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甲醇双效精馏过程参数优化及有效能分析
引用本文:刘启魁,王正权.甲醇双效精馏过程参数优化及有效能分析[J].化工技术与开发,2011,40(7):41-44.
作者姓名:刘启魁  王正权
作者单位:1. 大庆市南垣股份公司,黑龙江大庆,163517
2. 大连理工大学化工学院,辽宁大连,116024
摘    要:利用流程模拟软件Pro Ⅱ对甲醇双效精馏过程进行了参数优化,结果表明,适合的操作压力为800kPa,加压塔塔底与塔顶质量流量适合比为1.66.在优化参数的基础上对过程进行了模拟,并对传统两塔流程及双效梢馏流程进行了热力学分析,结果表明,双效精馏过程热力学效率为15.95%,与传统两塔流程相比,效率提高了7.72%.

关 键 词:甲醇  双效精馏  优化  流程模拟  热力学效率

Parameter Optimization and Available Energy Analysis for Methanol Process of Double-effect Rectification
LIU Qi-qui,WANG Zheng-quan.Parameter Optimization and Available Energy Analysis for Methanol Process of Double-effect Rectification[J].Technology & Development of Chemical Industry,2011,40(7):41-44.
Authors:LIU Qi-qui  WANG Zheng-quan
Affiliation:1.Nanyuan Company,Daqing 163517,China;2.College of Chemical Engineering, Dalian University of Technology,Dalian 116024,China)
Abstract:The operating parameters of double-effect rectification process for methanol were optimized by means of process simulation software Pro II.The results showed that,a suitable operating pressure was 800kPa,the ratio of bottom mass flow and top mass flow in high pressure distillation tower was 1.66.The double-effect rectification process on the optimized parameters was simulated.The thermodynamic analysis for traditional two-tower process and double-effect distillation process showed that the thermodynamic efficiency for double-effect distillation process was 15.95%,which was increased 7.72%compared with the traditional two-tower process.
Keywords:methanol  double-effect rectification  optimization  process simulation  thermodynamic efficiency
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