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公开(公告)号:DE19807079A1
公开(公告)日:1999-08-26
申请号:DE19807079
申请日:1998-02-20
Applicant: BASF AG
Inventor: JACHOW HARALD , TENTEN ANDREAS , UNVERRICHT SIGNE , ARNOLD HEIKO
IPC: B01J23/00 , C07C45/33 , C07C51/215 , C07C59/66 , C07C69/716 , C07C69/734 , C07C57/05 , B01J23/882 , B01J23/887 , B01J23/888 , C07C45/28 , C07C47/22
Abstract: Heterogeneous, catalytic, gas-phase oxidation of propane to acrolein and/or acrylic acid comprises passing a mixture of propane, oxygen and optionally an inert gas, at 300-500 deg C, over a two-part fixed-bed catalyst, each part containing different, specific mixed metal oxide phases. The catalyst in the first bed (A) has the formula M a Mo1-bM b Ox (I) M = cobalt, nickel, magnesium, manganese and/or copper; M = wolfram, vanadium, tellurium, niobium, phosphorus, chromium, iron, antimony, cerium, tin and/or lanthanum; a = 0.5-1.5; b = 0-0.5; x = a number required to satisfy the valencies of the other components and the catalyst in the second bed (B) has formula Bia,Mob, X c, X d, X e, X f, X g, X h, Ox, (II) X = wolfram, vanadium and/or tellurium; X = alkaline earth metal, cobalt, nickel, zinc, manganese, copper, cadmium, tin and/or mercury; X = iron, chromium and/or cerium; X = phosphorus, arsenic, antimony and/or boron; X = alkali metal, thallium and/or tin; X = rare earth metal, titanium, zirconium, niobium, tantalum, rhenium, ruthenium, rhodium, silver, gold, aluminum, gallium, indium, silicon, germanium, thorium and/or uranium; a' = 0.01-8; b' = 0.1-30; c', d' and e' = 0-20; f' = 0-6; g' = 0-4; h' = 0-15 The starting mixture of reactants contains at least 5 volume % propane, at least 15 volume % oxygen and 0-35 volume % inert gas and it passes through layer A first, then through B.
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公开(公告)号:CA2675506A1
公开(公告)日:2008-07-24
申请号:CA2675506
申请日:2008-01-14
Applicant: BASF AG
Inventor: WOELFERT ANDREAS , DRIESS HEINZ , JACHOW HARALD
Abstract: The invention relates to a reactor (1) and a method for continuously prod ucing H2S by reacting a feedstock mixture essentially containing gaseous sul fur and hydrogen on a catalyst. The reactor (1) comprises a sulfur melt (9), at least in a bottom subarea (8) of the reactor (1) into which gaseous hydr ogen is introduced. The catalyst is arranged in at least one U-shaped tube ( 21) that is in partial contact with the sulfur melt (9). The at least one U- shaped tube (21) has at least one inlet (23) on a leg (26) above the sulfur melt (9), the feedstock mixture being able to penetrate from a feedstock zon e (10) of the reactor (1) into the U-shaped tube (21) through said inlet (23 ). The at least one U-shaped tube (21) also has an internal flow path, along which the feedstock mixture can be reacted in a reaction zone containing th e catalyst (22), and at least one outlet (24) in another leg (27), a product being able to be discharged into a product zone (7) through said outlet (24 ).
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公开(公告)号:DE59901820D1
公开(公告)日:2002-07-25
申请号:DE59901820
申请日:1999-08-10
Applicant: BASF AG
Inventor: MACHHAMMER OTTO , TENTEN ANDREAS , JACHOW HARALD , HAUPT SUSANNE , ARNOLD HEIKO , UNVERRICHT SIGNE
IPC: C07C45/33 , C07C45/35 , C07C47/22 , C07C51/215 , C07C51/25 , C07C57/04 , C07C27/14 , C07C57/05 , C07C57/055
Abstract: In a process for the preparation of acrolein and/or acrylic acid from propane, the propane is subjected, in a first reaction stage, to an oxydehydrogenation with molecular oxygen under homogeneous and/or heterogeneous catalysis to give propene and the product gas mixture formed in the first reaction stage is then used for the preparation of acrolein and/or acrylic acid by gas-phase catalytic propene oxidation.
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公开(公告)号:DE59900495D1
公开(公告)日:2002-01-17
申请号:DE59900495
申请日:1999-02-11
Applicant: BASF AG
Inventor: JACHOW HARALD
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公开(公告)号:BR9914612A
公开(公告)日:2001-08-07
申请号:BR9914612
申请日:1999-08-10
Applicant: BASF AG
Inventor: MACHHAMMER OTTO , TENTEN ANDREAS , JACHOW HARALD , HAUPT SUSANNE , ARNOLD HEIKO , UNVERRICHT SIGNE
IPC: C07C27/12 , C07B61/00 , C07C5/48 , C07C11/06 , C07C45/28 , C07C45/33 , C07C45/35 , C07C47/22 , C07C51/215 , C07C51/25 , C07C57/05 , C07C57/055 , C07C5/333
Abstract: In a process for the preparation of acrolein and/or acrylic acid from propane, the propane is subjected, in a first reaction stage, to a partial oxydehydrogenation with molecular oxygen under homogeneous and/or heterogeneous catalysis to give propene and the product gas mixture formed in the first reaction stage is then used for the preparation of acrolein and/or acrylic acid by gas-phase catalytic propene oxidation.
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公开(公告)号:AU5512699A
公开(公告)日:2000-03-14
申请号:AU5512699
申请日:1999-08-10
Applicant: BASF AG
Inventor: MACHHAMMER OTTO , TENTEN ANDREAS , JACHOW HARALD , HAUPT SUSANNE , ARNOLD HEIKO , UNVERRICHT SIGNE
IPC: C07C27/12 , C07B61/00 , C07C5/48 , C07C11/06 , C07C45/28 , C07C45/33 , C07C45/35 , C07C47/22 , C07C51/215 , C07C51/25 , C07C57/05 , C07C57/055 , C07C5/333
Abstract: In a process for the preparation of acrolein and/or acrylic acid from propane, the propane is subjected, in a first reaction stage, to a partial oxydehydrogenation with molecular oxygen under homogeneous and/or heterogeneous catalysis to give propene and the product gas mixture formed in the first reaction stage is then used for the preparation of acrolein and/or acrylic acid by gas-phase catalytic propene oxidation.
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公开(公告)号:DE19837520A1
公开(公告)日:2000-02-24
申请号:DE19837520
申请日:1998-08-19
Applicant: BASF AG
Inventor: MACHHAMMER OTTO , TENTEN ANDREAS , JACHOW HARALD , HAUPT SUSANNE , ARNOLD HEIKO , UNVERRICHT SIGNE
IPC: C07C45/33 , C07C45/35 , C07C51/215 , C07C51/25 , C07C57/055 , C07C5/333 , C07C11/06 , C07C47/22
Abstract: In the production of acrolein and/or acrylic acid from propane, the oxygen required in reaction stage 1 (catalytic dehydrogenation to propene) is supplied in the form of air and at least some of the nitrogen in the stage 1 product is removed before this gas mixture is used for subsequent catalytic gas-phase oxidation of the propene content. A process for the production of acrolein (AC) and/or acrylic acid (AA) from propane, involving (1) partial oxydehydrogenation to propene with molecular oxygen using homogeneous and/or heterogeneous catalysts and (2) catalytic gas-phase oxidation of the propene in the gas mixture obtained to give AC and/or AA. In this process, the molecular oxygen required in stage 1 (other than circulating oxygen) is added to the starting gas mixture in the form of air, and at least some of the nitrogen is separated from the stage 1 product before this is used in stage 2.
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公开(公告)号:DE19837518A1
公开(公告)日:2000-02-24
申请号:DE19837518
申请日:1998-08-19
Applicant: BASF AG
Inventor: MACHHAMMER OTTO , TENTEN ANDREAS , JACHOW HARALD , HAUPT SUSANNE , ARNOLD HEIKO , UNVERRICHT SIGNE
IPC: C07C27/12 , C07B61/00 , C07C5/48 , C07C11/06 , C07C45/33 , C07C45/35 , C07C47/22 , C07C51/215 , C07C51/25 , C07C57/05 , C07C57/055 , C07C5/333
Abstract: In the production of acrolein and/or acrylic acid from propane, the oxygen required in reaction stage 1 (catalytic dehydrogenation to propene) is supplied as nitrogen-containing modified air containing less N2 and more O2 than normal air and some of the N2 in the stage 1 product is removed before this product is used in further stages (propene oxidation). A process for the production of acrolein (AC) and/or acrylic acid (AA) from propane, involving (1) partial oxydehydrogenation to propene with molecular oxygen using homogeneous and/or heterogeneous catalysts and (2) catalytic gas-phase oxidation of the propene-containing product gas in further stage(s) to give AC and/or AA. In this process, the molecular oxygen required in stage 1 (other than circulating oxygen) is added to the starting gas mixture in the form of nitrogen-containing modified air with a lower N2 content and a higher O2 content than normal air, and at least some of the molecular N2 in the product mixture from stage 1 is removed before this mixture is used in stage(s) 2.
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公开(公告)号:AU2724999A
公开(公告)日:1999-09-06
申请号:AU2724999
申请日:1999-02-11
Applicant: BASF AG
Inventor: JACHOW HARALD
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公开(公告)号:DE19807269A1
公开(公告)日:1999-08-26
申请号:DE19807269
申请日:1998-02-20
Applicant: BASF AG
Inventor: JACHOW HARALD
IPC: B01J23/00 , B01J23/882 , B01J23/887 , B01J35/10 , C01G1/02 , C01G39/00 , C01G51/00 , C01G53/00 , C07C5/48 , B01J23/76 , C07C5/333 , C07C11/06
Abstract: Multimetal oxide compositions, comprising molybdenum (Mo) modified with other specified element(s), have an average pore diameter /g. Multimetal oxide compositions of formula (I) have an average pore diameter /g: M aMo1-bM bOx (I) M = cobalt (Co), nickel (Ni), magnesium (Mg), zinc (Zn), manganese (Mn) and/or copper (Cu); M = tungsten (W), vanadium (V), tellurium (Te), niobium (Nb), phosphorus (P), chromium (Cr), iron (Fe), antimony (Sb), cerium (Ce), tin (Sn) and/or lanthanum (La); a = 0.5 - 1.5; b = 0 - 0.5; x = a valency depending on the valency and content of elements other than oxygen (O).
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