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Method for preparing methyl methacrylate through aldol condensation of methyl propionate and formaldehyde and multi-stage reaction system

A technology of methyl methacrylate and methyl propionate, applied in the field of methyl methacrylate synthesis, can solve the problems of catalyst running loss, high equipment cost, low reaction conversion rate and the like, achieve stable product quality and reduce operation load, the effect of reducing the variation range

Pending Publication Date: 2020-08-25
BEIJING RISUN TECH CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Using a circulating fluidized bed, the pulverization and running loss of the catalyst are serious, and the annual consumption of the catalyst is huge. Combined with the characteristics of low reaction conversion rate and easy carbon formation of the catalyst, it will directly lead to high production and operation costs. The structure of the fluidized bed is complex and the cost of equipment is high. From an economic point of view, the circulating fluidized bed is not suitable for the preparation of MMA by the aldol method
In the fixed bed switching reaction regeneration mode, with the intensification of catalyst deactivation, the composition of the reaction product changes greatly in the early and late stages, which brings certain challenges to the subsequent separation operation and is not conducive to the long-term stable operation of the device.

Method used

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  • Method for preparing methyl methacrylate through aldol condensation of methyl propionate and formaldehyde and multi-stage reaction system
  • Method for preparing methyl methacrylate through aldol condensation of methyl propionate and formaldehyde and multi-stage reaction system
  • Method for preparing methyl methacrylate through aldol condensation of methyl propionate and formaldehyde and multi-stage reaction system

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Embodiment 1

[0049] Such as figure 1 Shown methyl propionate and formaldehyde aldol method condensation to prepare the multistage reactor process of methyl methacrylate, it comprises the first section reactor 1, the second section reactor 2 and the third section reactor 3, wherein, There are two stages for reaction and one for catalyst regeneration. The reaction process conditions are: the weight hourly space velocity is 3 / h, the reaction pressure is normal pressure, the reaction temperature is 330°C, the molar ratio of raw material methyl propionate to formaldehyde is 2:1, and the molar ratio of formaldehyde to methanol is 1:4 ; The regeneration process conditions are: the volumetric space velocity is 600 / h, the regeneration temperature is 400°C, and the regeneration pressure is normal pressure. The life of the catalyst is 336 hours, that is, it needs to be regenerated after 336 hours of reaction, and each reactor is switched at an interval of 168 hours. The composition of the initial st...

Embodiment 2

[0051] A multi-stage reactor for the condensation of methyl propionate and formaldehyde to produce methyl methacrylate, which includes a first-stage reactor, a second-stage reactor, a third-stage reactor and a fourth-stage reactor, among which there are three One stage reactor is used for reaction, and one stage is used for catalyst regeneration. The reaction process conditions are: the weight hourly space velocity is 3 / h, the reaction pressure is normal pressure, the reaction temperature is 330°C, the molar ratio of raw material methyl propionate to formaldehyde is 2:1, and the molar ratio of formaldehyde to methanol is 1:4 ; The regeneration process conditions are: the volumetric space velocity is 600 / h, the regeneration temperature is 400°C, and the regeneration pressure is normal pressure. The life span of the catalyst is 336h, that is, regeneration is required after 336h of reaction, and each reactor is switched at an interval of 112 hours. The composition of the initial ...

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Abstract

The invention provides a method for preparing methyl methacrylate through aldol condensation of methyl propionate and formaldehyde and a multi-section reaction system. The multi-section reaction system at least comprises three sections of reactors, raw material gas can respectively enter each section of reactor and react under the action of a catalyst to generate methyl methacrylate. In the production process, at least two sections of reactors in the multiple sections of reactors are used for catalytic reaction, and generated products can enter a reaction product header pipe at the same time;at least one section of the reactor is regenerated in situ; and when the activity of the catalyst in the reactor is reduced to a preset percentage, the reactor performs in-situ regeneration. The molarfraction of the methyl methacrylate after the product generated by the multi-section reactor enters the reaction product main pipeline and is mixed is 5.0%-7.5%. According to the method and the system, the variation amplitude of the reaction product composition in the initial stage and the final stage of the reaction can be effectively reduced, the stability of the product quality is ensured, andthe operation load of the subsequent separation process is reduced.

Description

technical field [0001] The invention belongs to the technical field of methyl methacrylate synthesis, and in particular relates to a method for preparing methyl methacrylate by condensation of methyl propionate and formaldehyde aldol and a multi-stage reaction system used in the method. Background technique [0002] Methyl methacrylate (MMA) is an important organic chemical raw material, which is mainly used in many production fields such as organic glass (PMMA), resin, coating, and adhesive. At present, the most important MMA production technology, acetone cyanohydrin method (ACH method), has a tendency to be eliminated due to backward technology and serious environmental pollution. The newly developed MMA preparation technologies include Mitsubishi's isobutylene oxidation method, BASF's ethylene method, Lucite's alpha method, etc. The common feature of these technologies is that the process is relatively simple and safe and environmentally friendly. Among them, the alpha ...

Claims

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Application Information

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IPC IPC(8): C07C67/343C07C69/54B01J8/02
CPCC07C67/343B01J8/02C07C69/54Y02P20/584
Inventor 贾靖华张战党伟荣陈西波高桂余王朋李秀芝董文威
Owner BEIJING RISUN TECH CO LTD
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