초록 ▼

A catalyst useful for catalytic vapor-phase oxidation of isobutylene, t-butanol or propylene to produce respectively corresponding unsaturated aldehyde and unsaturated carboxylic acid is provided. The catalyst consists of ring-formed shaped bodies composed of (i) a catalyst composition containing at

A catalyst useful for catalytic vapor-phase oxidation of isobutylene, t-butanol or propylene to produce respectively corresponding unsaturated aldehyde and unsaturated carboxylic acid is provided. The catalyst consists of ring-formed shaped bodies composed of (i) a catalyst composition containing at least molybdenum and bismuth as the active ingredients and (ii) inorganic fibers. The catalyst excels in mechanical strength, can give the object products at high yield and shows little activity degradation with time.

대표청구항 ▼

1. A process for catalytic vapor phase oxidation of isobutylene, tertiary butanol or propylene with molecular oxygen to produce, respectively, corresponding methacrolein and methacrylic acid or acrolein and acrylic acid, the process comprises using a catalyst which is in the form of ring-shaped bodi

1. A process for catalytic vapor phase oxidation of isobutylene, tertiary butanol or propylene with molecular oxygen to produce, respectively, corresponding methacrolein and methacrylic acid or acrolein and acrylic acid, the process comprises using a catalyst which is in the form of ring-shaped bodies composed of a catalyst composition containing at least molybdenum and bismuth as the active ingredients and inorganic fibers, wherein the inorganic fibers are at least one selected from the group consisting of glass fibers, alumina fibers, silica fibers and carbon fibers, and have an average fiber length of from 50 um to 1.5 mm and an average fiber diameter of from 2 um to 20 um.2. The process of claim 1, wherein the catalyst contains from 0.01 to 30% by weight, based on the weight of the catalyst, of inorganic fibers.3. The process of claim 2, wherein the ring-shaped bodies have an outer diameter of 3-10 mm, an inner diameter that is 0.1-0.7 times the outer diameter, and a length that is 0.5-2 times the outer diameter.4. The process of claim 3, wherein the catalyst composition is expressed by the general formulaMOaBibFecAdBeOx wherein Mo is molybdenum; Bi is bismuth; Fe is iron; A is at least one element selected from the group consisting of nickel and cobalt; B is at least one element selected from the group consisting of alkali metal elements, alkaline earth metal elements, thallium, phosphorus, tellurium, antimony, tin, cerium, lead, niobium, manganese, arsenic, zinc, silicon, aluminum, titanium, zirconium, and tungsten; O is oxygen; a, b, c, d, e and x stand for the respective atomic numbers of Mo, Bi, Fe, A, B and O, where a is 12, b is 0.1-10, c is 0.1-20, d is 2-20, e is 0-30 and x is a numerical value determined by the extent of oxidation of the other elements.