Abstract:
The invention relates to a hydrocyanic acid containing bioresource carbon, and to a method for producing a raw material mainly containing the same by reacting ammonia with methane or methanol optionally in the presence of air and/or oxygen, characterized in that at least one of the reagents selected from ammonia, methane and methanol is obtained from a biomass. The invention also relates to the uses of the raw material for producing acetone cyanohydrin, adiponitrile, methionine or methionine hydroxyl-analog, and sodium cyanide.
Abstract:
A process for producing prussic acid by subjecting methanol to a gas-phase contact reaction with molecular oxygen and ammonia in the presence of a catalyst, wherein said catalyst is an oxide composition containing iron, antimony, phosphorus and vanadium with a content of vanadium content being at least 0.6 in terms of atomic ratio relative to iron content taken as 10, and a mixed raw material gas for the gas-phase contact reaction contains oxygen at an oxygen-to-methanol molar ratio of less than 1.6.
Abstract:
An iron-antimony-phosphorus-containing metal oxide catalyst for the catalytic oxidation, comprising a crystalline iron antimonate, the catalyst being represented by the following empirical formula:Fe.sub.a Sb.sub.b P.sub.c X.sub.d Q.sub.e R.sub.f O.sub.g (SiO.sub.2).sub.hwherein X represents at least one element selected from the group consisting of V, Mo and W; Q represents at least one element selected from the group consisting of Li, Na, K, Rb, Cs, Be, Mg, Ca, Sr, Ba, Sc, Y, La, Ce, Pr, Nd, Sm, Th, U, Ti, Zr, Hf, Nb, Ta, Cr, Mn, Re, Co, Ni, Ru, Rh, Pd, Os, Ir, Pt, Cu, Ag, Au, Zn, Cd, Hg, Al, Ga, In, Tl, Ge, Sn and Pb; R represents at least one element selected from the group consisting of B, As, Bi, Se and Te; a, b, c, d, e, f, g and h each is an atomic ratio as follows:a=about 5 to 15b=about 5 to 100c=about 1 to 30d=about 0 to 10e=about 0 to 15f=about 0 to 10h=about 0 to 300g is a number of oxygen atom as determined corresponding to the oxides formed by combining the above-mentioned components; the atomic ratio of P/Fe is at least 0.3; the atomic ratio of P/Sb is at least 0.1; and the atomic ratio of P/X is at least 1 when d>0.
Abstract:
A process for the ammoxidation of methanol or formaldehyde to hydrogen cyanide or oxidation of methanol to formaldehyde using a catalyst comprising boron and phosphorus oxides, wherein the boron to phosphorus atomic ratio is 0.8:1 to 1.25:1.
Abstract:
An iron-antimony oxide catalyst for use in the production of hydrogen cyanide by the vapor phase catalytic ammoxidation of methanol, and a process for the production of hydrogen cyanide in the presence of said improved catalyst are disclosed. This improved iron-antimony oxide catalyst is represented by the following formula:Fe.sub.a Cu.sub.b Sb.sub.c V.sub.d Mo.sub.e W.sub.f P.sub.g Q.sub.h R.sub.i S.sub.j O.sub.k (SiO.sub.2).sub.lwhereinQ is at least one element selected from the group consisting of Mg, Zn, La, Ce, Al, Cr, Mn, Co, Ni, Bi, U and Sn;R is at least one element selected from the group consisting of B and Te;S is at least one element selected from the group consisting of Li, Na, K, Rb, Cs, Ca and Ba; anda, b, c, d, e, f, g, h, i, j, k and l each represents the atomic ratio of the elements in the formula for which they are subscript whereinfor a=10,b=0.5-5,c=12-30,d=0-3,e=0-15,f=0-3,g=1-30,h=0-6,i=0-5,j=0-3,k=the number of oxygen atoms as determined corresponding to the oxide formed by combining the above-described elements, andl=25-200,and wherein c/g is more than 1.5 and iron antimony oxide is present as a crystalline phase.
Abstract:
Promoted bismuth rare earth molybdenum oxide complexes are excellent catalysts for the ammoxidation of methanol to HCN especially at high methanol throughputs at contact times appropriate for fluid-bed operation.
Abstract:
A process for preparing hydrogen cyanide which comprises reacting methanol or formaldehyde or their mixture, ammonia and oxygen in the presence of a catalyst composition at a temperature of 250* to 550*C and a space velocity of 50 to 5,000 hr 1 under a pressure of 0.5 to 10 atm., the said catalyst composition comprising a catalyst system of the formula: MoaBibFecXdYeZfOg wherein X is one or more of Cr, Mn, Co, Ni, Zn, Cd, Sn, W and Pb, Y is one or more of Tl and elements belonging to Group IA or IIA in the periodic table, Z is one or more of P, As and Sb and a, b, c, d, e, f and g represent respectively the number of atoms and are respectively 12, 0.1 to 24, 0 to 24, 0 to 15, 0 to 15, 0 to 5 and the total number of the oxygen atoms in the oxides of the other atoms.
Abstract:
A process for the ammoxidation of an alcohol feed, such as methanol, or a nitrile feed, such as propionitrile, or a mixture thereof, to form hydrogen cyanide uses a modified Mn—P catalyst having the following empirical formula: MnaP1AbOx where A=one or more of K, Ca, Mo, Zn, Fe or mixtures thereof; a=1 to 1.5; b=0.01 to 1.0 and x is a total number of oxygen atoms determined by the oxidation states of the other elements present.
Abstract translation:醇进料如甲醇或腈进料(如丙腈或其混合物)氨氧化形成氰化氢的方法使用具有以下经验式的改性Mn-P催化剂:MnaP1AbOx其中A = 1 或更多的K,Ca,Mo,Zn,Fe或其混合物; a = 1〜1.5; b = 0.01〜1.0,x是由其他元素的氧化态决定的氧原子总数。
Abstract:
A process for the ammoxidation of an alcohol feed, such as methanol, or a nitrile feed, such as propionitrile, or a mixture thereof, to form hydrogen cyamide uses a modified Mn—P catalyst having the following empirical formula: MnaP1AbOx where A=one or more of K, Ca, Mo, Zn, Fe or mixtures thereof; a=1 to 1.5; b=0.01 to 1.0 and x is a total number of oxygen atoms determined by the oxidation states of the other elements present.