Manufacture of multi-metal oxide composition, e.g. for hydrocarbon oxidation, involves preparing solutions containing specific metal complex, forming mixed solution stream, breaking formed stream into droplets, and calcining dried droplets

    公开(公告)号:DE10359027A1

    公开(公告)日:2005-05-25

    申请号:DE10359027

    申请日:2003-12-17

    Applicant: BASF AG

    Abstract: Solution streams are produced from solutions containing partial amounts of starting compounds of elemental constituents of multi-metal oxide composition, and combined to form a total solution stream (S1). S1 is mixed, to form a mixed solution stream (S2). S2 is broken into fine droplets and dried. The solid obtained is calcined at 200-1200[deg]C, to obtain a multi-metal oxide composition. At least two physically separate solutions containing partial amounts of starting compounds of elemental constituents of multi-metal oxide composition in dissolved form are prepared. Solution streams are produced from the obtained solution and combined, to form a total solution stream. The total solution stream is passed through a mixing zone and mixed solution stream comprising the total amount of the required starting compounds in dissolved form is formed. The mix solution stream is broken into fine droplets in the mixing zone or after discharging from the mixing zone. The fine droplets are contacted with hot gas and dried. The solid obtained is treated thermally at elevated temperature to obtain multi-metal oxide composition. The thermal treatment is calcination performed at 200-1200[deg]C. The multi-metal oxide composition has stoichiometry of: Mo1VaM1>bM2>cM3>dM4>eOn. M1>tellurium or antimony; M2>niobium, titanium, tungsten, tantalum, bismuth, zirconium or rhenium; M3>lead, nickel, cobalt, iron, palladium, silver, platinum, copper, gold, gallium, zinc, tin, indium, cerium, iridium, samarium, scandium, yttrium, praseodymium, neodymium or terbium; M4>lithium, sodium, potassium, rubidium, cesium, calcium, strontium or barium; a : 0.01-1; b, c, e : above 0-1; d : above 0-0.5; and n : number determined by the valence and abundance of elements other than oxygen. Independent claims are included for; (1) a multi-metal oxide composition; and (2) A method of heterogeneously catalyzed partial gas phase oxidation and/or ammoxidation of saturated and/or unsaturated hydrocarbon using the multi-metal oxide composition as active composition.

    23.
    发明专利
    未知

    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

    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.

    Heterogeneously catalyzed gas-phase partial oxidation of acrolein to acrylic acid, used to produce polymers for adhesives, involves using active multimetal oxide material containing e.g. molybdenum and vanadium

    公开(公告)号:DE10254279A1

    公开(公告)日:2004-06-03

    申请号:DE10254279

    申请日:2002-11-20

    Applicant: BASF AG

    Abstract: A heterogeneously catalyzed gas-phase partial oxidation of acrolein to acrylic acid over a catalytically active multimetal oxide material which contains the elements molybdenum and vanadium, tellurium or antimony, and elements consisting of niobium, tantalum, tungsten or titanium, whose X-ray diffraction pattern has no reflections with the peak position 2 theta = 50 +/- 0.30 but has reflections whose peaks are at specified diffraction angles. Heterogeneously catalyzed gas-phase partial oxidation of acrolein to acrylic acid over a catalytically active multimetal oxide material which contains the elements molybdenum and vanadium, tellurium or antimony, and elements consisting of niobium, tantalum, tungsten or titanium, whose X-ray diffraction pattern has no reflections with the peak position 2 theta = 50 +/- 0.30 but has reflections h, i and k whose peaks are at the diffraction angles (2 theta) 22.2 +/- 0.5 degrees (h), 27.3 +/- 0.50 (i) and 28.2 +/- 0.50 (k). The reflection (h ) is the one with the strongest intensity within the X-ray diffraction pattern and having a full width at half height of not more than 0.50; the intensity (Pi) of the reflection (i) and the intensity (Pk) of the reflection (k) fulfill the relationship that R is 0.65-0.85, where R is the intensity ratio defined by the formula R = Pi/(Pi + Pk); and the full width at half height of the reflection (i) and of the reflection (k) is in each case at most 10. The catalytically active multimetal oxide material is of formula (I). Mo1VaM1bM2cM3dOn (I). M1 = element(s) from the group consisting of Te and Sb; M2 = element(s) from the group consisting of Nb, Ti, W, Ta and Ce; M3 = element(s) consisting of Pb, Ni, Co, Bi, Pd, Ag, Pt, Cu, Au, Ga, Zn, Sn, In, Re, Ir, Sm, Sc, Y, Pr, Nd or Tb; a = 0.01-1; b = 0-1; c = 0-1; d = 0-0.5; n = number that is determined by the valency and frequency of the elements other than oxygen in formula (I).

    METHOD FOR THE PRODUCTION OF POLYETHEROLS

    公开(公告)号:AU2003267340A1

    公开(公告)日:2004-04-08

    申请号:AU2003267340

    申请日:2003-09-11

    Applicant: BASF AG

    Abstract: A process for preparation of polyetherols includes reaction of at least one alkylene oxide with at least one starter compound in the presence of a catalyst which is a multimetal oxide compound. A process for preparation of polyetherols includes reaction of at least one alkylene oxide with at least one starter compound in the presence of a catalyst, i.e. a multimetal oxide compound of formula (I). M1p(M2qOn(OH)2(3-n))x (I) M1 = at least 1 element from the groups IA, IIA, IIIA, IVA, VA, IB, IIB, IIIB, IVB, VB, VIB, VIIB and/or VIIIB; M2 = at least one element from groups IVA, VA and/or VIA, n = 2 or 3, p = 0 or fractional or whole number greater than 0, q = fractional or whole number greater than 0, x = 1-20 fractional or whole number. An Independent claim is included for a polyetherol obtained as above.

    Heterogeneously catalyzed gas-phase partial oxidation of acrolein to acrylic acid, used to produce polymers for adhesives, involves using active multimetal oxide material containing e.g. molybdenum and vanadium

    公开(公告)号:DE10254278A1

    公开(公告)日:2004-02-26

    申请号:DE10254278

    申请日:2002-11-20

    Applicant: BASF AG

    Abstract: A heterogeneously catalyzed gas-phase partial oxidation of acrolein to acrylic acid over a catalytically active multimetal oxide material which contains the elements molybdenum and vanadium, tellurium or antimony, and elements consisting of niobium, tantalum, tungsten or titanium, whose X-ray diffraction pattern has no reflections with the peak position 2 theta = 50 +/- 0.30 but has reflections whose peaks are at specified diffraction angles. Heterogeneously catalyzed gas-phase partial oxidation of acrolein to acrylic acid over a catalytically active multimetal oxide material which contains the elements molybdenum and vanadium, tellurium or antimony, and elements consisting of niobium, tantalum, tungsten or titanium, whose X-ray diffraction pattern has no reflections with the peak position 2 theta = 50 +/- 0.30 but has reflections h, i and k whose peaks are at the diffraction angles (2 theta) 22.2 +/- 0.5 degrees (h), 27.3 +/- 0.50 (i) and 28.2 +/- 0.50 (k). The reflection (h ) is the one with the strongest intensity within the X-ray diffraction pattern and having a full width at half height of not more than 0.50; the intensity (Pi) of the reflection (i) and the intensity (Pk) of the reflection (k) fulfill the relationship that R is 0.65-0.85, where R is the intensity ratio defined by the formula R = Pi/(Pi + Pk); and the full width at half height of the reflection (i) and of the reflection (k) is in each case at most 10. The catalytically active multimetal oxide material is of formula (I). Mo1VaM1bM2cM3dOn (I). M1 = element(s) from the group consisting of Te and Sb; M2 = element(s) from the group consisting of Nb, Ti, W, Ta and Ce; M3 = element(s) consisting of Pb, Ni, Co, Bi, Pd, Ag, Pt, Cu, Au, Ga, Zn, Sn, In, Re, Ir, Sm, Sc, Y, Pr, Nd or Tb; a = 0.01-1; b = 0-1; c = 0-1; d = 0-0.5; n = number that is determined by the valency and frequency of the elements other than oxygen in formula (I).

    30.
    发明专利
    未知

    公开(公告)号:DE59905239D1

    公开(公告)日:2003-05-28

    申请号:DE59905239

    申请日:1999-11-10

    Applicant: BASF AG

    Abstract: A multimetal oxide of the formula I Aga-bMbV2Ox*cH2O,  I where M is a metal selected from the group consisting of Li, Na, K, Rb, Cs, Tl, Mg, Ca, Sr, Ba, Cu, Zn, Cd, Pb, Cr, Au, Al, Fe, Co, Ni and/or Mo, a is from 0.3 to 1.9 and b is from 0 to 0.5, with the proviso that the difference (a−b)≧0.1 and c is from 0 to 20 and x is a number determined by the valence and amount of elements different from oxygen in the formula I, which has a crystal structure giving an X-ray powder diffraction pattern which displays reflections at the lattice spacings d of 15.23±0.6, 12.16±0.4, 10.68±0.3, 3.41±0.04, 3.09±0.04, 3.02±0.04, 2.36±0.04 and 1.80±0.04 Å. Precatalysts and catalysts produced therefrom for the partial oxidation of aromatic hydrocarbons are also provided.

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