TY - JOUR
T1 - Implementation of heat integration to improve the sustainability of an integrated biodiesel biorefinery
AU - Kastritis, Dimitrios
AU - Vlysidis, Anestis
AU - Perry, Simon
AU - Theodoropoulos, Constantinos
PY - 2012
Y1 - 2012
N2 - Recently, a great research effort has been dedicated in order to establish integrated biorefineries as the next generation plants for the production of fuels, energy and chemicals. In this work, heat integration techniques are applied to an integrated biodiesel biorefinery that as well as biodiesel it also produces succinic acid through a fermentation process in order to improve its economic efficiency. Initially, heat integration options are identified by extracting the thermodynamic results of the overall biorefinery from simulations carried out in Aspen Plus 2006.5. By implementing pinch analysis and stochastic optimisation techniques, we determine a new heat exchanger network (HEN) that shows a minimum total annualised cost (TAC) of the overall HEN. The optimisation of the HEN results in a 17.2 % reduction in the TAC and 62.3 % and 64.2 % reduction in the hot and cold utilities, respectively, compared to the initial plant. Copyright © 2012, AIDIC Servizi S.r.l.
AB - Recently, a great research effort has been dedicated in order to establish integrated biorefineries as the next generation plants for the production of fuels, energy and chemicals. In this work, heat integration techniques are applied to an integrated biodiesel biorefinery that as well as biodiesel it also produces succinic acid through a fermentation process in order to improve its economic efficiency. Initially, heat integration options are identified by extracting the thermodynamic results of the overall biorefinery from simulations carried out in Aspen Plus 2006.5. By implementing pinch analysis and stochastic optimisation techniques, we determine a new heat exchanger network (HEN) that shows a minimum total annualised cost (TAC) of the overall HEN. The optimisation of the HEN results in a 17.2 % reduction in the TAC and 62.3 % and 64.2 % reduction in the hot and cold utilities, respectively, compared to the initial plant. Copyright © 2012, AIDIC Servizi S.r.l.
U2 - 10.3303/CET1229072
DO - 10.3303/CET1229072
M3 - Article
SN - 1974-9791
VL - 29
SP - 427
EP - 432
JO - Chemical Engineering Transactions
JF - Chemical Engineering Transactions
ER -