IP Library Granted Patent US 7,217,680
Granted Patent B2
US 7,217,680 · App. 11/032,072 · Granted May 15, 2007

Method for producing composite oxide catalyst

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Quick Facts
Patent No.
US 7,217,680
App. No.
11/032,072
Granted
May 15, 2007
Kind
B2
Abstract

A method for producing a composite oxide catalyst for gas phase catalytic oxidation of an unsaturated aldehyde with a molecular oxygen-containing gas to produce the corresponding unsaturated carboxylic acid in good yield, is presented. A method for producing a composite oxide catalyst, which is a method for producing a composite oxide catalyst having the following formula (I), characterized in that Sb 2 O 3 of isometric system is used as at least a part of an antimony-supplying source compound: Mo 12 X a V b Sb c Cu d Si e C f O g   (I) (wherein the respective components and variables have the following meanings: X is at least one element selected from the group consisting of Nb and W; a, b, c, d, e, f and g represent atomic ratios of the respective elements, and against 12 of molybdenum atom, 0<a≦10, 0<b≦10, 0<c≦5, 0<d≦5, 0≦e≦1,000, and 0≦f≦1,000, and g is a number determined by the degrees of oxidation of the above respective components.)

Claims (15)

1. A method for producing a composite oxide catalyst, which is a method for producing a composite oxide catalyst having the following formula (I), to be used at the time of gas phase catalytic oxidation of an unsaturated aldehyde with a molecular oxygen-containing gas to produce the corresponding unsaturated carboxylic acid, characterized in that Sb 2 O 3 of isometric system is used as at least a part of an antimony-supplying source compound:

Mo 12 X a V b Sb c Cu d Si e C f O g   (I)

where the respective components and variables have the following meanings:

X is at least one element selected from the group consisting of Nb and W;

a, b, c, d, e, f and g represent atomic ratios of the respective elements;

against 12 of molybdenum atom 0<a≦10, 0<b≦10, 0<c≦5, 0<d≦5, 0≦e≦1,000 and 0≦f≦1,000; and

g is a number determined by the degrees of oxidation of the above respective components, wherein

Sb 2 O 3 is used as the antimony-supplying source compound; and

the ratio (a 1 /a 2 ) of the intensity (a 1 ) at 2θ=about 28.3° to the intensity (a 2 ) at 2θ=about 27.6° of an X-ray diffraction (anticathode Cu—Kα) of the antimony-supplying source compound is at most 0.2.

2. The method for producing a composite oxide catalyst according to claim 1 , wherein the Si and C components-supplying source compound is silicon carbide.

3. The method for producing a composite oxide catalyst according to claim 1 , wherein an aqueous solution or aqueous dispersion of supply source compounds containing the respective catalyst component elements shown by the formula (I), is prepared, and such an aqueous solution or aqueous dispersion is dried to a powder, which is molded by using at least one binder selected from the group consisting of silica, graphite and cellulose, and the molded product is calcined.

4. A composite oxide catalyst produced by the method as defined in claim 1 .

5. A method which comprises gas phase catalytic oxidation of acrolein with a molecular oxygen-containing gas in the presence of the composite oxide catalyst as defined in claim 4 , to produce the corresponding acrylic acid.

6. The method for producing a composite oxide catalyst according to claim 1 , wherein the antimony-supplying source compound comprises at least 80 wt % of the Sb 2 O 3 of isometric system.

7. The method for producing a composite oxide catalyst according to claim 1 , wherein the antimony-supplying source compound comprises at least 90 wt % of the Sb 2 O 3 of isometric system.

Assignments (2)
CHANGE OF NAME Recorded Sep 5, 2017
From: MITSUBISHI RAYON CO., LTD.
To: MITSUBISHI CHEMICAL CORPORATION
Reel/Frame 043750/0834 →
MERGER Recorded Sep 4, 2017
From: MITSUBISHI CHEMICAL CORPORATION
To: MITSUBISHI RAYON CO., LTD.
Reel/Frame 043750/0207 →