| 多元间歇精馏塔的模拟 |
| |
| 引用本文： | 马宏燎,陈绍洲.多元间歇精馏塔的模拟[J].华东理工大学学报(自然科学版),1999,25(2):205-208. |
| |
| 作者姓名： | 马宏燎 陈绍洲 |
| |
| 作者单位： | 华东理工大学石油加工研究所 |
| |
| 摘 要： | 针对油气田轻烃中组分数较多的特点，从精度，时间，通用性三方面综合考虑，采用ＳＰＫ或ＰＲ方程计算混合物的汽液平衡常数，考虑了持液量的影响，建立了一个基于半连续法的适用于多元物系的间歇精馏模型，开发并编制了模拟间歇精馏过程的软件。
|
| 关 键 词： | 精馏塔 模拟 逐板计算法 间歇精馏塔 轻烃 |
Simulation of Multicomponent Batch Distillation |
| |
| Ma Hongliao ,Chen Shaozhou and Bai Zilong.Simulation of Multicomponent Batch Distillation[J].Journal of East China University of Science and Technology,1999,25(2):205-208. |
| |
| Authors: | Ma Hongliao Chen Shaozhou and Bai Zilong |
| |
| Institution: | Ma Hongliao *,Chen Shaozhou and Bai Zilong |
| |
| Abstract: | In this thesis,comparison among several equation of state has been carried out.Considering precision,time and universality,PR or SRK is selected to calculate the phase equilibrium constant of the mixture.A model has been developed to simulate the operation of multicomponent batch distillation with holdup by a plate to plate method,and has been programmed with FORTRAN. |
| |
| Keywords: | batch distillation column simulation plate to plate calculation |
| 本文献已被 CNKI 维普 等数据库收录！ |
