生物乙醇装置蒸汽渗透与蒸馏吸附净化模拟

M. Gozan, Mia Sari Setiawan, Kenny Lischer
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引用次数: 6

摘要

在与汽油(EXX)混合的生物燃料中,需要高纯度的生物乙醇。在生物乙醇生产过程中,乙醇-水的共沸特性成为纯化工艺的主要障碍。本研究通过模拟工具Superpro Designer 9.0软件对两种生物乙醇分离过程进行了研究。乙醇纯度和低成本经济的工艺是主要考虑因素。对蒸汽渗透膜技术的P净化方法与蒸馏-吸附法进行了比较。本文采用了以往实验室实验数据和一些文献资料。结果表明,蒸馏-吸附法比蒸汽渗透法更经济。蒸馏吸附和蒸汽渗透的模拟投资回收期分别为3.9年和4.3年,IRR分别为20.23%和17.89%。蒸汽渗透的初始投资值比蒸馏法高9.6%。在运行成本上观察到显著的差异,因为更多的单位涉及蒸汽渗透,需要更多的劳动力来操作。
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Purification Simulation With Vapor Permeation and Distillation-Adsorption In Bioethanol Plant
High purity of Bioethanol is required in biofuel mi xing with gasoline (EXX). In bioethanol production li e, the azeotropic property of ethanol-water becomes the ba rrier for purification process. This study examined two bioethanol separation processes by support of simulation tools , Superpro Designer 9.0 software. Ethanol purity an d low costeconomical process were the major considerations. P urification method of vapor permeation membrane tec hnology was compared with distillation-adsorption method. Data from previous lab experiments and some literatures w re used. The results showed that distillation-adsorption method is more economical compared to vapor permeation tec hnology. Payback period of the simulation is 3.9 years and 4 .3 years to distillation adsorption and vapor perme ation respectively with each IRR value is 20.23% and 17.89%. Initial i nvestment value of vapor permeation is 9.6% higher t an distillation method. Significant difference observe d in operating costs, since more units involved in vapor permeation require more labors to operate.
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