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

Authors

  • Bipro Ranjan Dhar Chemical & Biochemical Engineering, University of Western Ontario, London, ON, Canada N6A 5B9
  • Kawnish Kirtania Lecturer, Department of Chemical Engineering, Bangladesh University of Engineering & Technology

DOI:

https://doi.org/10.3329/cerb.v13i2.3538

Keywords:

Biodiesel, Methanol Recovery, Distillation, Simulation, ASPEN PLUS

Abstract

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

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Published

2010-01-27

How to Cite

Dhar, B. R., & Kirtania, K. (2010). Excess Methanol Recovery in Biodiesel Production Process Using a Distillation Column: A Simulation Study. Chemical Engineering Research Bulletin, 13(2), 55–60. https://doi.org/10.3329/cerb.v13i2.3538

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Articles