TY - JOUR
T1 - Energy Efficient Bioethanol Purification by Heat Pump Assisted Extractive Distillation
AU - Kiss, Anton A.
AU - Luo, Hao
AU - Bildea, Costin Sorin
PY - 2015
Y1 - 2015
N2 - The purification of bioethanol fuel requires an energy demanding separation process to concentrate the diluted streams obtained in the fermentation stage and to overcome the azeotropic behaviour of ethanol-water mixture. The classic separation sequence consists of three distillation columns that carry out several energy demanding tasks: pre-concentration of ethanol, extractive distillation and solvent recovery. To solve this problem, we propose a novel heat pump assisted extractive distillation process taking place in a dividing-wall column (DWC). In this configuration, the ethanol top vapour stream of the extractive DWC is recompressed from atmospheric pressure to over 3.1. bar (thus to a higher temperature) and used to drive the side reboiler of the DWC, which is responsible for the water vaporization. The results show that the specific energy requirements drop from 2.07 kWh/kg (classic sequence) to only 1.24 kWh/kg ethanol (VRC assisted extractive DWC), thus energy savings of over 40 % and 24 % reduced total annual costs are possible, as compared to the conventional process.
AB - The purification of bioethanol fuel requires an energy demanding separation process to concentrate the diluted streams obtained in the fermentation stage and to overcome the azeotropic behaviour of ethanol-water mixture. The classic separation sequence consists of three distillation columns that carry out several energy demanding tasks: pre-concentration of ethanol, extractive distillation and solvent recovery. To solve this problem, we propose a novel heat pump assisted extractive distillation process taking place in a dividing-wall column (DWC). In this configuration, the ethanol top vapour stream of the extractive DWC is recompressed from atmospheric pressure to over 3.1. bar (thus to a higher temperature) and used to drive the side reboiler of the DWC, which is responsible for the water vaporization. The results show that the specific energy requirements drop from 2.07 kWh/kg (classic sequence) to only 1.24 kWh/kg ethanol (VRC assisted extractive DWC), thus energy savings of over 40 % and 24 % reduced total annual costs are possible, as compared to the conventional process.
KW - Dividing-wall column
KW - Energy savings
KW - Extractive distillation
KW - Heat pump
UR - http://www.scopus.com/inward/record.url?scp=84940488445&partnerID=8YFLogxK
U2 - 10.1016/B978-0-444-63577-8.50063-2
DO - 10.1016/B978-0-444-63577-8.50063-2
M3 - Article
AN - SCOPUS:84940488445
SN - 1570-7946
VL - 37
SP - 1307
EP - 1312
JO - Computer Aided Chemical Engineering
JF - Computer Aided Chemical Engineering
ER -