Method for producing ammoxidation catalyst and method for producing acrylonitrtie
A method for producing an ammoxidation catalyst, the method including: a step (i) of preparing a starting material slurry comprising molybdenum, bismuth, iron, and a carboxylic acid compound; a step (ii) of stirring the starting material slurry in a temperature range of 30 to 50° C. for 20 minutes to 8 hours, thereby preparing a precursor slurry; a step of spray-drying the precursor slurry, thereby obtaining a dried particle; and a step of calcining the dried particle.
1. A method for producing an ammoxidation catalyst, the method comprising:
a step (i) of preparing a starting material slurry comprising molybdenum, bismuth, iron, and a carboxylic acid compound;
a step (ii) of stirring the starting material slurry in a temperature range of 35 to 45° C. for 1 hour to 8 hours, thereby preparing a precursor slurry;
a step of spray-drying the precursor slurry, thereby obtaining a dried particle; and
a step of calcining the dried particle;
wherein the precursor slurry has a viscosity of 1 to 100 cp, and
wherein the ammoxidation catalyst has a composition represented by the following formula (1):
Mo 12 Bi a Fe b X c Y d Z e O f (1)
wherein X represents at least one element selected from the group consisting of nickel, cobalt, magnesium, calcium, zinc, strontium, and barium; Y represents at least one element selected from the group consisting of cerium, chromium, lanthanum, neodymium, yttrium, praseodymium, samarium, aluminum, gallium, and indium; Z represents at least one element selected from the group consisting of potassium, rubidium, and cesium; provided that a proportion of cobalt is 20 atomic % or more and/or a proportion of magnesium is 20 atomic % or less in the element X; a, b, c, d, and e satisfy 0.1≤a≤2.0, 0.1≤b≤3.0, 0.1≤c≤10.0, 0.1≤d≤3.0 and 0.01≤e≤2.0, respectively; and f represents a number of oxygen atoms needed to satisfy atomic valence requirements of other elements present therein.
2. The method for producing the ammoxidation catalyst according to claim 1 , wherein a content of the carboxylic acid compound in the precursor slurry is 0.01 to 0.10 mol equivalents based on a sum of metal elements constituting the ammoxidation catalyst.
3. A method for producing acrylonitrile by reacting propylene, molecular oxygen, and ammonia, wherein the ammoxidation catalyst produced by the method according to claim 1 is used.