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Preparation method of methyl methacrylate

A technology of methyl methacrylate and methacrolein, which is applied in the field of catalytic synthesis, can solve the problems of catalyst activity decline, catalyst collision wear, energy consumption and environment, etc., and achieve the goal of improving stability, improving environmental protection index and prolonging service life Effect

Active Publication Date: 2020-04-10
潍坊三力本诺化学工业有限公司 +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Among them, the catalyst used in CN109395732 patent is SiO 2 -Al 2 o 3 As a carrier, a large amount of nitric acid is introduced in the preparation process, and the precursor of alumina is aluminum nitrate, which causes a large amount of NOx to be produced in the subsequent roasting process, consumes a lot of energy and is not environmentally friendly, and the economy is poor
The reaction of co-oxidation of methacrolein and methanol to MMA is a gas-liquid-solid three-phase reaction. In the reaction, air or oxygen exists in a large amount as oxides in the reaction, so the catalyst is inevitably collided and worn during the reaction, and the active center falls off. phenomenon, which is the direct cause of the decline in catalyst activity; in addition, the polymerization and attachment of the product MMA in the reaction system makes the active center covered, which is also the cause of the decline in catalyst activity.

Method used

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  • Preparation method of methyl methacrylate
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Examples

Experimental program
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Effect test

Embodiment 1

[0046] The preparation method of the catalyst is the same as that of Comparative Example 1, except that the silica is replaced with Na-ZSM-5 molecular sieve powder of the same mass and the ratio of silicon to aluminum is 100, and the resultant is dried at 100 °C; the dried product is calcined at 450 °C for 5h , and then placed in a reduction furnace, the heating rate was 10-15 °C / min, and hydrogen was introduced for reduction, and the hydrogen flow rate was maintained at 30 ml / min. After reduction for 1 h, the catalyst Au / ZSM-5-A was obtained, in which the gold loading was 0.5%. wt. The attrition rate of the catalyst measured according to the American ASTM D5757-00 standard was 0.7%.

Embodiment 2

[0048] The preparation method of the catalyst is the same as that of Comparative Example 1, except that the silica is replaced with Na-Bate molecular sieve powder of the same mass and the ratio of silicon to aluminum is 100, and the resultant is dried at 100 °C; Put it in a reduction furnace with a heating rate of 10-15°C / min, and introduce hydrogen for reduction. The hydrogen flow rate is kept at 30ml / min. After reduction for 1h, the catalyst Au / Beta is obtained, and the gold loading is 0.5%wt. The wear rate of the catalyst measured according to the American ASTM D5757-00 standard was 0.9%.

Embodiment 3

[0050] The preparation method of the catalyst is the same as that of Comparative Example 1, except that the silica is replaced with Na-4A molecular sieve powder of the same mass and the ratio of silicon to aluminum is 100, and the resultant is dried at 100 °C; Placed in a reduction furnace, heating at a rate of 10-15°C / min, introducing hydrogen for reduction, maintaining a hydrogen flow rate of 30ml / min, and reducing the catalyst for 1 hour to obtain catalyst Au / 4A with a gold loading of 0.5%wt. The wear rate of the catalyst measured according to the American ASTM D5757-00 standard was 0.8%.

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PUM

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Abstract

The invention discloses a preparation method of methyl methacrylate, wherein the method comprises the steps: adding methylacrolein and methanol into an airtight continuous reactor, and sufficiently mixing until the mass concentration of methanol in the mixture is 45-80%; and adding a gold-based catalyst into the reactor in a stirring state, introducing an oxidant into the bottom of the reactor, controlling the reaction temperature to be 110-160 DEG C and the reaction pressure to be 0.5-2 MPa, and carrying out catalytic oxidation esterification to prepare methyl methacrylate. The preparation cost of the catalyst is reduced, the wear resistance of the catalyst is improved, the preparation conditions are more environment-friendly, and the catalytic activity is good. The methyl methacrylate product synthesized by catalysis has high yield and is not easy to polymerize in a reaction system.

Description

technical field [0001] The invention belongs to the technical field of catalytic synthesis, and in particular relates to a preparation method of methyl methacrylate. Background technique [0002] Methyl methacrylate (MMA) is an important organic chemical raw material. It is a colorless and transparent liquid with ether fragrance at room temperature. It is mainly used to produce plexiglass and resin materials. At present, the production technology of producing MMA in the world mainly includes the acetonitrile alcohol method and the isobutylene method (three-step reaction), but these technological processes have the shortcomings of large energy consumption and much pollution. Considering environmental protection and economic benefits, developing new The process route is very necessary. [0003] Using air or oxygen as an oxidant to directly oxidize methacrolein and methanol into the target product MMA in one step is undoubtedly a simple, green and economically competitive proc...

Claims

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Application Information

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IPC IPC(8): C07C67/44C07C69/54B01J29/44B01J29/74
CPCC07C67/44B01J29/44B01J29/7415B01J29/7407B01J2229/18C07C69/54Y02P20/584
Inventor 王晓光陈锴尚遇青黄家辉吕强
Owner 潍坊三力本诺化学工业有限公司
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