摘要
本文按经验产品分布关系对液化石油气、石脑油、航空煤油及柴油的收率作归一化处理,得到全循环和一次通过加氢裂化过程的利润模型:并以利润为目标对操作过程进行了优化,得出了过程最佳单程转化率以及相应的最佳产品分布。文中海讨论了后续工程配套生产对加弗裂化运行经济性能的影响。
There exists an optimal single-pass reaction conversion to each operation scheme of HC process which was determined by prduct prices and cost factors to reach the maximum operation profit,cor- respondingly the optimal opertion condtions were defined.A model plant was assumed to illstrate the optimizing results.
出处
《化学反应工程与工艺》
CAS
CSCD
北大核心
1990年第4期73-79,共7页
Chemical Reaction Engineering and Technology
关键词
石油
加氢
裂化
经济性
单程转化率
Hydrocracking
Economic optimization
Optimal single-pass conversion
Optimal operation scheme