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公开(公告)号:DE10051419A1
公开(公告)日:2002-04-18
申请号:DE10051419
申请日:2000-10-17
Applicant: BASF AG
Inventor: BORGMEIER FRIEDER , TENTEN ANDREAS , HIBST HARTMUT
IPC: B01J27/057 , B01J37/02 , C07B61/00 , C07C45/33 , C07C45/35 , C07C51/215 , C07C57/05 , B01J23/24 , B01J23/34 , B01J23/652 , B01J23/887
Abstract: Acrolein and acrylic acid are produced from propane and propene by absorption/desorption of propane and propene from a gas mixture followed by oxidation, in which no heterogeneously catalyzed dehydrogenation of propane occurs between the desorption and oxidation stages without addition of oxygen. Acrolein and acrylic acid are produced from propane and propene by: (a) separation of propane and propene from a gas mixture (A) by absorption in an absorption medium; (b) separation of propane and propene from the absorbent to give a mixture (B) containing propane and propene; and (c) using mixture (B) for oxidation to the required product(s). In this process, no catalytic dehydrogenation of propane without the addition of oxygen is carried out between stages (b) and (c).
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公开(公告)号:DE10033121A1
公开(公告)日:2002-01-17
申请号:DE10033121
申请日:2000-07-07
Applicant: BASF AG
Inventor: BORGMEIER FRIEDER , TENTEN ANDREAS , HIBST HARTMUT , MUELLER-ENGEL KLAUS JOACHIM
IPC: C07C45/33 , C07C45/35 , C07C57/05 , B01J27/057
Abstract: Acrolein and acrylic acid are produced from propane and propene by absorption/desorption of propane and propene from a gas mixture followed by oxidation, in which no heterogeneously catalyzed dehydrogenation of propane occurs between the desorption and oxidation stages without addition of oxygen. Acrolein and acrylic acid are produced from propane and propene by: (a) separation of propane and propene from a gas mixture (A) by absorption in an absorption medium; (b) separation of propane and propene from the absorbent to give a mixture (B) containing propane and propene; and (c) using mixture (B) for oxidation to the required product(s). In this process, no catalytic dehydrogenation of propane without the addition of oxygen is carried out between stages (b) and (c).
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公开(公告)号:DE10029338A1
公开(公告)日:2002-01-03
申请号:DE10029338
申请日:2000-06-20
Applicant: BASF AG
Inventor: BORGMEIER FRIEDER , TENTEN ANDREAS , HIBST HARTMUT , MUELLER-ENGEL KLAUS JOACHIM
Abstract: Acrolein and acrylic acid are produced from propane and propene by absorption/desorption of propane and propene from a gas mixture followed by oxidation, in which no heterogeneously catalyzed dehydrogenation of propane occurs between the desorption and oxidation stages without addition of oxygen. Acrolein and acrylic acid are produced from propane and propene by: (a) separation of propane and propene from a gas mixture (A) by absorption in an absorption medium; (b) separation of propane and propene from the absorbent to give a mixture (B) containing propane and propene; and (c) using mixture (B) for oxidation to the required product(s). In this process, no catalytic dehydrogenation of propane without the addition of oxygen is carried out between stages (b) and (c).
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公开(公告)号:AU5036201A
公开(公告)日:2001-09-24
申请号:AU5036201
申请日:2001-03-06
Applicant: BASF AG
Inventor: WEIGUNY JENS , STORCK SEBASTIAN , TENTEN ANDREAS
IPC: C07D307/60 , B01J27/198 , B01J35/00 , B01J35/02 , C07B61/00 , C07C51/215 , C07C51/25 , C07C57/145
Abstract: A catalyst used in a process for preparing maleic anhydride by heterogeneously catalyzed gas-phase oxidation of a hydrocarbon having at least four carbon atoms by means of oxygen-containing gases comprises a catalytically active composition comprising vanadium, phosphorus and oxygen and has a essentially hollow cylindrical structure in which (a) the ratio of the height h to the diameter of the continuous hole d2 is not more than 1.5 and (b) the ratio of the geometric surface area Ageo to the geometric volume Vgeo is at least 2 mm-1.
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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:AU2673001A
公开(公告)日:2001-06-18
申请号:AU2673001
申请日:2000-12-11
Applicant: BASF AG
Inventor: BITTERLICH STEFAN , VOSS HARTWIG , HIBST HARTMUT , TENTEN ANDREAS , VOIGT INGOLF , PIPPARDT UTE
IPC: C07D307/60 , B01D69/04 , B01D69/06 , B01D69/12 , B01D71/02 , B01J20/28 , B01J23/00 , B01J23/34 , B01J27/198 , B01J35/02 , B01J35/06 , C07B41/00 , C07B61/00 , C07C5/48 , C07C45/35 , C07C45/38 , C07C51/215 , C07C51/25 , C07C51/265 , C07C253/24 , C07C253/26 , C07C253/28 , C07D307/89 , B01J35/00
Abstract: Reactor membranes advantageously useful in oxidation reactions of hydrocarbons involving oxygen comprise a selective oxidation catalyst on a mixed conducting, oxide ion selective ceramic membrane of the composition (Sr1-xCax)1-yAyMn1-zBzO3-delta, where A is Ba, Pb, Na, K, Y, an element of the lanthanide group or a combination thereof, B is Mg, Al, Ga, In, Sn, an element of the 3d or 4d period or a combination thereof, x is from 0.2 to 0.8, y is from 0 to 0.4, z is from 0 to 0.6, and delta is a number, dependent on x, y and z, that renders the composition charge neutral.
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公开(公告)号:DE19927624A1
公开(公告)日:2000-12-21
申请号:DE19927624
申请日:1999-06-17
Applicant: BASF AG
Inventor: UNVERRICHT SIGNE , ARNOLD HEIKO , TENTEN ANDREAS , HAMMON ULRICH , NEUMANN HANS-PETER , HARTH KLAUS
IPC: C07C45/35 , C07C57/055 , C07C57/05 , B01J23/887
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:SG75800A1
公开(公告)日:2000-10-24
申请号:SG1996010394
申请日:1996-07-31
Applicant: BASF AG
Inventor: TENTEN ANDREAS , HIBST HARTMUT , MAROSI KASZLO
IPC: B01J23/88 , B01J23/00 , B01J23/887 , B01J23/888 , B01J35/00 , C01G31/00 , C01G39/00 , C07B61/00 , C07C51/235 , C07C51/25 , C07C57/05 , C07C57/055 , B01J23/885
Abstract: Multi-metal oxide compsn. of general formula ÄAÜpÄBÜq (I) is new (where, A = Mo12Va(X b)(X c)(X d)X e)(X f )(X g)Ox, B = X 12CuhHiOy (promoter phase); X = W, Nb, Ta, Cr and/or Ce; X = Cu, Ni, Co, Fe, M n and/or Zn; X = Sb and/or Bi; X = Li, Na, K, Rb, Cs and/or H; X = Mg, Ca, Sr and/or Br; X = Si, Al, Ti and/or Zr; X = Mo, W, V, Nb and/or Ta; a = 1-8; b = 0.2-5; c = 0-23; d = 0-50; e = 0-2; f = 0-5; g = 0-50; h = 4-30; i = 0-20; x, y = values determining the valency and frequency of elements different from oxygen in the compsn.; and p, q = values other than zero, whose ratio p/q = 160-1:1. The proportions of (A)p and (B)q are in the form of chemical compsns. differing from their local environment. A and B are distributed relative to each other such as a mixt. of finely divided A and finely divided B, with the proviso that B contains crystals B* of oxometallates of formula CuMoaWbVcNbdTeOy (II) (where, a/(A+B+C+D+E)=0.7-1.3; (B+C+D+E)/A = 0.01-1; and Y = a value determined by the valency and frequency of elements in (II) different from oxygen) of a new structure type (HT-Cu molybdate) defined by the X-ray diffraction pattern: d(A)=6.79+/-0.3; 3.56+/-0.3; 3.54+/-0.3, 3.40+/-0.3; 3.04+/-0.3, 2.96+/-0.3; 2.67+/-0.2; 2.66+/-0.2; 2.56+/-0.2, 2.36+/-0.2; 2.35+/-0.2; 2.27+/-0.2; 2.00+/-0.2;1.87+/-0.3; 1.70+/-0.2; 1.64+/-0.2; 1.59+/-0.2; 1.57+/-0.2; 1.57+/-0.2; 1.55+/-0.2; 1.51+/-0.2; 1.44+/-0.2. Also claimed are: (i) the oxometallates of formula (II); (ii) mixt. of oxometallates (II); (iii) prodn. of the multi-metal oxide compsn..
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公开(公告)号:BR9813872A
公开(公告)日:2000-09-26
申请号:BR9813872
申请日:1998-10-05
Applicant: BASF AG
Inventor: JACHOW HARAL , TENTEN ANDREAS , UNVERRICHT SIGNE , ARNOLD HEIKO
IPC: B01J23/88 , B01J23/00 , C07B61/00 , C07C45/33 , C07C47/22 , C07C51/215 , C07C57/04 , C07C57/05 , C07C57/055 , C07C59/66 , C07C69/716 , C07C69/734
Abstract: In a process for heterogeneously catalyzed gas-phase oxidation, a reaction gas starting mixture comprising propane, molecular oxygen and, if desired, inert gas is passed at from 300 to 500° C. over a fixed-bed catalyst.
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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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