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(Referência obtida automaticamente do Web of Science, por meio da informação sobre o financiamento pela FAPESP e o número do processo correspondente, incluída na publicação pelos autores.)

A simple approach to improve the robustness of equation-oriented simulators: Multilinear look-up table interpolators

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Autor(es):
Furlan, Felipe Fernando [1] ; de Andrade Lino, Anderson Rodrigo [2] ; Matugi, Karina [1] ; Goncalves Cruz, Antonio Jose [1, 2] ; Secchi, Argimiro Resende [3] ; Giordano, Roberto de Campos [1, 2]
Número total de Autores: 6
Afiliação do(s) autor(es):
[1] Univ Fed Sao Carlos UFSCar, Chem Engn Grad Program, Rodovia Washington Luis SP 310, Km 235, BR-13565905 Sao Carlos, SP - Brazil
[2] Univ Fed Sao Carlos UFSCar, Dept Chem Engn, UFSCar, Rodovia Washington Luis SP 310, Km 235, BR-13565905 Sao Carlos, SP - Brazil
[3] Univ Fed Rio de Janeiro, UFRJ, COPPE, Chem Engn Grad Program, Cidade Univ, BR-21941972 Rio De Janeiro, RJ - Brazil
Número total de Afiliações: 3
Tipo de documento: Artigo Científico
Fonte: Computers & Chemical Engineering; v. 86, p. 1-4, MAR 4 2016.
Citações Web of Science: 2
Resumo

Equation-oriented simulators have some advantages over the modular sequential ones, but improvements are still necessary to deal with nonlinearities, while preserving the robustness of the solver. Linear approximations and/or surrogate models can be used in place of nonlinear models, but the loss of predictive accuracy may be a drawback. An alternative to circumvent this problem is the use of grid-based look-up tables for interpolating responses from rigorous models. This methodology was integrated in an equation-oriented simulator (EMSO). A case study involving the production of bioethanol from sugarcane is used to demonstrate the robustness of this approach. Look-up tables replaced the models of two distillation column trains and of the cellulose hydrolysis reactor. These models were included into the global process and an optimization problem aiming at the maximum production of ethanol was successfully solved by a PSO algorithm varying the solid mass fraction in the hydrolysis reactor. (C) 2015 Elsevier Ltd. All rights reserved. (AU)

Processo FAPESP: 08/56246-0 - Bioprocess Systems Engineering (BSE) applied to the production of bioethanol from sugarcane bagasse
Beneficiário:Roberto de Campos Giordano
Linha de fomento: Auxílio à Pesquisa - Programa BIOEN - Temático
Processo FAPESP: 09/13325-0 - Desenvolvimento de um ambiente integrado para simulação e otimização estática da produção de etanol a partir do bagaço de cana-de-açúcar por rota bioquímica
Beneficiário:Felipe Fernando Furlan
Linha de fomento: Bolsas no Brasil - Mestrado