Dynamic simulation of a bioethanol distillation column in batch regime

Authors

  • Eliana Jara Morante Facultad de Ingeniería Química y Textil, Universidad Nacional de Ingeniería, Perú
  • Emerson Collado Dominguez Facultad de Ingeniería Química y Textil, Universidad Nacional de Ingeniería, Perú
  • Mario De la Cruz Azabache Facultad de Ingeniería Química y Textil, Universidad Nacional de Ingeniería, Perú
  • Magali Vivas Cuellar Facultad de Ingeniería Química y Textil, Universidad Nacional de Ingeniería, Perú

DOI:

https://doi.org/10.21754/tecnia.v21i1.95

Keywords:

batch distillation, bioethanol, simulation

Abstract

Batch distillation is a process used in many industrial processes, from small to big scale, therefore it has a great commercial interest. In the process simulation context it presents challenges due to the system complexity, especially in the startup stage because there are many variables changing simultaneously. This work simulates the distillation process of a bench plant installed in the Unit Operations Laboratory of the FIQT of the UNI. Commercial simulation software ASPEN Batch Distillation V7.1 is used. The results are useful to establish a protocol of operation that allows us to obtain high bioethanol purity and the improvement of the process. 

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References

[1] Jr.,Costa,E. F., Vieira,R. C.et al.,"Dynamic Simulation of High-Index Modelsof Batch Distillation Processes." LatinAmerican Applied Research33, pp. 155-160,2003.

[2] Arndt,Mehlhorn., A., Nougués, J.M.,Puigjaner, L.,“Using rate-based approachunder consideration of different contactingregimes for multicomponent”,Computers &Chemical Engineering,22, Sup. 1, pp.S645-S648,1998.

[3] Bonsfills, A., Puigjaner, L., "Batchdistillation: Simulation and ExperimentalValidation", Chemical Engineering andProcessing43, pp. 1239-1252, 2004.

[4] Wang, L., P. Li,et al,"A startup model forsimulation of batch distillation starting from acold state",Computers & ChemicalEngineering27(10), pp.1485-1497, (2003)

[5] Schneider, R., C. Noeres,et al.,“Dynamicmodeling and simulation of reactive batchdistillation", Computers& ChemicalEngineering25(1), pp. 169-176, (2001)

[6] Fang, J., Li,C.,et al.,"A Quasi-steady-stateModel for Numerical Simulation of BatchExtractive Distillation", Chinese Journal ofChemical Engineering18(1), pp. 43-47,(2010)

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Published

2011-06-01

How to Cite

[1]
E. Jara Morante, E. Collado Dominguez, M. De la Cruz Azabache, and M. Vivas Cuellar, “Dynamic simulation of a bioethanol distillation column in batch regime”, TECNIA, vol. 21, no. 1, pp. 39–45, Jun. 2011.

Issue

Vol. 21 No. 1 (2011)

Section

Articles

License

Copyright (c) 2011 TECNIA

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