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N-甲酰基吗啉芳烃萃取精馏工艺的模拟及优化
引用本文:曲宏亮,王俊,刘艳升,胡玉峰. N-甲酰基吗啉芳烃萃取精馏工艺的模拟及优化[J]. 石油炼制与化工, 2012, 43(4): 74-79
作者姓名:曲宏亮  王俊  刘艳升  胡玉峰
作者单位:1. 中国石化北京燕山分公司化工七厂;2. 中国石油大学(北京)化学工程学院;
摘    要:以文献中的相平衡数据为基础,利用Aspen Plus 软件,建立N-甲酰基吗啉(NFM)芳烃萃取精馏工艺模型。模拟结果表明:该模型可以较好地反映装置的实际操作状况。考察剂油比、贫溶剂进料温度以及贫溶剂中苯含量等参数对分离过程的影响,获得N-甲酰基吗啉芳烃萃取精馏工艺的最佳操作参数为:剂油质量比4.66,贫溶剂进料温度112 ℃,贫溶剂中苯质量分数在1%左右。优化工况的模拟计算结果表明,优化后苯收率和苯纯度明显提高,其中苯收率提高0.6百分点,苯纯度提高0.06百分点。

关 键 词:萃取精馏  N-甲酰基吗琳  芳烃  优化   
收稿时间:2011-08-29
修稿时间:2011-11-10

PROCESS SIMULATION AND OPTIMIZATION OF AROMATIC EXTRACTION DISTILLATION WITH N-FORMYLMORPHOLINE
Qu Hongliang , Wang Jun , Liu Yansheng , Hu Yufeng. PROCESS SIMULATION AND OPTIMIZATION OF AROMATIC EXTRACTION DISTILLATION WITH N-FORMYLMORPHOLINE[J]. Petroleum Processing and Petrochemicals, 2012, 43(4): 74-79
Authors:Qu Hongliang    Wang Jun    Liu Yansheng    Hu Yufeng
Affiliation:1.Yanshan Petrochemical Company,SINOPEC,Beijing,100250; 2.Faculty of Chemical Engineering,China University of Petroleum-Beijing)
Abstract:Using Aspen Plus software,a process model of separating aromatics from non-aromatics by extractive distillation with N-formylmorpholine(NFM) is set up based on vapor-liquid equilibrium data of NFM andhydrocarbons system.Simulation results show that the calculations agree well with the actual operation data.The effect of solvent/oil ratio,inlet temperature of lean solvent and benzene content in lean solvent on the separation is investigated.Optimum operation parameters are obtained as follows: solvent/oil mass ratio of 4.66,lean solvent inlet temperature of 112 ℃ and mass fraction of benzene in lean solvent of about 1%.Calculations under optimization conditions show that the yield and purity of benzene enhance significantly,they increase 0.6 and 0.06 percentage points,respectively.
Keywords:extractive distillation  N-formylmorpholine  aromatic hydrocarbon  optimization
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