IP Library Granted Patent US 7,662,742
Granted Patent B2
US 7,662,742 · App. 10/577,136 · Granted Feb 16, 2010

Process for producing catalyst for methacrylic acid production, catalyst for methacrylic acid production, and process for producing methacrylic acid

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Quick Facts
Patent No.
US 7,662,742
App. No.
10/577,136
Granted
Feb 16, 2010
Kind
B2
Abstract

A method for producing a catalyst containing given atoms in a given atomic proportion for use in producing methacrylic acid through gas-phase catalytic oxidation of methacrolein with molecular oxygen comprising the steps of: (i) preparing a solution or slurry containing at least molybdenum, phosphorus, and vanadium (liquid I); (ii) preparing a solution or slurry containing ammonium radical (liquid II); (iii) preparing a mixture of the liquid I and the liquid II by introducing one liquid (liquid PR) of the liquid I and the liquid II into a tank (tank A) and pouring the other liquid (liquid LA) on a continuous region in the surface of the liquid PR, the continuous region occupying 0.01 to 10% of the whole area of the surface of the liquid PR; and (iv) drying and calcining the resultant solution or slurry containing a catalyst precursor comprising all the catalyst constituents.

Claims (19)

1. A method for producing a catalyst having a composition represented by the following formula (1) for use in producing methacrylic acid through gas-phase catalytic oxidation of methacrolein with molecular oxygen, comprising:

(i) preparing a solution or slurry comprising at least molybdenum, phosphorus, and vanadium (liquid I);

(ii) preparing a solution or slurry containing ammonium radical (liquid II);

(iii) preparing a mixture of the liquid I and the liquid II by:

introducing one of the liquid I and the liquid II (liquid PR) into a tank (tank A),

subsequently pouring the other of the liquid I and the liquid II (liquid LA) into the tank already containing the liquid PR,

the liquid LA is poured into the tank A so that when the liquid LA contacts the liquid PR the contact occurs at a continuous region on a surface of the liquid PR, and

the continuous region comprises 0.01 to 10% of an entire surface area of the liquid PR in the tank A; and

(iv) drying and calcining the resultant solution or slurry containing a catalyst precursor comprising all the catalyst constituents,

P a Mo b V c Cu d X e Y f Z g O h   (1)

wherein:

P, Mo, V, Cu and O represent phosphorous, molybdenum, vanadium, copper and oxygen, respectively;

X represents at least one element selected from the group consisting of antimony, bismuth, arsenic, germanium, zirconium, tellurium, silver, selenium, silicon, tungsten and boron;

Y represents at least one element selected from the group consisting of iron, zinc, chromium, magnesium, tantalum, cobalt, manganese, barium, gallium, cerium and lanthanum;

Z represents at least one element selected from the group consisting of potassium, rubidium and cesium;

subscripts a, b, c, d, e, f, g and h represent an atomic ratio of each element, respectively; and

when b is 12, a is in the range of from 0.5 to 3, c is in the range of from 0.01 to 3, d is in the range of from 0.01 to 2, e is in the range of from 0 to 3, f is in the range of from 0 to 3, g is in the range of from 0.01 to 3 and h represents the atomic ratio of oxygen necessary for fulfilling the requirement of the valence of each element above.

2. The method according to claim 1 , wherein the liquid LA is poured while stirring the liquid PR introduced into the tank A with a stirring power of 0.01 to 3.5 kW/m 3 .

3. The method according to claim 1 , wherein the liquid LA is poured from a height of 0.05 to 2 m above the surface of the liquid PR introduced into the tank A.

Assignments (1)
CHANGE OF NAME Recorded Sep 5, 2017
From: MITSUBISHI RAYON CO., LTD.
To: MITSUBISHI CHEMICAL CORPORATION
Reel/Frame 043750/0834 →