TY - JOUR
T1 - Modelling batch bioreactions with continuous process simulators
AU - Zhang, Yechun
AU - Munir, Muhammad Tajammal
AU - Yu, Wei
AU - Young, Brent Richmond
N1 - Publisher Copyright:
© 2016, Korean Institute of Chemical Engineers, Seoul, Korea.
PY - 2016/12/1
Y1 - 2016/12/1
N2 - Process models are increasingly becoming necessary for process understanding and optimizing. However, in the field of bioprocessing, modelling using a generic process simulator suffers from shortcomings given that many simulators cannot model batch mode bioreactors with varying reaction rates based on microbial metabolism. Bioprocesses, mostly batch, are difficult to model because most of the available unit operations in process simulators operate continuously. Our aim is to provide a general simulation platform to model these batch bioprocesses in commercial process simulators and explain how to transform batch processes with varying reaction rate into continuous unit operations for simulation purposes. Two typical fermentation processes, lactose fermentation and glucose/xylose co-fermentation, were simulated in steady state as case studies. The results are discussed as examples using the proposed approach. The potential of how to extend the simulation platform is also explained in detail.
AB - Process models are increasingly becoming necessary for process understanding and optimizing. However, in the field of bioprocessing, modelling using a generic process simulator suffers from shortcomings given that many simulators cannot model batch mode bioreactors with varying reaction rates based on microbial metabolism. Bioprocesses, mostly batch, are difficult to model because most of the available unit operations in process simulators operate continuously. Our aim is to provide a general simulation platform to model these batch bioprocesses in commercial process simulators and explain how to transform batch processes with varying reaction rate into continuous unit operations for simulation purposes. Two typical fermentation processes, lactose fermentation and glucose/xylose co-fermentation, were simulated in steady state as case studies. The results are discussed as examples using the proposed approach. The potential of how to extend the simulation platform is also explained in detail.
KW - Batch Processing
KW - Bioreactor
KW - Dairy Processing
KW - Process Simulation
UR - http://www.scopus.com/inward/record.url?scp=84991075577&partnerID=8YFLogxK
U2 - 10.1007/s11814-016-0244-x
DO - 10.1007/s11814-016-0244-x
M3 - Article
AN - SCOPUS:84991075577
SN - 0256-1115
VL - 33
SP - 3343
EP - 3349
JO - Korean Journal of Chemical Engineering
JF - Korean Journal of Chemical Engineering
IS - 12
ER -