用精馏塔回收生物柴油生产过程中过量甲醇的模拟研究

B. Dhar, K. Kirtania
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引用次数: 69

摘要

本文介绍了利用ASPEN PLUS TM进行生物柴油连续生产过程中过量甲醇回收的模拟研究。用于生产生物柴油的原料是含15%游离脂肪酸(油酸)的三油酸。重点讨论了不同醇油比、精馏塔重要设计和操作参数对产品剩余甲醇回收的影响。能耗用精馏塔再沸器热负荷表示。仿真结果分析表明,在一定的蒸馏操作条件和反应参数下,生物柴油和甘油相分离前可以回收95-98%左右的多余甲醇,但对于高醇油比,能量需求呈指数级增长。DOI: 10.3329/cerb.v13i2.3538化学工程研究通报13 (2009)55-60
本文章由计算机程序翻译,如有差异,请以英文原文为准。
EXCESS METHANOL RECOVERY IN BIODIESEL PRODUCTION PROCESS USING A DISTILLATION COLUMN: A SIMULATION STUDY
This paper presents an ASPEN PLUS TM simulation study for excess methanol recovery in continuous biodiesel production process using a distillation column. The feedstock used for biodiesel production was Triolein containing 15% free fatty acid (Oleic Acid). The special attention was devoted to the effect of different alcohol to oil ratio and important design and operating parameters of distillation column on excess methanol recovery from the product. The energy consumption is represented by reboiler heat duty of distillation column. Analysis of simulation results shows that for a certain distillation operating condition and reaction parameters it is possible to recover around 95-98% of excess methanol before phase separation of biodiesel and glycerol, although for high alcohol to oil ratio the energy requirement increases exponentially. DOI: 10.3329/cerb.v13i2.3538 Chemical Engineering Research Bulletin 13 (2009) 55-60
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