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公开(公告)号:ZA200700832B
公开(公告)日:2008-11-26
申请号:ZA200700832
申请日:2007-01-30
Applicant: BASF AG
Inventor: DIETERLE MARTIN , MUELLER-ENGEL KLAUS , HECHLER CLAUS , HAMMON ULRICH , DIEFENBACHER ARMIN
IPC: C07C20090101 , C07C51/25
Abstract: The invention relates to a method for producing acrylic acid by means of two-stage heterogeneously catalyzed partial gas phase oxidation of propylene. According to said method, previously dehydrogenated propane is used as a propylene source while the first partial oxidation stage is operated so as to limit propylene reaction. Furthermore, unreacted propane and propylene contained in the product gas mixture of the second partial oxidation stage are largely redirected into the propane dehydrogenation process taking place upstream.
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公开(公告)号:ZA200700833B
公开(公告)日:2008-10-29
申请号:ZA200700833
申请日:2007-01-30
Applicant: BASF AG
Inventor: MACHHAMMER OTTO , SCHINDLER GOTZ-PETER , ADAMI CHRISTOPH , HECHLER CLAUS , DIETERLE MARTIN
IPC: C07C20090101 , C07C45/35 , C07C51/25
Abstract: A process for preparing acrolein or acrylic acid or a mixture thereof from propane, in which the propane is initially dehydrogenated under heterogeneous catalysis to give propene, secondary components are removed and the remaining gas mixture, comprising propane and propene, is subjected to the heterogeneously catalyzed partial oxidation to acrolein or acrylic acid or a mixture thereof as the target product, target product is removed from the product gas mixture and the remaining residual gas, comprising excess oxygen and unconverted propane, is recycled into the propane dehydrogenation in such a way that the other propane fed to the dehydrogenation is at least partly converted under dehydrogenating conditions at the recycle point.
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公开(公告)号:ES2276808T3
公开(公告)日:2007-07-01
申请号:ES01956472
申请日:2001-06-13
Applicant: BASF AG
Inventor: MACHHAMMER OTTO , ADAMI CHRISTOPH , HECHLER CLAUS , ZEHNER PETER
IPC: C07C27/14 , C07C45/33 , B01J23/00 , B01J23/28 , B01J23/31 , B01J23/34 , B01J23/652 , B01J23/656 , B01J23/88 , B01J27/057 , B01J37/02 , C07B61/00 , C07C5/333 , C07C5/48 , C07C7/11 , C07C11/06 , C07C27/00 , C07C45/35 , C07C47/22 , C07C51/215 , C07C51/25 , C07C57/04 , C07C57/05 , C07C57/07
Abstract: Un proceso para la preparación de acroleína y/o ácido acrílico a partir de propane, comprendiendo el proceso los siguientes pasos: (a) deshidrogenación homogénea y/o heterogénea de propano hasta propeno para dar lugar a propeno o a una mezcla A que comprende gas propano y propeno. (b) separación de propeno o propane de la mezcla de gas A mediante absorción sobre un absorbente. (c) separación del propeno o del propeno y propano del absorbente para dar lugar un propeno o un gas B que comprende propeno y propano y (d) uso del gas B obtenido en la etapa (c) para una oxidación de propeno hasta acroleína y/o ácido acrílico, en el cual no se lleva a cabo una deshidrogenación catalizada heterogéneamente de propano sin un suministro de oxígeno entre las etapas (c) and (d), y en el cual la hidrogenación se lleva a cabo oxidativamente y la etapa (d) tiene lugar directamente después de la etapa (c).
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公开(公告)号:BRPI0418085A
公开(公告)日:2007-04-17
申请号:BRPI0418085
申请日:2004-12-21
Applicant: BASF AG
Inventor: HECHLER CLAUS , OLBERT GERHARD , WEN DIETMAR L
IPC: C07C57/05 , C07C45/35 , C07C51/16 , C07C51/21 , C07C51/235
Abstract: A process is proposed for preparing (meth)acrolein and/or (meth)acrylic acid by partially oxidizing C 3 and/or C 4 precursor compounds in the gas phase in the presence of a heterogeneous particulate catalyst, in a reactor having two or more thermoplates ( 1 ) arranged vertically and parallel to each other while in each case leaving a gap ( 2 ), the heterogeneous particulate catalyst being installed in the gaps ( 2 ) and the gaseous reaction mixture being passed through the gaps ( 2 ), which comprises monitoring, controlling and/or regulating the process by selecting as a monitoring, control and/or regulation parameter one or more temperatures which are measured in one or more gaps ( 2 ), at one or more measurement points which are distributed over the height of each gap ( 2 ).
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公开(公告)号:DE102005009891A1
公开(公告)日:2006-09-07
申请号:DE102005009891
申请日:2005-03-01
Applicant: BASF AG
Inventor: DIETERLE MARTIN , MUELLER-ENGEL KLAUS-JOACHIM , HECHLER CLAUS , HAMMON ULRICH , DIEFENBACHER ARMIN
Abstract: Acrolein or acrylic acid is prepared by catalyzing partial gas phase oxidation of propene, where a starting reaction gas mixture having propylene and molecular oxygen reactants and inert molecular nitrogen and propane diluent gasses is conducted at elevated temperature through a fixed catalyst bed whose active composition is a multimetal oxide having molybdenum, iron and bismuth. Preparation of acrolein or acrylic acid involves catalyzing partial gas phase oxidation of propene, where a starting reaction gas mixture having propylene and molecular oxygen reactants and the inert molecular nitrogen and propane diluent gasses and having the molecular oxygen and the propylene in a molar oxygen;C 3H 6 ratio of >=1 is conducted at elevated temperature through a fixed catalyst bed whose active composition is a multimetal oxide having molybdenum, iron and bismuth based on its total volume of 6-9 vol.% propylene, 8-18 vol.% molecular oxygen. 6-30 vol.% propane and 32-72 vol.% molecular nitrogen. The molar ratio V 1 of propane in starting reaction gas mixture to propylene in starting reaction gas mixture is 1-4. The molar V 2 of molecular nitrogen present in starting reaction gas mixture to molecular oxygen in starting reaction the mixture is 2-6, and the molar ratio of the molecular oxygen in starting reaction gas mixture to propylene in starting reaction mixture is 1.3-2.4.
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46.
公开(公告)号:ZA200503358B
公开(公告)日:2006-07-26
申请号:ZA200503358
申请日:2005-04-26
Applicant: BASF AG
Inventor: ADAMI CHRISTOPH , HECHLER CLAUS , SCHINDLER GOETZ-PETER , PETZOLDT JOCHEN , MACHHAMMER OTTO , MUELLER-ENGEL KLAUS J , MARTAN HANS
IPC: C07C20060101 , C07C7/05 , C07C47/22 , C07C57/04 , C07C253/18 , C07C255/08 , C07D20060101 , C07D301/08 , C07D303/04
Abstract: Preparation of at least one partial oxidation and/or ammoxidation product of propylene involves subjecting crude propylene (prepared by dehydrogenation or oxydehydrogenation in the presence and/or absence of oxygen) in the presence of unconverted propane as a constituent of a gas mixture 2 which comprises a total 4C-hydrocarbon content of at most 3 vol.%, to a heterogeneously catalyzed gas phase partial oxidation and/or ammoxidation. Preparation of at least one partial oxidation and/or ammoxidation product of propylene involves: (a) subjecting crude propane in the presence of and/or absence of oxygen to a homogeneously and/or a heterogeneously catalyzed dehydrogenation and/or oxydehydrogenation to obtain a propane- and propylene-containing gas mixture 1; (b) optionally removing and/or converting to other compounds a portion of the constituents other than propane and propylene contained in the gas mixture 1 to obtain a gas mixture 1' comprising propane and propylene and also compounds other than oxygen, propane and propylene; and (c) subjecting gas mixture 1 and/or gas mixture 1' as a constituent of a gas mixture 2 to a heterogeneously catalyzed gas phase partial oxidation and/or partial gas phase ammoxidation of propylene contained in gas mixture 1 and/or 1'. The total content of 4C-hydrocarbons of gas mixture 2 is at most 3 vol.%.
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公开(公告)号:DE50008266D1
公开(公告)日:2004-11-18
申请号:DE50008266
申请日:2000-10-31
Applicant: BASF AG
Inventor: TENTEN ANDREAS , HIBST HARTMUT , MACHHAMMER OTTO , HECHLER CLAUS , MUELLER-ENGEL JOACHIM , UNVERRICHT SIGNE
IPC: C07C51/215 , C07B61/00 , C07C51/25 , C07C57/04 , C07C57/05
Abstract: In a process for the two-stage catalytic gas-phase oxidation of propene to acrylic acid, the reaction gas starting mixture is passed, in a tube-bundle reactor, with a propene loading of >=160 l (S.T.P.) of propene/l.h, first over a fixed catalyst bed 1 present in two successive temperature zones A, B and then over a fixed catalyst bed 2 which is housed either in one further temperature zone C or in two further temperature zones D, E, the temperature of the zone A being kept at a lower temperature than the zone B and the temperature of the zone D at a lower temperature than the zone E.
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公开(公告)号:AT266615T
公开(公告)日:2004-05-15
申请号:AT01907432
申请日:2001-01-10
Applicant: BASF AG
Inventor: HECHLER CLAUS , KAMMEL ULRICH , MACHHAMMER OTTO , OLBERT GERHARD , ZEHNER PETER
IPC: B01J8/02 , B01J19/24 , C07C51/265 , C07C51/31 , C07C57/145 , F28D9/00 , F28F13/08
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公开(公告)号:BR0103915A
公开(公告)日:2001-12-18
申请号:BR0103915
申请日:2001-01-10
Applicant: BASF AG
Inventor: ZEHNER PETER , MACHHMMER OTTO , HECHLER CLAUS , WECK ALEXANDRE , OLBERT ERHARD , STABEL UWE
IPC: F28F3/00 , B01J8/02 , B01J19/24 , B01J35/04 , C07C51/215 , C07C57/145 , C07D307/60
Abstract: A process for the preparation of maleic anhydride by heterogeneously catalyzed gas-phase oxidation in a reactor with feed for the reaction mixture at one end of the reactor and discharge of the product mixture at the opposite end of the reactor, and with devices for dissipating the heat of reaction which are arranged in the reactor interior and through which a heat-exchange medium flows and which are designed as heat-exchanger plates.
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公开(公告)号:DE19952964A1
公开(公告)日:2001-05-10
申请号:DE19952964
申请日:1999-11-03
Applicant: BASF AG
Inventor: HECHLER CLAUS , MACHHAMMER OTTO , OLBERT GERHARD , STABEL UWE , ZEHNER PETER
IPC: B01J8/02 , B01J19/24 , C07B61/00 , C07C27/00 , C07C45/33 , C07C45/35 , C07C45/37 , C07C47/22 , C07C51/235 , C07C57/05 , C07C57/055 , F28D9/00 , C07C45/27
Abstract: The invention relates to a method for the continuous gas phase oxidation of C3- and C4-precursors to (meth)acrolein and/or (meth)acrylic acid in the presence of a catalyst, in a reactor. Said reactor has a feed element for the reaction mixture at one reactor end and a discharge element for the reaction mixture at the opposite reactor end and is equipped with devices for dissipating the reaction heat inside the reactor. A heat exchanger agent flows through said devices, which are configured in the form of heat exchanger plates.
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