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公开(公告)号:DE19948241A1
公开(公告)日:2001-04-12
申请号:DE19948241
申请日:1999-10-07
Applicant: BASF AG
Inventor: ARNOLD HEIKO , UNVERRICHT SIGNE , HAMMON ULRICH , NEUMANN HANS-PETER , HARTH KLAUS , TENTEN ANDREAS
IPC: B01J23/887 , C07C45/35 , C07C51/25 , B01J23/28 , B01J23/30 , B01J23/31 , B01J23/888 , B01J27/057 , C07C47/22
Abstract: Gas phase oxidation of propylene into acrylic acid in which the mixture of reaction gas is oxidized on a first fixed-bed catalyst and the mixture of product gas which contain acrolein oxidized on a second fixed-bed catalyst. The catalyst shaped bodies comprise an annular geometry in both reaction steps. Gas-phase oxidation of propylene in a one-stage reaction to acrolein and/or acrylic acid or in a two-stage reaction to acrylic acid is such that (i) the initial charge in both cases is \- 160 Nl propylene/l catalyst hour; (ii) the charge to the 2nd stage (if used) includes \- 140 NL acrolein/l catalyst hour ; and (iii) the catalyst or catalysts is/are of ring form with an outer diameter 2-11 mm, length 2-11 mm and a wall-thickness 1-5 mm. The process comprises (A) feeding a mixture of propylene, molecular oxygen and an inert gas with molar ratio O2 : C3H6 \- 1 at high temperature over a solid bed catalyst with characteristics (i) and (iii) above and comprising a multi-metal oxide containing Mo and/or W together with Bi, Te, Sb, Sn and/or Cu such that the propylene conversion and the combined selectivity for acrolein and the acrylic acid by-product are both \- 90 mol.%; and optionally (B) cooling the acrolein-containing gas product and optionally adding molecular O2 and/or inert gas prior to passing it at high temperature and with molar ratio O2 : acrolein \- 0.5 over a Mo- and V-containing multi-metal oxide solid bed catalyst such that the acrolein conversion is \- 90 mol.% and the combined two-stage acrylic acid selectivity (based on propylene conversion) is \- 80 mol.%.
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公开(公告)号:BR9908730A
公开(公告)日:2000-11-21
申请号:BR9908730
申请日:1999-03-04
Applicant: BASF AG
Inventor: HAMMON ULRICH , HERBST HOLGER , NESTLER GERHARD
IPC: C07C51/44 , C07C51/50 , C07C57/04 , C07C57/055 , C07C57/07 , C07C57/075
Abstract: In a process for rectificative isolation of (meth)acrylic acid from a mixture containing, as main components, (meth)acrylic acid and an organic liquid having a higher boiling point than (meth)acrylic acid, the rectification is carried out with the addition of a surfactant.
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公开(公告)号:AU3425400A
公开(公告)日:2000-09-28
申请号:AU3425400
申请日:2000-02-28
Applicant: BASF AG
Inventor: UNVERRICHT SIGNE , ARNOLD HEIKO , TENTEN ANDREAS , HAMMON ULRICH , NEUMANN HANS-PETER , HARTH KLAUS
IPC: B01J23/88 , B01J23/00 , B01J23/31 , B01J23/887 , B01J35/00 , C07B61/00 , C07C27/14 , C07C45/35 , C07C47/22 , C07C51/215 , C07C51/25 , C07C57/04 , C07C57/05
Abstract: A process for the catalytic gas-phase oxidation of propene to acrylic acid, in which the reaction gas starting mixture is oxidized, with an increased propene loading, in a first reaction stage, over a first fixed-bed catalyst and then the acrolein-containing product gas mixture of the first reaction stage is oxidized, in a second reaction stage, with an increased acrolein loading, over a second fixed-bed catalyst, the catalyst moldings in both reaction stages having an annular geometry.
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公开(公告)号:DE19910506A1
公开(公告)日:2000-09-14
申请号:DE19910506
申请日:1999-03-10
Applicant: BASF AG
Inventor: ARNOLD HEIKO , UNVERRICHT SIGNE , HAMMON ULRICH , NEUMANN HANS-PETER , HARTH KLAUS , TENTEN ANDREAS
IPC: B01J23/00 , B01J23/31 , B01J23/887 , B01J35/00 , C07C45/35 , C07C51/25 , C07C57/055 , C07C57/05
Abstract: Production of acrolein or acrylic acid by gas-phase oxidation of propene comprises passing a mixture of propene, oxygen and inert gas (including at least 20 vol.% nitrogen) through a first fixed bed of catalyst at a temperature (T1) of 300-330 deg C and then through a second fixed bed of catalyst at a temperature (T2) of 300-365 deg C, where T2 is at least 5 deg C above T1. The molar ratio of oxygen to propene is at least 1:1. The catalyst is a mixed metal oxide comprising (i) molybdenum and/or tungsten and (ii) bismuth, tellurium, antimony, tin and/or copper. The propene supply rate is at least 160 Nl per liter of catalyst per hour. The single-pass propene conversion is at least 90%, with at least 90% selectivity for acrolein plus acrylic acid. The propene conversion in the first bed is 40-80%.
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125.
公开(公告)号:DE19810962A1
公开(公告)日:1999-09-16
申请号:DE19810962
申请日:1998-03-13
Applicant: BASF AG
Inventor: HAMMON ULRICH , HERBST HOLGER , NESTLER GERHARD
IPC: C07C51/44 , C07C51/50 , C07C57/04 , C07C57/055 , C07C57/07 , C07C57/075
Abstract: A surfactant is added in the separation of (meth)acrylic acid (I) from a mixture containing an organic liquid with a higher boiling point than (I) as main constituent by rectification. An Independent claim is also included for (I) production by catalytic gas phase oxidation of 3/4 carbon (C) educts.
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公开(公告)号:ES2126787T3
公开(公告)日:1999-04-01
申请号:ES94929529
申请日:1994-10-11
Applicant: BASF AG
Inventor: TENTEN ANDREAS , HAMMON ULRICH , WEIDLICH PETER
IPC: B01J23/00 , B01J23/28 , B01J23/88 , B01J23/887 , B01J23/888 , B01J37/00 , B01J37/02 , B01J37/08 , C07B33/00 , C07B35/04 , C07C51/25 , C07C57/04 , C07C57/055 , C07C253/26
Abstract: PCT No. PCT/EP94/03345 Sec. 371 Date Apr. 19, 1996 Sec. 102(e) Date Apr. 19, 1996 PCT Filed Oct. 11, 1994 PCT Pub. No. WO95/11081 PCT Pub. Date Apr. 27, 1995In a process for the preparation of catalytically active poly-metal oxide materials containing Mo and V, a catalyst intermediate is calcined at from 300 DEG to 450 DEG C. in a gas atmosphere which, in addition to inert gases and/or steam, consists of from 0.5 to 4% by volume of O2 and, averaged over the calcination time, from 1 to 8% by volume of NH3.
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公开(公告)号:CA2261617A1
公开(公告)日:1998-02-12
申请号:CA2261617
申请日:1997-08-04
Applicant: BASF AG
Inventor: HEIDA BERND , HAMMON ULRICH , THIESSEN FRITZ
IPC: B01D17/025 , B01D17/02 , C07C51/25 , C07C57/04 , C07C57/055 , C07C57/07
Abstract: In a separator (11), designed to separate mixtures composed of liquids of various densities, the inflow (12) of the liquid mixture is so arranged and so designed that the inflowing liquid mixture hits an inner wall(16), located opposite the separator outflows, at an angle .alpha. of 0~ - 45~ relative to the normal to the container wall. Such a separator can be used in the manufacturing process for acrylic acid through catalytic vapour-phase oxidation of propene.
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公开(公告)号:ID17416A
公开(公告)日:1997-12-24
申请号:ID972713
申请日:1997-08-05
Applicant: BASF AG
Inventor: HEIDA BERND , THIESSEN FRITZ , HAMMON ULRICH , DAMS ALBRECHT
Abstract: PCT No. PCT/EP97/04214 Sec. 371 Date Feb. 4, 1999 Sec. 102(e) Date Feb. 4, 1999 PCT Filed Aug. 1, 1997 PCT Pub. No. WO98/05622 PCT Pub. Date Feb. 12, 1998A process for isolating acrylic acid forward during catalytic gas phase oxidation of propene, which entails separating acrylic acid from the gas phase oxidation reaction using an absorbent containing biphenyl, diphenyl ether or dimethyl phthalate; and extracting acrylic acid from acid water of the gas phase reaction with a solvent containing biphenyl, diphenyl ether or dimethyl phthalate.
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公开(公告)号:BRPI0607566B1
公开(公告)日:2016-03-29
申请号:BRPI0607566
申请日:2006-03-01
Applicant: BASF AG
Inventor: PETZOLDT JOCHEN , MÜLLER-ENGEL KLAUS JOACHIM , DIETERLE MARTIN , HAMMON ULRICH
IPC: C07C57/05
Abstract: processo para a preparação de pelo menos um composto alvo orgânico, e, aparelho. a invenção refere-se a um processo para a produção de um composto alvo orgânico pela realização de uma oxidação parcial em fase gasosa heterogeneamente catalisada em um composto precursor orgânico com oxigénio molecular nos percursos de reator de oxidação que são operados em paralelo, e eliminação do composto alvo da mistura dos fluxos de gás de produto em um percurso de reprocessamento. o catalisador alimentado a um dos percursos de oxidação contém uma quantidade parcial de catalisador na qual a oxidação parcial em fase gasosa heterogeneamente catalisada já tenha sido realizada em mais que as quantidades parcial de catalisador alimentado para o outro percurso de reator de oxidação.
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公开(公告)号:CZ303338B6
公开(公告)日:2012-08-08
申请号:CZ20013233
申请日:2000-02-28
Applicant: BASF AG
Inventor: UNVERRICHT SIGNE , ARNOLD HEIKO , TENTEN ANDREAS , HAMMON ULRICH , NEUMANN HANS-PETER , HARTH KLAUS
IPC: B01J23/88 , C07C27/14 , B01J23/00 , B01J23/31 , B01J23/887 , B01J35/00 , C07B61/00 , C07C45/35 , C07C47/22 , C07C51/215 , C07C51/25 , C07C57/04 , C07C57/05 , C07C57/055
Abstract: Zpusob katalytické oxidace plynných fází propenu na kyselinu akrylovou spocívá v tom, že se výchozí smes reakcního plynu se zvýšeným zatížením propenem oxiduje v prvním reakcním stupni na prvním pevne uloženém katalyzátoru a následne se oxiduje akrolein obsahující produkcní smes z prvního reakcního stupne ve druhém reakcním stupni za zvýšeného zatížení akroleinem na druhém pevne uloženém katalyzátoru, pricemž katalyzátorové tvarové teleso má v obou reakcních stupních prstencový tvar.
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