Model-based identifiable parameter determination applied to a simultaneous saccharification and fermentation process model for bio-ethanol production

In this work, a methodology for the model-based identifiable parameter determination (MBIPD) is presented. This systematic approach is proposed to be used for structure and parameter identification of nonlinear models of biological reaction networks. Usually, this kind of problems are over-parameter...

Full description

Autores:
Villegas Quiceno, Adriana patricia
Tipo de recurso:
Article of journal
Fecha de publicación:
2023
Institución:
Universidad Cooperativa de Colombia
Repositorio:
Repositorio UCC
Idioma:
OAI Identifier:
oai:repository.ucc.edu.co:20.500.12494/50060
Acceso en línea:
https://doi.org/10.1002/btpr.1753
https://www.scopus.com/inward/record.uri?eid=2-s2.0-84881611828&doi=10.1002%2fbtpr.1753&partnerID=40&md5=ab2e130c83c53679261911f94e3133fb
https://hdl.handle.net/20.500.12494/50060
Palabra clave:
ALCOHOL
ALGORITHM
ALGORITHMS
ARTICLE
BIOETHANOL
BIO-ETHANOL
BIO-ETHANOLS
BIOLOGICAL MODEL
BIOTECHNOLOGY
ETHANOL
FERMENTATION
IDENTIFIABILITY ANALYSIS
ILL POSED PROBLEM
ILL-POSED PROBLEM
INVERSE PROBLEMS
ITERATIVE METHODS
METABOLISM
MODELS, BIOLOGICAL
NONLINEAR DYNAMICS
NON-LINEAR LEAST SQUARES
NONLINEAR LEAST SQUARES PARAMETER ESTIMATION
NONLINEAR SYSTEM
PARAMETER ESTIMATION
PARAMETER SUBSET SELECTION
PARAMETER SUBSETS
SSF PROCESS
SUGARCANE BAGASSE
SUGAR-CANE BAGASSE
Rights
openAccess
License
http://purl.org/coar/access_right/c_abf2
Description
Summary:In this work, a methodology for the model-based identifiable parameter determination (MBIPD) is presented. This systematic approach is proposed to be used for structure and parameter identification of nonlinear models of biological reaction networks. Usually, this kind of problems are over-parameterized with large correlations between parameters. Hence, the related inverse problems for parameter determination and analysis are mathematically ill-posed and numerically difficult to solve. The proposed MBIPD methodology comprises several tasks: (i) model selection, (ii) tracking of an adequate initial guess, and (iii) an iterative parameter estimation step which includes an identifiable parameter subset selection (SsS) algorithm and accuracy analysis of the estimated parameters. The SsS algorithm is based on the analysis of the sensitivity matrix by rank revealing factorization methods. Using this, a reduction of the parameter search space to a reasonable subset, which can be reliably and efficiently estimated from available measurements, is achieved. The simultaneous saccharification and fermentation (SSF) process for bio-ethanol production from cellulosic material is used as case study for testing the methodology. The successful application of MBIPD to the SSF process demonstrates a relatively large reduction in the identified parameter space. It is shown by a cross-validation that using the identified parameters (even though the reduction of the search space), the model is still able to predict the experimental data properly. Moreover, it is shown that the model is easily and efficiently adapted to new process conditions by solving reduced and well conditioned problems. © 2013 American Institute of Chemical Engineers.