NO893322
申请日:1989-08-18
Applicant: BASF AG
Inventor: GERHARDT WOLFGANG , HEFNER WERNER
Abstract: The present invention relates to a process for removing CO2 and possibly H2S from a gas containing CO2 and possibly H2S by means of an absorption fluid, wherein the gas containing CO2 and possibly H2S is treated in an absorption zone with the absorption fluid, the treated gas is extracted from the absorption zone, the absorption fluid laden with CO2 and possibly H2S is then regenerated by expanding the absorption fluid laden with CO2 and possibly H2S in one or more expansion stages and extracting an expansion gas at the top of the first expansion stage or, in the case of more than one expansion stages, at the top of at least one of the first to penultimate expansion stages and feeding, if desired, the partially regenerated absorption fluid obtained from the last expansion stage to a stripping zone for further regeneration, at least one acid gas stream containing the CO2 and possibly H2S being extracted from the regeneration and the regenerated absorption fluid being recycled into the absorption zone, wherein a part stream of fully or partially regenerated absorption fluid is fed to at least one of the expansion stages, from which the expansion gas is extracted, at a point above the feed of the absorption fluid which is to be expanded.
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公开(公告)号:NO893322L
公开(公告)日:1990-02-20
申请号:NO893322
申请日:1989-08-18
Applicant: BASF AG
Inventor: GERHARDT WOLFGANG , HEFNER WERNER
Abstract: The present invention relates to a process for removing CO2 and possibly H2S from a gas containing CO2 and possibly H2S by means of an absorption fluid, wherein the gas containing CO2 and possibly H2S is treated in an absorption zone with the absorption fluid, the treated gas is extracted from the absorption zone, the absorption fluid laden with CO2 and possibly H2S is then regenerated by expanding the absorption fluid laden with CO2 and possibly H2S in one or more expansion stages and extracting an expansion gas at the top of the first expansion stage or, in the case of more than one expansion stages, at the top of at least one of the first to penultimate expansion stages and feeding, if desired, the partially regenerated absorption fluid obtained from the last expansion stage to a stripping zone for further regeneration, at least one acid gas stream containing the CO2 and possibly H2S being extracted from the regeneration and the regenerated absorption fluid being recycled into the absorption zone, wherein a part stream of fully or partially regenerated absorption fluid is fed to at least one of the expansion stages, from which the expansion gas is extracted, at a point above the feed of the absorption fluid which is to be expanded.
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公开(公告)号:NO893322D0
公开(公告)日:1989-08-18
申请号:NO893322
申请日:1989-08-18
Applicant: BASF AG
Inventor: GERHARDT WOLFGANG , HEFNER WERNER
Abstract: The present invention relates to a process for removing CO2 and possibly H2S from a gas containing CO2 and possibly H2S by means of an absorption fluid, wherein the gas containing CO2 and possibly H2S is treated in an absorption zone with the absorption fluid, the treated gas is extracted from the absorption zone, the absorption fluid laden with CO2 and possibly H2S is then regenerated by expanding the absorption fluid laden with CO2 and possibly H2S in one or more expansion stages and extracting an expansion gas at the top of the first expansion stage or, in the case of more than one expansion stages, at the top of at least one of the first to penultimate expansion stages and feeding, if desired, the partially regenerated absorption fluid obtained from the last expansion stage to a stripping zone for further regeneration, at least one acid gas stream containing the CO2 and possibly H2S being extracted from the regeneration and the regenerated absorption fluid being recycled into the absorption zone, wherein a part stream of fully or partially regenerated absorption fluid is fed to at least one of the expansion stages, from which the expansion gas is extracted, at a point above the feed of the absorption fluid which is to be expanded.
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