Article ID | Journal | Published Year | Pages | File Type |
---|---|---|---|---|
657435 | International Journal of Heat and Mass Transfer | 2014 | 8 Pages |
Abstract
This paper concerns techno-economic optimization of the production process of raw ethanol in a continuous distillation column as a part of the plant for production of rectified alcohol. Optimization was performed in order to determine the optimal ethanol concentration in the residue, which provides the minimum total production costs of existing plant. Total production costs are determined on the basis of experimental data, investment and operating costs and the estimated working life of the plant. It was found that ethanol concentration in the residue is significantly higher than values that can be found in the open literature.
Keywords
Related Topics
Physical Sciences and Engineering
Chemical Engineering
Fluid Flow and Transfer Processes
Authors
Branislav M. Jaćimović, Srbislav B. Genić, Nikola J. Budimir, Marko S. Jarić,