Heteropoly-acids and their production and use
    4.
    发明授权
    Heteropoly-acids and their production and use 失效
    杂多酸及其生产和使用

    公开(公告)号:US4565801A

    公开(公告)日:1986-01-21

    申请号:US371223

    申请日:1982-04-23

    摘要: A heteropoly-acid of the formula:H.sub.3+x (PMo.sub.12-x V.sub.x O.sub.40).nH.sub.2 Owherein x and n are numbers satisfying respectively the equations: 0.ltoreq.x.ltoreq.3 and n.ltoreq.6, and comprising phosphorus as the central atom and molybdenum or molybdenum and vanadium as the coordinating atoms, or its reduction-form product, which is in a cubic crystal structure having diffraction lines at lattice spacings (d) of at least 8.4, 6.8, 5.9, 4.8, 4.2 and 3.4 in the X-ray powder diffraction. The heteropoly-acid is useful as a catalyst, especially as a catalyst in the production of methacrylic acid by the gas-phase catalytic oxidation of methacrolein.

    摘要翻译: 具有下式的杂多酸:H3 + x(PMo12-xVxO40)·nH2O其中x和n分别满足等式:0≤x≤3和n≤6,并且包含磷作为 中心原子和钼或钼和钒作为配位原子,或其还原形式的产物,其在晶格间距(d)处具有至少8.4,6.8,5.9,4.8,4.2和3.4的衍射线的立方晶体结构 在X射线粉末衍射中。 杂多酸可用作催化剂,特别是通过甲基丙烯醛的气相催化氧化生产甲基丙烯酸时的催化剂。

    Catalytic process for the production of acrylonitrile
    6.
    发明授权
    Catalytic process for the production of acrylonitrile 失效
    用于生产丙烯腈的催化工艺

    公开(公告)号:US4058547A

    公开(公告)日:1977-11-15

    申请号:US302882

    申请日:1972-11-01

    摘要: In the production of acrylonitrile by a vapor phase reaction of propylene, ammonia and oxygen at an elevated temperature, a process which comprises contacting propylene, ammonia and oxygen with a catalyst composition comprising a catalyst system of the formula: Tl.sub.a P.sub.b Mo.sub.c Fe.sub.d Bi.sub.e X.sub.f O.sub.g wherein X represents one or more of the metals, Ni, Mg and Co, and a, b, c, d, e, f and g represent respectively the relative number of atoms of each component; provided that when c is 12, a is 2 or less, but not 0; b is 0 to 5; d is 0.1 to 5; e is 0.1 to 5; f is 2 to 15; and the value of g depends on the number of the other atoms and is usually from 38.3 to 81.5.

    摘要翻译: 在通过丙烯,氨和氧在升高的温度下的气相反应生产丙烯腈的过程中,包括使丙烯,氨和氧与包含下式催化剂体系的催化剂组合物接触的方法:其中X代表一个或多个 更多的金属,Ni,Mg和Co,以及a,b,c,d,e,f和g分别表示各成分的相对原子数。 条件是当c为12时,a为2或更小,但不为0; b为0〜5; d为0.1〜5; e为0.1〜5; f为2〜15; g的值取决于其他原子的数量,通常为38.3〜81.5。