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Method for preparing methyl methacrylate by dehydrogenation esterification of isobutyric acid

A technology of methyl methacrylate and isobutyric acid is applied in the preparation of carboxylate, chemical instruments and methods, catalyst activation/preparation, etc., and can solve the problems of insufficient market competitiveness, low selectivity, and many by-products. , to achieve the effect of more dehydrogenation active centers, increase product yield, and reduce reaction steps

Pending Publication Date: 2022-07-12
RUNTAI CHEM TAIXING CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The process has many steps, low selectivity, many by-products, and insufficient market competitiveness
The isobutene oxidation method is to oxidize isobutene to methacrylic acid first, and then esterify with methanol to generate MMA. This method generally uses noble metals as catalysts, and the cost is relatively high.

Method used

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  • Method for preparing methyl methacrylate by dehydrogenation esterification of isobutyric acid
  • Method for preparing methyl methacrylate by dehydrogenation esterification of isobutyric acid
  • Method for preparing methyl methacrylate by dehydrogenation esterification of isobutyric acid

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0023] (1) Dissolve ammonium molybdate into methanol to obtain solution A, dissolve 2-methylimidazole into methanol to obtain solution B, slowly add solution A to solution B under vigorous stirring, and continue stirring for 1 h. The molar ratio of molybdenum atom to 2-methylimidazole was 1:5.

[0024] (2) Transfer the above solution to an autoclave with a polytetrafluoroethylene lining, and react at 100° C. for 24 hours. After cooling, take out, filter, wash with methanol, and vacuum dry at 50 °C for 20 h to obtain catalyst precursor M / ZIF.

[0025] (3) The precursor M / ZIF was placed in a quartz tube, and 120ml / min of NH was introduced 3 / N 2 The mixed gas was calcined at 700 °C for 3 h to obtain a MN / N-C bifunctional catalyst. The mixed gas NH 3 / N 2 The ratio is 15:1.

[0026] (4) 0.2g of catalyst is loaded into the fixed bed reactor, and the isobutyric acid and methanol mixed solution whose mass ratio is 1:8 is added, and N 2 The reaction temperature is 400℃, the pre...

Embodiment 2

[0028] (1) Dissolve ammonium tungstate into methanol to obtain A, dissolve 2-methylimidazole into methanol to obtain solution B, slowly add solution A to solution B dropwise with vigorous stirring, and continue stirring for 1 h. The molar ratio of molybdenum atom to 2-methylimidazole is 1:8.

[0029] (2) Transfer the above solution into an autoclave with a polytetrafluoroethylene lining, and react at 80° C. for 36 hours. After cooling, take out, filter, wash with methanol, and vacuum dry at 80 °C for 16 h to obtain catalyst precursor M / ZIF.

[0030] (3) The precursor M / ZIF was placed in a quartz tube, and 120ml / min of NH was introduced 3 / N 2 The mixed gas was calcined at 800 °C for 4 h to obtain the MN / N-C bifunctional catalyst. Mixed gas NH 3 / N 2 The ratio is 12:1.

[0031] (4) 0.2g of catalyst is loaded into the fixed bed reactor, and the isobutyric acid and methanol mixed solution whose mass ratio is 1:8 is added, and N 2 The reaction temperature is 400℃, the press...

Embodiment 3

[0033] (1) Dissolve ammonium molybdate and cobalt nitrate into methanol to obtain A, dissolve 2-methylimidazole into methanol to obtain solution B, slowly add solution A to solution B dropwise with vigorous stirring, and continue stirring for 1 h. The molar ratio of the sum of molybdenum + cobalt atoms to 2-methylimidazole is 1:10, and the molybdenum atom to cobalt atom ratio is 1:1.

[0034] (2) Transfer the above solution to an autoclave with a polytetrafluoroethylene lining, and react at 120° C. for 24 hours. After cooling, take out, filter, wash with methanol, and vacuum dry at 40 °C for 20 h to obtain catalyst precursor M / ZIF.

[0035] (3) The precursor M / ZIF was placed in a quartz tube, and 100ml / min of NH was introduced 3 / N 2 The mixed gas was calcined at 600 °C for 5 h to obtain the MN / N-C bifunctional catalyst. Mixed gas NH 3 / N 2 The ratio is 10:1.

[0036] (4) 0.2 g of catalyst is loaded into the fixed bed reactor, and the isobutyric acid and methanol mixed s...

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Abstract

The invention belongs to the technical field of preparation of methyl methacrylate, relates to a method for preparing methyl methacrylate by dehydrogenation esterification of isobutyric acid, and particularly relates to a method for preparing methyl methacrylate by esterification of isobutyric acid and methanol in N2 atmosphere under the action of an MN / N-C catalyst in a fixed bed reactor. During preparation of the MN / N-C catalyst, when an organic matter is converted into an N-modified C carrier, metal embedded in a C wall is converted into MN, MN can catalyze dehydrogenation of isobutyric acid, N is alkaline and can catalyze an esterification reaction, and catalyst deactivation caused by coking caused by B acid in the dehydrogenation process is avoided. Meanwhile, MN particles are wrapped and isolated by C and cannot be sintered in the high-temperature dehydrogenation process, and the stability of the catalyst is high. According to the method, isobutyric acid is subjected to one-step dehydrogenation esterification to generate methyl methacrylate, the reaction steps are simplified, and the esterification efficiency is high.

Description

technical field [0001] The invention belongs to the technical field of catalyst preparation, and in particular relates to a method for preparing methyl methacrylate by dehydroesterification of isobutyric acid. Background technique [0002] Methyl methacrylate (MMA) is the basic raw material for the synthesis of polymethyl methacrylate (PMMA). PMMA, also known as plexiglass, is widely used in construction, automobile, paint and other industries due to its excellent properties, such as high light transmittance, high mechanical strength, corrosion resistance, wear resistance, etc. Therefore, with the development of society, the demand for MMA continues to increase, especially in the past ten years, the demand for MMA has grown rapidly. [0003] At present, the methods for producing MMA mainly include acetone cyanohydrin method (ACH method), ethylene and isobutylene oxidation method. The ACH method is currently the most important process for producing MMA in the world, but thi...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J27/24B01J35/00B01J37/08C07C67/317C07C67/08C07C69/653
CPCB01J27/24B01J37/086C07C67/317C07C67/08B01J35/394B01J35/393C07C69/653Y02P20/584
Inventor 杨萍卢小松张世元
Owner RUNTAI CHEM TAIXING CO LTD