首页> 外国专利> PROCESS AND DEVICE SYSTEM FOR PRODUCING DIMETHYL OXALATE BY HIGH-PRESSURE CARBONYLATION OF INDUSTRIAL SYNTHESIS GAS AND PRODUCING ETHYLENE GLYCOL BY HYDROGENATION

PROCESS AND DEVICE SYSTEM FOR PRODUCING DIMETHYL OXALATE BY HIGH-PRESSURE CARBONYLATION OF INDUSTRIAL SYNTHESIS GAS AND PRODUCING ETHYLENE GLYCOL BY HYDROGENATION

机译:工业合成气高压羰基化生产草酸二甲酯,加氢制乙二醇的工艺及装置系统

摘要

The present invention relates to a process and a device system for producing dimethyl oxalate by high-pressure carbonylation of industrial synthesis gas and producing ethylene glycol by hydrogenation. The process comprises the steps of: using industrial NO, O2 and methanol as raw materials for an esterification reaction to produce methyl nitrite; and then using industrial CO and methyl nitrite for a carbonylation reaction in a plate reactor to produce carbonylation products, which mainly include dimethyl oxalate and dimethyl carbonate; separating the carbonylation products to obtain dimethyl carbonate products; subjecting dimethyl oxalate to subsequent hydrogenation in the plate reactor to produce ethylene glycol products; subjecting the waste acids in the esterification reaction and purge gases in the carbonylation reaction to a coupling recovery treatment for recycling. The system comprises an esterification reaction system, a carbonylation reaction system, a coupling recovery system for purge gases and waste acids and a hydrogenation reaction system. The process has the characteristic that device consumption is remarkably reduced, and particularly the nitric acid waste liquid recycling and purge gas recycling are highly coupled as well as the separation process thereof; recycling of the raw materials in reaction waste gases is realized, and the effect is remarkable.
机译:本发明涉及通过工业合成气的高压羰基化生产草酸二甲酯并通过氢化生产乙二醇的方法和设备系统。该方法包括以下步骤:以工业NO,O 2 和甲醇为原料进行酯化反应以生产亚硝酸甲酯。然后使用工业CO和亚硝酸甲酯在平板反应器中进行羰基化反应,生成羰基化产物,主要包括草酸二甲酯和碳酸二甲酯。分离羰基化产物以获得碳酸二甲酯产物;将草酸二甲酯在平板反应器中随后氢化以生产乙二醇产物;对酯化反应中的废酸和羰基化反应中的吹扫气体进行偶联回收处理以进行再循环。该系统包括酯化反应系统,羰基化反应系统,用于吹扫气体和废酸的偶联回收系统以及氢化反应系统。该工艺具有显着降低设备消耗的特点,特别是硝酸废液的循环利用和吹扫气的循环及其分离过程是高度耦合的。实现了反应废气中原料的循环利用,效果显着。

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