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公开(公告)号:DE19839782A1
公开(公告)日:2000-03-02
申请号:DE19839782
申请日:1998-09-01
Applicant: BASF AG
Inventor: UNVERRICHT SIGNE , ARNOLD HEIKO , TENTEN ANDREAS , MACHHAMMER OTTO , ZEHNER PETER
Abstract: A metallic reactor tube with a catalytic coating of multi-metal oxide material containing molybdenum and bismuth, directly applied to the tube. Independent claims are also included for (a) a pipe bundle reactor with reactor tubes as defined; (b) a process for the production of coated reactor tubes or pipe bundle reactors, comprising (1) preparation of solutions, emulsions and/or dispersions of the elements and/or their compounds required for the catalyst and/or its precursor, (2) possible addition of coupling agents, binders, viscosity regulators and/or pH regulators, (3) application to the tube(s), preferably on the inside, preferably by spraying or dip-coating and (4) drying and possibly sintering or calcining by heating the coated tube at 20-1500 (preferably 200-400) deg C, optionally in presence of inert or reactive gas; (c) a process for the production of (meth)acrolein and/or (meth)acrylic acid by the catalytic gas-phase oxidation of 1-6C alkanes, 2-6C alkenes, 1-6C alkanols and/or alkanals and/or precursors thereof, using a reactor tube or pipe bundle reactor as above.
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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:ES2139266T3
公开(公告)日:2000-02-01
申请号:ES96103300
申请日:1996-03-04
Applicant: BASF AG
Inventor: HEFNER WERNER , MACHHAMMER OTTO , NEUMANN HANS-PETER , TENTEN ANDREAS , RUPPEL WILHELM , VOGEL HERBERT
IPC: C07C47/22 , C07B61/00 , C07C5/333 , C07C11/06 , C07C45/33 , C07C45/35 , C07C51/215 , C07C51/25 , C07C57/04 , C07C57/05 , C07C57/055
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:DE19806848A1
公开(公告)日:1999-08-19
申请号:DE19806848
申请日:1998-02-18
Applicant: BASF AG
Inventor: HIBST HARTMUT , TENTEN ANDREAS , DEMUTH DIRK , SCHUETH FERDI
IPC: B01J8/06 , B01J19/00 , B01J35/00 , B01J35/04 , C07B61/00 , C40B30/08 , C40B40/18 , C40B60/14 , B01J35/02 , B01J37/00 , B01J37/02
Abstract: Array of heterogeneous catalysts and/or their precursors (A) comprises a body having at least n channels, preferably arranged in parallel, passing through it, with n different (A) present in the channels (n is at least 2, preferably 10 and especially 10000). An Independent claim is also included for preparation of these arrays.
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公开(公告)号:DE19805719A1
公开(公告)日:1999-08-19
申请号:DE19805719
申请日:1998-02-12
Applicant: BASF AG
Inventor: HIBST HARTMUT , TENTEN ANDREAS , DEMUTH DIRK , SCHUETH FERDI
IPC: B01J8/06 , B01J19/00 , B01J23/31 , B01J35/00 , B01J35/04 , C07B61/00 , C07C45/35 , C07C51/25 , C40B30/08 , C40B40/18 , C40B60/14 , B01J37/02 , G01N31/10
Abstract: Array of heterogeneous catalysts and/or their precursors (A) comprises a body having at least n channels, preferably arranged in parallel, passing through it, with n different (A) present in the channels (n is at least 2, preferably 10 and especially 10000). An Independent claim is also included for preparation of these arrays.
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公开(公告)号:AU7209998A
公开(公告)日:1998-10-20
申请号:AU7209998
申请日:1998-03-24
Applicant: BASF AG
Inventor: HIBST HARTMUT , TENTEN ANDREAS
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公开(公告)号:ES2119293T3
公开(公告)日:1998-10-01
申请号:ES95118264
申请日:1995-11-21
Applicant: BASF AG
Inventor: TENTEN ANDREAS , WEIDLICH PETER , LINDEN GERD
IPC: B01J23/34 , B01J21/16 , B01J23/88 , B01J23/885 , B01J23/887 , B01J27/192 , B01J35/00 , B01J35/02 , B01J35/08 , B01J35/10 , B01J37/02 , C07B61/00 , C07C27/00 , C07C27/14 , C07C45/32 , C07C45/33 , C07C45/35 , C07C45/37 , C07C47/22 , C07C51/235 , C07C51/25 , C07C57/055
Abstract: A catalyst having a catalytically active oxide on the surface of a carrier is mfd. by moistening the carrier with a liq. binder consisting of a soln. of 10-80 wt.% of organic binder dissolved in 20-90 wt.% of H2O, contacting its surface with finely divided oxide particles, and removing the binding agent. The organic binder has a b.pt. or sublimation temp. of > 100 degrees C at atmos. pressure. Also claimed are: (i) a shell catalyst consisting of a hollow cylinder carrier 2-10 mm long with an external dia. 4-10 mm and a 1-4 mm wall thickness coated on its external surface with an oxide of general formula Mo12VaX bX cX dX eX fX 6gOn in which, X is W, Nb, Ta, Cr and/or Ce, X is Cu, Ni, Co, Fe, Mn and/or Zn, X is Sb and/or Bi, X is 1 or more alkali metals, X is 1 or more alkaline earth metals, X is Si, Al, Ti and/or Zr and a = 1-6, b = 0.2-4, c = 0.5-18, d = 0-40, e = 0-2, f = 0-4, g = 0-40 and n is a number determined by the valency and the abundance of the different elements in the general formula. The thickness of oxide is 10-1000 mu m, the specific active surface is 20-30 m /g and a value of cX dX eX fOn in which, X is Ni and/or Co, X is Tl, an alkali metal and/or an alkaline earth metal, X is P, As, B, Sb, Sn, Ce, Pb, Nb and/or W, X is Si, Al, Ti and/or Zr and a = 0.5-5, b = 0.01-3, c = 3-10, d = 0.02-2, e = 0-5, f = 0-10 and n is a number determined by the valency and the abundance of the different elements in the general formula.
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公开(公告)号:ID16006A
公开(公告)日:1997-08-28
申请号:ID963350
申请日:1996-11-15
Applicant: BASF AG
Inventor: HIBST HARTMUT , TENTEN ANDREAS , MAROSI LASZLO
IPC: C01G1/00 , B01J23/00 , B01J23/20 , B01J23/28 , B01J23/30 , B01J23/88 , B01J23/887 , B01J23/888 , B01J35/00 , C01G31/00 , C01G39/00 , C01G41/00 , C07B61/00 , C07C45/33 , C07C45/34 , C07C45/35 , C07C45/38 , C07C51/235 , C07C51/25 , C07C57/05 , C07C57/055 , B01J27/00
Abstract: A multimetal oxide of formula (I) Mo12-a-b-cVaM bM cOx is new, where: M = tungsten (W) and/or niobium (Nb); M = titanium (Ti), zirconium (Zr), hafnium (Hf), tantalum (Ta), chromium (Cr), silicon (Si) and/or germanium (Ge); a = 0.1-6; b = 0-6; c = 0-6; a+b+c = 0.1-6; and x = number determined by the valency and frequency of the element in (I) except oxygen. Its atomic space arrangement is determined by powder X-ray diffraction (the intensity A of the diffracted X-ray beam as a function of two-fold diffraction angle (2&thetas; )) using Cu-K alpha -radiation ( lambda = 1.54178 Angstrom ), so that in the 2&thetas; region of 5-50 degrees the following diffraction lines are produced: Al(X-ray diffraction line) = 8.3 plus or minus 0.7 (2&thetas; degrees ); A2=14.4 plus or minus 0.7; A3=22.3 plus or minus 0.2; A4=23.5 plus or minus 0.7; A5=27.2 plus or minus 0.4; A6=32.0 plus or minus 0.8; A7=34.8 plus or minus 0.6; A8=38.7 plus or minus 0.5; A9=45.4 plus or minus 0.4; and A10=48.8 plus or minus 0.4. Also claimed are: (i) a process for catalytic gas phase oxidation of organic compounds using the above multimetal oxide; and (ii) a finely divided mixture containing the above multimetal oxide (I) and a multimetal oxide (II) of formula: M 12CudHeOy, where: M = molybdenum (Mo), W, vanadium (V), Nb and/or Ta; d = 4-30; e = 0-20; and y = a number determined by the valency and frequency of the elements in (II) except oxygen.
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公开(公告)号:CZ9503112A3
公开(公告)日:1997-07-16
申请号:CZ311295
申请日:1995-11-24
Applicant: BASF AG
Inventor: TENTEN ANDREAS , WEIDLICH PETER , LINDEN GERD
IPC: B01J23/34 , B01J21/16 , B01J23/88 , B01J23/885 , B01J23/887 , B01J27/192 , B01J35/00 , B01J35/02 , B01J35/08 , B01J35/10 , B01J37/02 , C07B61/00 , C07C27/00 , C07C27/14 , C07C45/32 , C07C45/33 , C07C45/35 , C07C45/37 , C07C47/22 , C07C51/235 , C07C51/25 , C07C57/055
CPC classification number: C07C45/37 , B01J23/002 , B01J23/8876 , B01J23/8877 , B01J35/026 , B01J37/0215 , B01J37/0217 , B01J37/0223 , B01J2523/00 , C07C45/32 , C07C45/33 , C07C45/35 , C07C51/252 , Y10S502/523 , C07C47/22 , C07C57/04 , B01J2523/17 , B01J2523/55 , B01J2523/68 , B01J2523/69 , B01J2523/847
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