Method and device for preparing dimethyl maleate by membrane separation coupled catalytic rectification

By coupling a solid acid catalyst with membrane separation and utilizing a porous diatomaceous earth membrane for online dehydration, the problems of equipment corrosion, high energy consumption, and low conversion rate in existing processes have been solved, achieving efficient and green preparation of dimethyl maleate.

CN122404140APending Publication Date: 2026-07-17JIANGXI YUANXIN RESOURCE RECYCLING INVESTMENT DEV
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Patent Information

Application Number
CN202610629602.6
Authority / Receiving Office
CN · China
Patent Type
Applications(China)
Current Assignee / Owner
Filing Date
2026-05-09
Publication Date
2026-07-17

AI Technical Summary

Technical Problem

In the existing dimethyl maleate preparation process, traditional homogeneous acid catalysis leads to equipment corrosion and the generation of saline wastewater. Azeotropic distillation has high energy consumption. Membrane separation process is not resistant to high temperature and has not achieved coupling of reactive distillation and membrane separation. Simple reactive distillation does not completely remove water and has limited improvement in conversion rate.

Method used

By coupling a solid acid catalyst with membrane separation and using an inorganic porous membrane for online dehydration, the reactive distillation and membrane separation are integrated. The diatomaceous earth porous membrane selectively permeates water molecules, and methanol vapor is condensed, recovered, and recycled. The reaction temperature and vacuum are controlled, and the catalyst recovery and utilization are optimized.

Benefits of technology

It significantly improved the maleic anhydride conversion rate to 98.51%, reduced methanol consumption by 20.4%, achieved a product purity of 99.1%, reduced by-products, realized green and continuous production, and reduced equipment corrosion and wastewater generation.

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Abstract

本发明公开了一种膜分离耦合催化精馏制备顺丁烯二酸二甲酯的方法及装置,属于顺丁烯二酸二甲酯合成技术领域。以顺酐和甲醇为原料,在固体酸催化剂存在下进行酯化反应,反应精馏塔塔顶气相引出通入无机多孔膜组件,通过膜的选择性渗透在线脱除反应生成的水,同时将经膜分离脱水后的甲醇蒸气冷凝回收并循环回反应精馏塔。控制塔釜反应温度为105~108℃,操作真空度为‑0.08~‑0.10 MPa(表压),顺酐与甲醇摩尔比为1:3.0~6.0,甲醇回用1~3次。本发明顺酐转化率达98.51%,产品纯度≥99.1%,甲醇用量减少20.4%,回收甲醇纯度≥96%可直接循环使用,解决了传统工艺甲醇消耗大、转化率低、副产反丁烯二酸二甲酯多的问题,具有高效、节能、环保、适合工业化生产等优点。
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Citation Information

Patent Citations

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