Composite oxide catalyst and method of producing the same
View Patent ↗A composite oxide catalyst for the oxidation of an olefin containing Mo and Bi as essential components, characterized in that it has a specific surface area of 5 to 25 m 2 /g and a pore volume of 0.2 to 0.7 cc/g, and has a pore diameter distribution wherein the volume of the pores having a pore diameter of 0.03 to 0.1 μm accounts for 30% or more of the total pore volume, the volume of the pores having a pore diameter of 0.1 to 1 μm accounts for 20% or more of the total pore volume, and the volume of the pores having a pore diameter of less than 0.03 μm is 10% or less of the total pore volume; a composite oxide catalyst for use in the vapor phase catalytic oxidation of acrolein or methacrolein or the like which comprises Mo, Bi and a halogen; either of the above two composite oxide catalysts which comprises Mo, Bi, Fe, Si and an element selected from alkali metals and thallium, and optionally Co, Ni, Mg, Ca, Zn, Ce, Sm, a halogen, B, P, As and W; a method for preparing any of the above composite catalysts; and a method for using any of the above composite oxide catalysts.
1. A process which comprises oxidizing propylene to produce acrolein and/or acrylic acid, by vapor phase oxidation in the presence of a catalyst, wherein the catalyst is a composite oxide catalyst expressed by the following formula (1):
Mo a Bi b Co c Ni d Fe e X f Y g Z h Si i O j (1)
(wherein X is at least one kind of element selected from the group consisting of magnesium (Mg), calcium (Ca), zinc (Zn), cerium (Ce), samarium (Sm) and halogen, Y is at least one of element selected from the group consisting of sodium (Na), potassium (K), rubidium (Rb), cesium (Cs) and thallium (Tl), Z is at least one kind of element selected from the group consisting of boron (B), phosphorus (P), arsenic (As) and tungsten (W), the letters a to j are atomic ratios of the respective elements, where if a=12, then b=0.5-7, c=0-10, d=0-10 (where c+d=1-10), e=0.05-3, f=0-2, g=0.04-2, h=0-3 and i=5-48, and j is a numeral which satisfies the oxidation state of the other elements),
wherein the catalyst is produced by a process comprising incorporating supply source compounds of the respective elements into a composite in an aqueous solution, and subjecting the composite to heat treatment, comprising a pre-step for producing a catalyst precursor by heat-treating a raw material salt solution containing molybdenum equivalent to partial atomic ratio (a 1 ) of the entire atomic ratio (a) of molybdenum, at least one of iron, nickel and cobalt, and silicon or a dried article obtained by drying it, and an after-step in which said catalyst precursor, molybdenum equivalent to the remaining atomic ratio (a 2 ) after subtracting said a1 from the entire atomic ratio (a) of molybdenum, and a bismuth compound are incorporated together with an aqueous solution, and dried and calcined.
2. A process as claimed in claim 1 wherein the catalyst is produced by a process comprising incorporating supply source compounds of the respective elements into a composite in an aqueous solution, and subjecting the composite to heat treatment, wherein as at least part of a molybdenum supply source compound, an aqueous dispersion obtained by incorporating a molybdenum-containing compound and a silicon-containing compound in an aqueous solution is used.
3. A process as claimed in claim 1 wherein the catalyst is produced by a process comprising incorporating supply source compounds of the respective elements into a composite in an aqueous solution, and subjecting the composite to heat treatment, wherein it comprises the step of producing a catalyst precursor in which raw material salt solution containing at least one of molybdenum, iron, nickel and cobalt, and silicon or a dried product obtained by drying it are subjected to heat treatment, and the step of producing said catalyst in which said catalyst precursor and a bismuth compound are incorporated in an aqueous solution and dried and calcined.