Abstract:
Disclosed is ammoxidation of C₃ to C₅ acyclic alkanes with NH₃ and O₂ using (1) a mole ratio of alkane:NH₃ in the range from 2 to 16 and a mole ratio of alkane:O₂ in the range 1 to 10 and (2) a mixture of particulate catalyst compositions, the first being especially effective to promote formation of an unsaturated nitrile and an olefin from the paraffin, and the second catalyst composition being especially effective to promote the conversion of the olefin to the unsaturated mononitrile. Catalyst compositions useful in the process are also disclosed.
Abstract:
Disclosed is ammoxidation of C₃ to C₅ acyclic alkanes with NH₃ and O₂ using (1) a mole ratio of alkane:NH₃ in the range from 2 to 16 and a mole ratio of alkane:O₂ in the range 1 to 10 and (2) a mixture of particulate catalyst compositions, the first being especially effective to promote formation of an unsaturated nitrile and an olefin from the paraffin, and the second catalyst composition being especially effective to promote the conversion of the olefin to the unsaturated nitrile. Catalyst compositions useful in the process are also disclosed.
Abstract:
Disclosed is ammoxidation of C₃ to C₅ acyclic alkanes with NH₃ and O₂ using (1) a mole ratio of alkane:NH₃ in the range from 2 to 16 and a mole ratio of alkane:O₂ in the range 1 to 10 and (2) a mixture of particulate catalyst compositions, the first being especially effective to promote formation of an unsaturated nitrile and an olefin from the paraffin, and the second catalyst composition being especially effective to promote the conversion of the olefin to the unsaturated mononitrile. Catalyst compositions useful in the process are also disclosed.
Abstract:
A method of preparing a catalyst having the elements and the proportions indicated by the following empirical formula:
VSb m A a D d O x
where
A is one or more Ti, Sn, where Sn is always present D is one or more Li, Mg, Ca, Sr, Ba, Co, Fe, Cr, Ga, Ni, Zn, Ge, Nb, Zr, Mo, W, Cu, Te, Ta, Se, Bi, Ce, In, As, B, Al and Mn wherein m is 0.5 to 10 a is greater than zero to 10 d is zero to 10 x is determined by the oxidation state of the cations present, comprising making an aqueous slurry of a mixture of source batch materials comprising compounds of said elements to be included in the final catalyst, followed by drying and heat calcining the mixture to an active catalyst, wherein the source batch material for the tin is a solution which comprises SnO 2 ·xH 2 O wherein x ≥ 0 dispersed in tetraalkyl ammonium hydroxide wherein the tetraalkyl ammonium hydroxide is defined by the following formula:
C n H 2n+1 NOH
wherein 5 ≥ n ≥ 1, drying said slurry and calcining the mixture to an upper calcination temperature of at least 500°C.
Abstract translation:通过制备所需元素化合物的混合物(II)的水性浆料,然后干燥并煅烧混合物以形成活性催化剂(I),制备含有氧化态的钒,锑和锡的催化剂(I)。 (II)是分散在式(CnH2n + 14NOH(1)的四烷基氢氧化铵中的SnO 2·xH 2 O(其中x> = 0)的溶液,还要求的是制备α,β-不饱和单腈,优选丙烯腈 或甲基丙烯腈在丙烷或异丁烷的气相中与氧和氨在催化剂(I)的存在下,通式为VSbmAaDdOx(2)的催化反应,石蜡与NH 3的摩尔比为2.5-16,摩尔比为 石蜡至O2为1-10,n = 1-5; A =总是存在Sn的Ti和/或Sn D = Li,Mg,Ca,Sr,Ba,Co,Fe,Cr,Ga,Ni,Zn, Ge,Nb,Zr,Mo,W,Cu,Te,Ta,Se,Bi,Ce,In,As,B,Al和/或Mn,m = 0.5-10; a = 0-10; d = 10; x由存在的阳离子的氧化态决定。
Abstract:
Disclosed is ammoxidation of C₃ to C₅ acyclic alkanes with NH₃ and O₂ using (1) a mole ratio of alkane:NH₃ in the range from 2 to 16 and a mole ratio of alkane:O₂ in the range 1 to 10 and (2) a mixture of particulate catalyst compositions, the first being especially effective to promote formation of an unsaturated nitrile and an olefin from the paraffin, and the second catalyst composition being especially effective to promote the conversion of the olefin to the unsaturated mononitrile. Catalyst compositions useful in the process are also disclosed.
Abstract:
Disclosed is ammoxidation of C₃ to C₅ acyclic alkanes with NH₃ and O₂ using (1) a mole ratio of alkane:NH₃ in the range from 2 to 16 and a mole ratio of alkane:O₂ in the range 1 to 10 and (2) a mixture of particulate catalyst compositions, the first being especially effective to promote formation of an unsaturated nitrile and an olefin from the paraffin, and the second catalyst composition being especially effective to promote the conversion of the olefin to the unsaturated mononitrile. Catalyst compositions useful in the process are also disclosed.