摘要
通过Aspen Plus软件模拟PTA生产的醋酸脱水共沸精馏系统。稳态模拟结果与现场数据吻合较好。在稳态模型的基础上,设计两种控制方案,利用Aspen Dynamics进行动态模拟,测试这两种控制方案的性能,找出较好的控制方案。模拟的结果对生产操作和控制方案的设计具有重要的指导意义。
A model of pure terephthalic acid solvent dehydratic distillation based on Aspen Plus has been studied. The results of steady-state simulation were identical with the real system. Meanwhile, two control structures were proposed. Through simulation based on Aspen Dynamics, the better control structure is obtained by testing the system performances of the two structures. The simulating resuits have an important guidance value for practice operation and control structure design.
出处
《计算机与应用化学》
CAS
CSCD
北大核心
2008年第5期533-536,共4页
Computers and Applied Chemistry
基金
国家杰出青年基金(60625302)
上海市自然科学基金资助(06ZR14027)
上海市重点学科建设项目资助(B504)
关键词
共沸精馏
醋酸脱水
动态模拟
精馏塔控制
azeotropic distillation, acetic acid dehydration, dynamic simulation, distillation column control
