摘要
以Aspen Plus模拟乙烯装置汽油分馏塔系统,其轻烃部分物性可以用Peng-Robison、Redich-Kwong-Seave等状态方程来描述,馏分油部分物性则用虚拟组分(Fictitious Components)描述,文章还以此研究了各工艺参数对塔板温度的影响。
The gasoline fractionator system is simulated by Aspen Hus. The properties of light hydrocarbons are described by Peng - Robison or Redich - Kwong -Seave, etc. state equations, the properties of distillate oil are described by fictitious components. The paper studies the effect of various parameters to plate temperature.
出处
《乙烯工业》
CAS
2002年第4期13-17,共5页
Ethylene Industry
