TY - CHAP
T1 - Modeling and identification of the bio-ethanol production process from starch
T2 - Cybernetic vs. unstructured modeling
AU - Ochoa, Silvia
AU - Yoo, Ahrim
AU - Repke, Jens Uwe
AU - Wozny, Günter
AU - Yang, Dae Ryook
PY - 2008
Y1 - 2008
N2 - In this work, an unstructured and a cybernetic model are proposed and compared for the Simultaneous Saccharification_- Fermentation process from Starch to Ethanol (SSFSE), in order to have good, reliable, and highly predictive models, which can be used in optimization and process control applications. The cybernetic is a novel model, which especially considers i) the starch degradation into both glucose and dextrins, and ii) the dynamic behavior of the concentration of the main enzymes involved in the intracellular processes, giving a more detailed description of the process. Furthermore, a new identification procedure based on a sensitivity index is proposed to identify the best set of parameters that not only minimizes the error function, but also contains a fewer number of parameters depending on the initial conditions of the process. Finally, an application of the two models for controlling the SSFSE process using an NMPC (following an optimal reference trajectory for the ethanol concentration) is presented, showing the potential and usefulness of each type of models.
AB - In this work, an unstructured and a cybernetic model are proposed and compared for the Simultaneous Saccharification_- Fermentation process from Starch to Ethanol (SSFSE), in order to have good, reliable, and highly predictive models, which can be used in optimization and process control applications. The cybernetic is a novel model, which especially considers i) the starch degradation into both glucose and dextrins, and ii) the dynamic behavior of the concentration of the main enzymes involved in the intracellular processes, giving a more detailed description of the process. Furthermore, a new identification procedure based on a sensitivity index is proposed to identify the best set of parameters that not only minimizes the error function, but also contains a fewer number of parameters depending on the initial conditions of the process. Finally, an application of the two models for controlling the SSFSE process using an NMPC (following an optimal reference trajectory for the ethanol concentration) is presented, showing the potential and usefulness of each type of models.
KW - Cybernetic Model
KW - Ethanol
KW - NMPC
KW - Parameter Identification
KW - Sensitivity Analysis
UR - http://www.scopus.com/inward/record.url?scp=53049095065&partnerID=8YFLogxK
U2 - 10.1016/S1570-7946(08)80123-X
DO - 10.1016/S1570-7946(08)80123-X
M3 - Chapter
AN - SCOPUS:53049095065
SN - 9780444532275
T3 - Computer Aided Chemical Engineering
SP - 707
EP - 712
BT - 18th European Symposium on Computer Aided Process Engineering
A2 - Braunschweig, Bertrand
A2 - Joulia, Xavier
ER -