摘要
应用HYSIM软件建立并模拟了以重整二甲苯塔底重芳烃为原料的偏三甲苯分离装置的工艺流程。与生产实际的对比结果表明:模拟计算的结果是准确的。根据模拟计算的结果,分析了工艺参数对工艺过程的影响并提出了优化的操作工艺参数。
Raw material used for 1.2.4 - trimethylbenzene separation plant in which heavy aromatics hydrocarbons come from the bottom of reformation dimethylbenzene tower has been established and simulated . The results, compared with actual process, show that the simulation calculation results are accuracy. By the results of simulation calculation, the influence of process parameters on the process has been analyzed and the optimized process parameters deduced.
出处
《石油化工设计》
CAS
1999年第2期48-51,共4页
Petrochemical Design
