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Excess Methanol Recovery in Biodiesel Production Process Using a Distillation Column: A Simulation Study

机译:使用蒸馏塔在生物柴油生产过程中过量回收甲醇的模拟研究

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This paper presents an ASPEN PLUSTM 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
机译:本文介绍了使用蒸馏塔在连续生物柴油生产过程中过量甲醇回收的ASPEN PLUSTM模拟研究。用于生产生物柴油的原料是含有15%游离脂肪酸(油酸)的甘油三油精。特别注意不同的醇/油比以及蒸馏塔的重要设计和操作参数对产物中过量甲醇回收的影响。能量消耗由蒸馏塔的再沸器热负荷表示。对模拟结果的分析表明,对于一定的蒸馏操作条件和反应参数,在生物柴油和甘油相分离之前,有可能回收约95-98%的过量甲醇,尽管对于高醇/油比而言,能量需求呈指数增长。 :10.3329 / cerb.v13i2.3538化学工程研究通报13(2009)55-60

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