IP Library Granted Patent US 12709591
Granted Patent B2
US 12709591 · App. 17/758,486 · Granted Aug 18, 2026

Method for producing acrylic acid

Inventors: Nao Igata (Himeji, JP); Masaaki Okuno (Himeji, JP); Tatsuya Nakanishi (Himeji, JP)
Assignee: NIPPON SHOKUBAI CO., LTD.
C07C51/252
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Quick Facts
Patent No.
US 12709591
App. No.
17/758,486
Granted
Aug 18, 2026
Kind
B2
Abstract

A method includes supplying a gas containing acrolein to a fixed bed reactor including a reaction tube to produce acrylic acid by vapor phase catalytic oxidation of acrolein. The reaction tube is packed with catalysts having different activities in such a way that catalyst layers are formed in a tube axis direction. A catalyst X having the highest activity among the catalysts contained in all the catalyst layers is placed in the whole or a part of a section up to 30% of a length of all the catalyst layers from a rearmost portion on a gas outlet side toward a gas inlet side. A catalytically active component x in the catalyst X has Mo, V, and optionally Cu. When Cu is included, its amount is 0.8 mol or less per 12 mol of Mo. A specific surface area of the catalytically active component x is 15-40 m 2 /g.

Claims (11)

1 . A method d for producing acrylic acid, comprising supplying a gas containing acrolein to a fixed bed reactor including a reaction tube to produce acrylic acid by vapor phase catalytic oxidation of acrolein,

wherein the reaction tube is packed with catalysts having different activities in such a way that two or more catalyst layers are formed in a tube axis direction of the reaction tube;

a catalyst X having the highest activity among the catalysts contained in all the catalyst layers is placed in the whole or a part of a section up to 30% of a length of all the catalyst layers from a rearmost portion on a gas outlet side toward a gas inlet side of all the catalyst layers;

a layer length of a catalyst layer including the catalyst X is 3 to 30% of the length of all the catalyst layers;

a catalytically active component x in the catalyst X has Mo, V, and optionally Cu, and when Cu is included, an amount thereof is 0.8 mol or less per 12 mol of Mo; and

a specific surface area of the catalytically active component x is 15 m 2 /g to 40 m 2 /g.

2 . The method for producing acrylic acid according to claim 1 , wherein

a composition of the catalytically active component x is represented by the following general formula (1), provided that oxygen in an oxidation state is omitted:

Mo 12 Cu a V b A c B d C e D f E g   (1)

wherein Mo is molybdenum, Cu is copper, V is vanadium, A is at least one element selected from niobium, tungsten, and tantalum, B is at least one element selected from antimony and tellurium, C is at least one element selected from chromium, manganese, iron, cobalt, nickel, zinc, bismuth, tin, thallium, and a rare earth element, D is at least one element selected from an alkali metal and an alkaline earth metal, E is at least one element selected from silicon, aluminum, titanium, zirconium, and cerium, and a, b, c, d, e, f, and g represent the numbers of atoms of Cu, V, A, B, C, D, and E, respectively, and 0≤a≤0.8, 2≤b≤10, 0≤c≤12, 0≤d≤6, 0≤e≤12, 0≤f≤5, and 0≤g≤50.

3 . The method for producing acrylic acid according to claim 1 , wherein the amount of Cu in the catalytically active component x is 0.6 mol or less per 12 mol of Mo.