摘要
探讨了加压-常压与常压-加压两种变压精馏工艺对分离甲醇-碳酸二甲酯的影响。通过Aspen Plus模拟计算发现,在指定甲醇和碳酸二甲酯产品纯度的前提下,采用相同塔板数的高压塔和常压塔,两种工艺的能耗有显著差别;加压-常压工艺比常压-加压工艺的再沸器负荷高20%以上,应该选用常压-加压工艺分离甲醇-碳酸二甲酯。在设计变压精馏系统时,如若改变高压塔和低压塔次序能实现共沸物的分离,需要对两种工艺进行能耗或经济性分析,选取更优的工艺。
This article explores the effects of two pressure swing distillation processes,pressure-atmospheric and atmospheric-pressure,on the separation of methanol dimethyl carbonate.Through Aspen Plus simulation calculations,it was found that under the premise of specifying the purity of methanol and dimethyl carbonate products,there is a significant difference in energy consumption between high-pressure and atmospheric-pressure towers with the same number of trays;the reboiler load of the pressure-atmospheric process is more than 20%higher than that of the atmospheric-pressure process.Therefore,the atmospheric-pressure process should be used to separate methanol dimethyl carbonate.When designing a pressure swing distillation system,if changing the order of the high-pressure and low-pressure towers can achieve the separation of azeotropes,it is necessary to conduct energy consumption or economic analysis on the two processes and select the more optimal one.
出处
《化工设计通讯》
CAS
2024年第8期101-104,共4页
Chemical Engineering Design Communications
关键词
碳酸二甲酯
精馏工艺
甲醇
dimethyl carbonate
distillation process
methanol