3.
    发明专利
    未知

    公开(公告)号:DD155484A5

    公开(公告)日:1982-06-16

    申请号:DD22395180

    申请日:1980-09-17

    Abstract: A process for preparing a supported solid oxide complex catalyst using silica as support characterised in that one adds fumed silica to a mixture containing one or more active components of the catalyst; dries said mixture to form a dried first-stage mixture; adds, in solution, silica or a silica-containing compound other than fumed silica to the dried first stage mixture optionally with further fumed silica; and dries and calcines the resulting mixture is provided. The use of fumed silica produces a supported solid oxide complex catalyst of increased attrition resistance. Such catalyst is useful in the preparation of unsaturated aldehydes and acids from propylene or isobutylene by vapour phase oxidation. The use of inert or recycle gas increases the performance of such catalyst in this reaction.

    METHOD FOR THE PREPARATION OF HIGH ACTIVITY PHOSPHOMOLYBDIC ACID BASED CATALYSTS

    公开(公告)号:CA1191828A

    公开(公告)日:1985-08-13

    申请号:CA401808

    申请日:1982-04-28

    Abstract: The present invention relates to a method for the preparation of phosphomolybdic acid based catalysts by forming a solution of hydrated phosphomolybdic acid in a substantially anhydrous alkyl alcohol, optionally adding a base to the solution, evaporating the solution to yield a catalyst powder and thereafter drying and calcining the powder to form the active catalyst. A second method for preparation is also provided and includes the steps of forming a solution of hydrated phosphomolybdic acid in a substantially anhydrous alkyl alcohol evaporating the solution to form a concentrate, impregnating a catalyst support material with the concentrate, contacting the impregnated support with ammonia gas in an amount sufficient to form an insoluble precipitate of ammonium alkyl phosphomolybdic acid within the pore structure of said support material and thereafter drying and calcining said impregnated support material so as to form a coated catalyst.

    PROCESS FOR THE PREPARATION OF DIOLEFINS FROM OLEFINS

    公开(公告)号:CA1037500A

    公开(公告)日:1978-08-29

    申请号:CA210722

    申请日:1974-10-03

    Abstract: PROCESS FOR THE PREPARATION OF DIOLEFINS FROM OLEFINS A catalyst is disclosed wherein the atomic ratios are disclosed by the empirical formula: Aa Cc Dd Fee Bif Mog Ox wherein A is chromium, tellurium, germanium, tungsten, manganese, thorium, niobium, praseodymium, cerium, lanthanum, zinc or mixture thereof; C is an alkali metal, alkaline earth metal, Tl, In, Ag, Cu, Sn, Sb, rare earth metal or mixture thereof; D is nickel, cobalt, magnesium, zinc, cadmium, manganese, calcium or mixture thereof; A is not the same as D; and wherein a is greater than zero to about 4; c is 0 to about 4; d is 0.1 to about 20; e and f are 0.01 to 12; g is 10 to 15; and x is the number of oxygens required by the valence states of the other elements present. This catalyst may be employed for the oxidative dehydrogenation of olefins of 1 to about 10 carbon atoms.

    REMOVAL OF AMMONIA AND ORGANIC IMPURITIES FROM AN AMMONIA PLANT EFFLUENT

    公开(公告)号:CA991383A

    公开(公告)日:1976-06-22

    申请号:CA173339

    申请日:1973-06-06

    Abstract: 1409599 Purifying NH 3 plant effluent STANDARD OIL CO 19 June 1973 [22 June 1972] 28937/73 Heading C1A A gas stream containing at least 90% by vol. steam and 0À1-10% by vol. of NH 3 and/or organic compounds with up to 6 carbon atoms is contacted with a catalyst containing the oxides of Cu, Fe, Mn, Bi, Ni, Co, U, Mo, V, Cr, W, Pd, Pt, Ag, Zn, alkali metal, alkaline earth metal, Sn and/or Sb at a temperature of 200-800‹ C. to oxidize the NH 3 or organic compound, wherein the said gas stream is obtained as a result of (a) stripping a hot K 2 CO 3 solution to form a gas stream containing H 2 O, CO 2 , together with NH 3 and/or the organic compounds, (b) condensing or washing the gas stream with H 2 O to form an aqueous stream containing NH 3 and/or the organic compounds and (c) steam stripping the aqueous stream to obtain the said gas stream containing NH 3 and/or the organic compounds. O 2 in the form of air is preferably added to the gas stream prior to catalysis. The K 2 CO 3 solution containing the CO 2 together with NH 3 and the organic compounds may be that formed on scrubbing a gas stream formed on catalytic oxidation of CH 4 with steam and air to form H 2 and CO 2 , in which case the organic compounds are CH 3 OH, HCOOH and HCHO.

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