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  • Source: Computers and Chemical Engineering. Unidade: EP

    Assunto: CONTROLE PREDITIVO

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      HINOJOSA CALVO, Aldo Ignacio et al. One-layer gradient-based MPC + RTO of a propylene/propane splitter. Computers and Chemical Engineering, v. 106, p. 160-170, 2017Tradução . . Disponível em: https://doi.org/10.1016/j.compchemeng.2017.06.006. Acesso em: 05 jun. 2024.
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      Hinojosa Calvo, A. I., Ferramosca, A., Gonzalez, A. H., & Odloak, D. (2017). One-layer gradient-based MPC + RTO of a propylene/propane splitter. Computers and Chemical Engineering, 106, 160-170. doi:10.1016/j.compchemeng.2017.06.006
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      Hinojosa Calvo AI, Ferramosca A, Gonzalez AH, Odloak D. One-layer gradient-based MPC + RTO of a propylene/propane splitter [Internet]. Computers and Chemical Engineering. 2017 ; 106 160-170.[citado 2024 jun. 05 ] Available from: https://doi.org/10.1016/j.compchemeng.2017.06.006
    • Vancouver

      Hinojosa Calvo AI, Ferramosca A, Gonzalez AH, Odloak D. One-layer gradient-based MPC + RTO of a propylene/propane splitter [Internet]. Computers and Chemical Engineering. 2017 ; 106 160-170.[citado 2024 jun. 05 ] Available from: https://doi.org/10.1016/j.compchemeng.2017.06.006
  • Source: Computers and Chemical Engineering. Conference titles: International Symposium on Process Systems Engineering. Unidades: EACH, EP

    Subjects: AUTÔMATOS CELULARES, PETRÓLEO, PROCESSOS QUÍMICOS (OTIMIZAÇÃO)

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      BRESCIANI, Antonio Esio et al. Modeling the kinetics of the coalescence of water droplets in crude oil emulsions subject to an electric field, with the cellular automata technique. Computers and Chemical Engineering. New York: Escola de Artes, Ciências e Humanidades, Universidade de São Paulo. Disponível em: https://doi.org/10.1016/j.compchemeng.2010.07.006. Acesso em: 05 jun. 2024. , 2010
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      Bresciani, A. E., Mendonça Neto, C. F. X. de, Alves, R. M. de B., & Nascimento, C. A. O. do. (2010). Modeling the kinetics of the coalescence of water droplets in crude oil emulsions subject to an electric field, with the cellular automata technique. Computers and Chemical Engineering. New York: Escola de Artes, Ciências e Humanidades, Universidade de São Paulo. doi:10.1016/j.compchemeng.2010.07.006
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      Bresciani AE, Mendonça Neto CFX de, Alves RM de B, Nascimento CAO do. Modeling the kinetics of the coalescence of water droplets in crude oil emulsions subject to an electric field, with the cellular automata technique [Internet]. Computers and Chemical Engineering. 2010 ; 34( 12): 1962-1968.[citado 2024 jun. 05 ] Available from: https://doi.org/10.1016/j.compchemeng.2010.07.006
    • Vancouver

      Bresciani AE, Mendonça Neto CFX de, Alves RM de B, Nascimento CAO do. Modeling the kinetics of the coalescence of water droplets in crude oil emulsions subject to an electric field, with the cellular automata technique [Internet]. Computers and Chemical Engineering. 2010 ; 34( 12): 1962-1968.[citado 2024 jun. 05 ] Available from: https://doi.org/10.1016/j.compchemeng.2010.07.006
  • Source: Computers and Chemical Engineering. Unidade: EP

    Subjects: CONTROLE PREDITIVO, ESTABILIDADE DE SISTEMAS, OTIMIZAÇÃO MATEMÁTICA, PROGRAMAÇÃO NÃO LINEAR

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      SOUZA, Glauce Freitas de e ODLOAK, Darci e ZANIN, Antônio Carlos. Real time optimization (RTO) with model predictive control MPC. Computers and Chemical Engineering, v. 34, n. 12, p. 1999-2006, 2010Tradução . . Disponível em: https://doi.org/10.1016/j.compchemeng.2010.07.001. Acesso em: 05 jun. 2024.
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      Souza, G. F. de, Odloak, D., & Zanin, A. C. (2010). Real time optimization (RTO) with model predictive control MPC. Computers and Chemical Engineering, 34( 12), 1999-2006. doi:10.1016/j.compchemeng.2010.07.001
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      Souza GF de, Odloak D, Zanin AC. Real time optimization (RTO) with model predictive control MPC [Internet]. Computers and Chemical Engineering. 2010 ;34( 12): 1999-2006.[citado 2024 jun. 05 ] Available from: https://doi.org/10.1016/j.compchemeng.2010.07.001
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      Souza GF de, Odloak D, Zanin AC. Real time optimization (RTO) with model predictive control MPC [Internet]. Computers and Chemical Engineering. 2010 ;34( 12): 1999-2006.[citado 2024 jun. 05 ] Available from: https://doi.org/10.1016/j.compchemeng.2010.07.001
  • Source: Computers and Chemical Engineering. Unidade: EP

    Subjects: CONTROLE PREDITIVO, OTIMIZAÇÃO MATEMÁTICA, ESTABILIDADE DE SISTEMAS

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      ALVAREZ TORO, Luz Adriana e ODLOAK, Darci. Robust integration of real time optimization with linear model predictive control. Computers and Chemical Engineering, v. 34, n. 12, p. 1937-1944, 2010Tradução . . Disponível em: https://doi.org/10.1016/j.compchemeng.2010.06.017. Acesso em: 05 jun. 2024.
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      Alvarez Toro, L. A., & Odloak, D. (2010). Robust integration of real time optimization with linear model predictive control. Computers and Chemical Engineering, 34( 12), 1937-1944. doi:10.1016/j.compchemeng.2010.06.017
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      Alvarez Toro LA, Odloak D. Robust integration of real time optimization with linear model predictive control [Internet]. Computers and Chemical Engineering. 2010 ;34( 12): 1937-1944.[citado 2024 jun. 05 ] Available from: https://doi.org/10.1016/j.compchemeng.2010.06.017
    • Vancouver

      Alvarez Toro LA, Odloak D. Robust integration of real time optimization with linear model predictive control [Internet]. Computers and Chemical Engineering. 2010 ;34( 12): 1937-1944.[citado 2024 jun. 05 ] Available from: https://doi.org/10.1016/j.compchemeng.2010.06.017
  • Source: Computers and Chemical Engineering. Unidade: EP

    Subjects: DISTRIBUIÇÃO LOGÍSTICA, INDÚSTRIA PETROQUÍMICA, ÓLEOS COMBUSTÍVEIS, OTIMIZAÇÃO MATEMÁTICA, PLANEJAMENTO DA PRODUÇÃO, PROGRAMAÇÃO MATEMÁTICA, REFINARIAS

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      REJOWSKI JUNIOR, Rubens e PINTO, José Maurício. A novel continuous time representation for the scheduling of pipeline systems with pumping yield rate constraints. Computers and Chemical Engineering, v. 32, n. 4-5, p. 1042-1066, 2008Tradução . . Disponível em: https://doi.org/10.1016/j.compchemeng.2007.06.021. Acesso em: 05 jun. 2024.
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      Rejowski Junior, R., & Pinto, J. M. (2008). A novel continuous time representation for the scheduling of pipeline systems with pumping yield rate constraints. Computers and Chemical Engineering, 32( 4-5), 1042-1066. doi:10.1016/j.compchemeng.2007.06.021
    • NLM

      Rejowski Junior R, Pinto JM. A novel continuous time representation for the scheduling of pipeline systems with pumping yield rate constraints [Internet]. Computers and Chemical Engineering. 2008 ; 32( 4-5): 1042-1066.[citado 2024 jun. 05 ] Available from: https://doi.org/10.1016/j.compchemeng.2007.06.021
    • Vancouver

      Rejowski Junior R, Pinto JM. A novel continuous time representation for the scheduling of pipeline systems with pumping yield rate constraints [Internet]. Computers and Chemical Engineering. 2008 ; 32( 4-5): 1042-1066.[citado 2024 jun. 05 ] Available from: https://doi.org/10.1016/j.compchemeng.2007.06.021
  • Source: Computers and Chemical Engineering. Unidade: EP

    Subjects: CADEIA DE SUPRIMENTOS (ADMINISTRAÇÃO), INDÚSTRIA QUÍMICA, MÉTODOS DE DECOMPOSIÇÃO, MODELOS MATEMÁTICOS, OTIMIZAÇÃO MATEMÁTICA, PROGRAMAÇÃO NÃO LINEAR, PRODUÇÃO CONTÍNUA (OTIMIZAÇÃO)

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      CHEN, Peter e PINTO, José Maurício. Lagrangean-based techniques for the supply chain management of flexible process networks. Computers and Chemical Engineering, v. No, n. 11, p. 2505-2528, 2008Tradução . . Disponível em: https://doi.org/10.1016/j.compchemeng.2007.12.006. Acesso em: 05 jun. 2024.
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      Chen, P., & Pinto, J. M. (2008). Lagrangean-based techniques for the supply chain management of flexible process networks. Computers and Chemical Engineering, No( 11), 2505-2528. doi:10.1016/j.compchemeng.2007.12.006
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      Chen P, Pinto JM. Lagrangean-based techniques for the supply chain management of flexible process networks [Internet]. Computers and Chemical Engineering. 2008 ; No( 11): 2505-2528.[citado 2024 jun. 05 ] Available from: https://doi.org/10.1016/j.compchemeng.2007.12.006
    • Vancouver

      Chen P, Pinto JM. Lagrangean-based techniques for the supply chain management of flexible process networks [Internet]. Computers and Chemical Engineering. 2008 ; No( 11): 2505-2528.[citado 2024 jun. 05 ] Available from: https://doi.org/10.1016/j.compchemeng.2007.12.006
  • Source: Computers and Chemical Engineering. Unidade: EP

    Subjects: MODELOS MATEMÁTICOS (APLICAÇÕES), PLANEJAMENTO DA PRODUÇÃO, PROCESSOS QUÍMICOS (OTIMIZAÇÃO), PROGRAMAÇÃO MATEMÁTICA, REFINARIAS

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      MICHELETTO, Sandra Regina e CARVALHO, Maria Cristina Alves e PINTO, José Maurício. Operational optimization of the utility system of an oil refinery. Computers and Chemical Engineering, v. 32, n. Ja, p. 170-185, 2008Tradução . . Disponível em: https://doi.org/10.1016/j.compchemeng.2007.05.013. Acesso em: 05 jun. 2024.
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      Micheletto, S. R., Carvalho, M. C. A., & Pinto, J. M. (2008). Operational optimization of the utility system of an oil refinery. Computers and Chemical Engineering, 32( Ja), 170-185. doi:10.1016/j.compchemeng.2007.05.013
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      Micheletto SR, Carvalho MCA, Pinto JM. Operational optimization of the utility system of an oil refinery [Internet]. Computers and Chemical Engineering. 2008 ; 32( Ja): 170-185.[citado 2024 jun. 05 ] Available from: https://doi.org/10.1016/j.compchemeng.2007.05.013
    • Vancouver

      Micheletto SR, Carvalho MCA, Pinto JM. Operational optimization of the utility system of an oil refinery [Internet]. Computers and Chemical Engineering. 2008 ; 32( Ja): 170-185.[citado 2024 jun. 05 ] Available from: https://doi.org/10.1016/j.compchemeng.2007.05.013
  • Source: Computers and Chemical Engineering. Unidade: EP

    Subjects: INDÚSTRIA PETROQUÍMICA, MODELOS MATEMÁTICOS, ÓLEOS COMBUSTÍVEIS, OTIMIZAÇÃO MATEMÁTICA, PROCESSOS QUÍMICOS, PROGRAMAÇÃO MATEMÁTICA, REFINARIAS

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      CASAS LIZA, Jorge e PINTO, José Maurício. Optimal scheduling of a lube oil and paraffin production plant. Computers and Chemical Engineering, v. 29, n. 6, p. 1329-1344, 2005Tradução . . Disponível em: https://doi.org/10.1016/s1570-7946(04)80215-3. Acesso em: 05 jun. 2024.
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      Casas Liza, J., & Pinto, J. M. (2005). Optimal scheduling of a lube oil and paraffin production plant. Computers and Chemical Engineering, 29( 6), 1329-1344. doi:10.1016/s1570-7946(04)80215-3
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      Casas Liza J, Pinto JM. Optimal scheduling of a lube oil and paraffin production plant [Internet]. Computers and Chemical Engineering. 2005 ;29( 6): 1329-1344.[citado 2024 jun. 05 ] Available from: https://doi.org/10.1016/s1570-7946(04)80215-3
    • Vancouver

      Casas Liza J, Pinto JM. Optimal scheduling of a lube oil and paraffin production plant [Internet]. Computers and Chemical Engineering. 2005 ;29( 6): 1329-1344.[citado 2024 jun. 05 ] Available from: https://doi.org/10.1016/s1570-7946(04)80215-3
  • Source: Computers and Chemical Engineering. Unidade: EP

    Subjects: DISTRIBUIÇÃO LOGÍSTICA, DUTOS, PLANEJAMENTO DA PRODUÇÃO, PROGRAMAÇÃO MATEMÁTICA, PROGRAMAÇÃO DA PRODUÇÃO

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      REJOWSKI JUNIOR, Rubens e PINTO, José Maurício. Efficient MILP formulations and valid cuts for multiproduct pipeline scheduling. Computers and Chemical Engineering, v. 28, n. 8, p. 1511-1528, 2004Tradução . . Disponível em: https://doi.org/10.1016/j.compchemeng.2003.12.001. Acesso em: 05 jun. 2024.
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      Rejowski Junior, R., & Pinto, J. M. (2004). Efficient MILP formulations and valid cuts for multiproduct pipeline scheduling. Computers and Chemical Engineering, 28( 8), 1511-1528. doi:10.1016/j.compchemeng.2003.12.001
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      Rejowski Junior R, Pinto JM. Efficient MILP formulations and valid cuts for multiproduct pipeline scheduling. [Internet]. Computers and Chemical Engineering. 2004 ;28( 8): 1511-1528.[citado 2024 jun. 05 ] Available from: https://doi.org/10.1016/j.compchemeng.2003.12.001
    • Vancouver

      Rejowski Junior R, Pinto JM. Efficient MILP formulations and valid cuts for multiproduct pipeline scheduling. [Internet]. Computers and Chemical Engineering. 2004 ;28( 8): 1511-1528.[citado 2024 jun. 05 ] Available from: https://doi.org/10.1016/j.compchemeng.2003.12.001
  • Source: Computers and Chemical Engineering. Unidade: EP

    Subjects: DISTRIBUIÇÃO LOGÍSTICA, PETRÓLEO, PLANEJAMENTO DA PRODUÇÃO, PROGRAMAÇÃO MATEMÁTICA, PROGRAMAÇÃO DA PRODUÇÃO, REFINARIAS

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      NEIRO, Sérgio Mauro da Silva e PINTO, José Maurício. A general modeling framework for the operational planning of petroleum supply chains. Computers and Chemical Engineering, v. 28, n. ju 2004., p. 871-896, 2004Tradução . . Disponível em: https://doi.org/10.1016/j.compchemeng.2003.09.018. Acesso em: 05 jun. 2024.
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      Neiro, S. M. da S., & Pinto, J. M. (2004). A general modeling framework for the operational planning of petroleum supply chains. Computers and Chemical Engineering, 28( ju 2004.), 871-896. doi:10.1016/j.compchemeng.2003.09.018
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      Neiro SM da S, Pinto JM. A general modeling framework for the operational planning of petroleum supply chains. [Internet]. Computers and Chemical Engineering. 2004 ;28( ju 2004.): 871-896.[citado 2024 jun. 05 ] Available from: https://doi.org/10.1016/j.compchemeng.2003.09.018
    • Vancouver

      Neiro SM da S, Pinto JM. A general modeling framework for the operational planning of petroleum supply chains. [Internet]. Computers and Chemical Engineering. 2004 ;28( ju 2004.): 871-896.[citado 2024 jun. 05 ] Available from: https://doi.org/10.1016/j.compchemeng.2003.09.018
  • Source: Computers and Chemical Engineering. Unidade: EP

    Subjects: INDÚSTRIA QUÍMICA, OTIMIZAÇÃO MATEMÁTICA, PROCESSOS QUÍMICOS, PRODUÇÃO INDUSTRIAL (OTIMIZAÇÃO), PROGRAMAÇÃO MATEMÁTICA, PROGRAMAÇÃO NÃO LINEAR

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      ALLE, Alessandro e PAPAGEORGIOU, Lazaros G. e PINTO, José Maurício. A mathematical programming approach for cyclic production and cleaning scheduling of multistage continuous plants. Computers and Chemical Engineering, v. 28, n. ja 2004., p. 3-15, 2004Tradução . . Disponível em: https://doi.org/10.1016/s0098-1354(03)00171-6. Acesso em: 05 jun. 2024.
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      Alle, A., Papageorgiou, L. G., & Pinto, J. M. (2004). A mathematical programming approach for cyclic production and cleaning scheduling of multistage continuous plants. Computers and Chemical Engineering, 28( ja 2004.), 3-15. doi:10.1016/s0098-1354(03)00171-6
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      Alle A, Papageorgiou LG, Pinto JM. A mathematical programming approach for cyclic production and cleaning scheduling of multistage continuous plants. [Internet]. Computers and Chemical Engineering. 2004 ;28( ja 2004.): 3-15.[citado 2024 jun. 05 ] Available from: https://doi.org/10.1016/s0098-1354(03)00171-6
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      Alle A, Papageorgiou LG, Pinto JM. A mathematical programming approach for cyclic production and cleaning scheduling of multistage continuous plants. [Internet]. Computers and Chemical Engineering. 2004 ;28( ja 2004.): 3-15.[citado 2024 jun. 05 ] Available from: https://doi.org/10.1016/s0098-1354(03)00171-6
  • Source: Computers and Chemical Engineering. Unidade: EP

    Subjects: CONTROLE DE PROCESSOS, COMPUTADORES, ENGENHARIA QUÍMICA

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      PINTO, José Maurício e CRISALLE, Oscar D. The 2nd Pan American Workshop on Process Systems Engineering..[Prefácio]. Computers and Chemical Engineering. New York: Escola Politécnica, Universidade de São Paulo. . Acesso em: 05 jun. 2024. , 2003
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      Pinto, J. M., & Crisalle, O. D. (2003). The 2nd Pan American Workshop on Process Systems Engineering..[Prefácio]. Computers and Chemical Engineering. New York: Escola Politécnica, Universidade de São Paulo.
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      Pinto JM, Crisalle OD. The 2nd Pan American Workshop on Process Systems Engineering..[Prefácio]. Computers and Chemical Engineering. 2003 ; 27 1041.[citado 2024 jun. 05 ]
    • Vancouver

      Pinto JM, Crisalle OD. The 2nd Pan American Workshop on Process Systems Engineering..[Prefácio]. Computers and Chemical Engineering. 2003 ; 27 1041.[citado 2024 jun. 05 ]
  • Source: Computers and Chemical Engineering. Unidades: EP, IQ

    Subjects: DESTILAÇÃO AZEOTRÓPICA, REDES NEURAIS, SISTEMA BINÁRIO

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      ALVES, Rita Maria de Brito e QUINA, Frank Herbert e NASCIMENTO, Cláudio Augusto Oller do. New approach for the prediction of azeotropy in binary systems. Computers and Chemical Engineering, v. 27, n. 12, p. 1755-1759, 2003Tradução . . Disponível em: https://doi.org/10.1016/s0098-1354(03)00150-9. Acesso em: 05 jun. 2024.
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      Alves, R. M. de B., Quina, F. H., & Nascimento, C. A. O. do. (2003). New approach for the prediction of azeotropy in binary systems. Computers and Chemical Engineering, 27( 12), 1755-1759. doi:10.1016/s0098-1354(03)00150-9
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      Alves RM de B, Quina FH, Nascimento CAO do. New approach for the prediction of azeotropy in binary systems [Internet]. Computers and Chemical Engineering. 2003 ;27( 12): 1755-1759.[citado 2024 jun. 05 ] Available from: https://doi.org/10.1016/s0098-1354(03)00150-9
    • Vancouver

      Alves RM de B, Quina FH, Nascimento CAO do. New approach for the prediction of azeotropy in binary systems [Internet]. Computers and Chemical Engineering. 2003 ;27( 12): 1755-1759.[citado 2024 jun. 05 ] Available from: https://doi.org/10.1016/s0098-1354(03)00150-9
  • Source: Computers and Chemical Engineering. Unidade: EP

    Subjects: CONTROLE PREDITIVO, MODELOS MATEMÁTICOS, SISTEMAS INTEGRADOS EM LARGA ESCALA

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      RODRIGUES, Marco Antonio e ODLOAK, Darci. An Infinite horizon model predictive control for stable and integrating processes. Computers and Chemical Engineering, v. 27, n. 8-9, p. 1113-1128, 2003Tradução . . Disponível em: https://doi.org/10.1016/s0098-1354(03)00040-1. Acesso em: 05 jun. 2024.
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      Rodrigues, M. A., & Odloak, D. (2003). An Infinite horizon model predictive control for stable and integrating processes. Computers and Chemical Engineering, 27( 8-9), 1113-1128. doi:10.1016/s0098-1354(03)00040-1
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      Rodrigues MA, Odloak D. An Infinite horizon model predictive control for stable and integrating processes [Internet]. Computers and Chemical Engineering. 2003 ; 27( 8-9): 1113-1128.[citado 2024 jun. 05 ] Available from: https://doi.org/10.1016/s0098-1354(03)00040-1
    • Vancouver

      Rodrigues MA, Odloak D. An Infinite horizon model predictive control for stable and integrating processes [Internet]. Computers and Chemical Engineering. 2003 ; 27( 8-9): 1113-1128.[citado 2024 jun. 05 ] Available from: https://doi.org/10.1016/s0098-1354(03)00040-1
  • Source: Computers and Chemical Engineering. Unidade: EP

    Subjects: DERIVADOS DE PETRÓLEO, DISTRIBUIÇÃO LOGÍSTICA, OTIMIZAÇÃO MATEMÁTICA, PETRÓLEO, TUBULAÇÕES

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      REJOWSKI JUNIOR, Rubens e PINTO, José Maurício. Scheduling of a multiproduct pipeline system. Computers and Chemical Engineering, v. 27, n. 8-9, p. 1229-1246, 2003Tradução . . Disponível em: https://doi.org/10.1016/s0098-1354(03)00049-8. Acesso em: 05 jun. 2024.
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      Rejowski Junior, R., & Pinto, J. M. (2003). Scheduling of a multiproduct pipeline system. Computers and Chemical Engineering, 27( 8-9), 1229-1246. doi:10.1016/s0098-1354(03)00049-8
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      Rejowski Junior R, Pinto JM. Scheduling of a multiproduct pipeline system [Internet]. Computers and Chemical Engineering. 2003 ; 27( 8-9): 1229-1246.[citado 2024 jun. 05 ] Available from: https://doi.org/10.1016/s0098-1354(03)00049-8
    • Vancouver

      Rejowski Junior R, Pinto JM. Scheduling of a multiproduct pipeline system [Internet]. Computers and Chemical Engineering. 2003 ; 27( 8-9): 1229-1246.[citado 2024 jun. 05 ] Available from: https://doi.org/10.1016/s0098-1354(03)00049-8
  • Source: Computers and Chemical Engineering. Unidade: EP

    Subjects: MODELOS MATEMÁTICOS, POLIMERIZAÇÃO (OTIMIZAÇÃO), REATORES QUÍMICOS

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      ARAUJO, Pedro Henrique Hermes de e GIUDICI, Reinaldo. Optimization of semicontinuous emulsion polymerization reactions by IDP procedure with variable time intervals. Computers and Chemical Engineering, v. 27, n. 8-9, p. 1345-1360, 2003Tradução . . Disponível em: https://doi.org/10.1016/S0098-1354(03)00057-7. Acesso em: 05 jun. 2024.
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      Araujo, P. H. H. de, & Giudici, R. (2003). Optimization of semicontinuous emulsion polymerization reactions by IDP procedure with variable time intervals. Computers and Chemical Engineering, 27( 8-9), 1345-1360. doi:10.1016/S0098-1354(03)00057-7
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      Araujo PHH de, Giudici R. Optimization of semicontinuous emulsion polymerization reactions by IDP procedure with variable time intervals [Internet]. Computers and Chemical Engineering. 2003 ; 27( 8-9): 1345-1360.[citado 2024 jun. 05 ] Available from: https://doi.org/10.1016/S0098-1354(03)00057-7
    • Vancouver

      Araujo PHH de, Giudici R. Optimization of semicontinuous emulsion polymerization reactions by IDP procedure with variable time intervals [Internet]. Computers and Chemical Engineering. 2003 ; 27( 8-9): 1345-1360.[citado 2024 jun. 05 ] Available from: https://doi.org/10.1016/S0098-1354(03)00057-7
  • Source: Computers and Chemical Engineering. Unidade: EP

    Subjects: BIOTECNOLOGIA, PROCESSOS QUÍMICOS

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      ASENJO, Juan A et al. Strategies for the simultaneous optimization of the structure and the process variables of a protein production plant. Computers and Chemical Engineering, v. 24, p. 2277-2290, 2000Tradução . . Disponível em: https://doi.org/10.1016/s0098-1354(00)00572-x. Acesso em: 05 jun. 2024.
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      Asenjo, J. A., Montagna, J. M., Vecchietti, A. R., Iribarren, O. A., & Pinto, J. M. (2000). Strategies for the simultaneous optimization of the structure and the process variables of a protein production plant. Computers and Chemical Engineering, 24, 2277-2290. doi:10.1016/s0098-1354(00)00572-x
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      Asenjo JA, Montagna JM, Vecchietti AR, Iribarren OA, Pinto JM. Strategies for the simultaneous optimization of the structure and the process variables of a protein production plant [Internet]. Computers and Chemical Engineering. 2000 ; 24 2277-2290.[citado 2024 jun. 05 ] Available from: https://doi.org/10.1016/s0098-1354(00)00572-x
    • Vancouver

      Asenjo JA, Montagna JM, Vecchietti AR, Iribarren OA, Pinto JM. Strategies for the simultaneous optimization of the structure and the process variables of a protein production plant [Internet]. Computers and Chemical Engineering. 2000 ; 24 2277-2290.[citado 2024 jun. 05 ] Available from: https://doi.org/10.1016/s0098-1354(00)00572-x
  • Source: Computers and Chemical Engineering. Unidade: EP

    Assunto: PROCESSOS QUÍMICOS

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      NASCIMENTO, Cláudio Augusto Oller do e GIUDICI, Reinaldo e GUARDANI, Roberto. Neural network based approach for optimization of industrial chemical processes. Computers and Chemical Engineering, v. 24, n. 9/10, p. 2302-2314, 2000Tradução . . Disponível em: https://doi.org/10.1016/S0098-1354(00)00587-1. Acesso em: 05 jun. 2024.
    • APA

      Nascimento, C. A. O. do, Giudici, R., & Guardani, R. (2000). Neural network based approach for optimization of industrial chemical processes. Computers and Chemical Engineering, 24( 9/10), 2302-2314. doi:10.1016/S0098-1354(00)00587-1
    • NLM

      Nascimento CAO do, Giudici R, Guardani R. Neural network based approach for optimization of industrial chemical processes [Internet]. Computers and Chemical Engineering. 2000 ; 24( 9/10): 2302-2314.[citado 2024 jun. 05 ] Available from: https://doi.org/10.1016/S0098-1354(00)00587-1
    • Vancouver

      Nascimento CAO do, Giudici R, Guardani R. Neural network based approach for optimization of industrial chemical processes [Internet]. Computers and Chemical Engineering. 2000 ; 24( 9/10): 2302-2314.[citado 2024 jun. 05 ] Available from: https://doi.org/10.1016/S0098-1354(00)00587-1
  • Source: Computers and Chemical Engineering. Unidade: EP

    Subjects: ENGENHARIA QUÍMICA, REFINARIAS, MODELOS MATEMÁTICOS

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    • ABNT

      PINTO, José Maurício e JOLY, Marcel e MORO, Lincoln Fernando Lautenschlager. Planning and scheduling models for refinery operations. Computers and Chemical Engineering, v. 24, n. 9/10, p. 2259-2276, 2000Tradução . . Disponível em: https://doi.org/10.1016/s0098-1354(00)00571-8. Acesso em: 05 jun. 2024.
    • APA

      Pinto, J. M., Joly, M., & Moro, L. F. L. (2000). Planning and scheduling models for refinery operations. Computers and Chemical Engineering, 24( 9/10), 2259-2276. doi:10.1016/s0098-1354(00)00571-8
    • NLM

      Pinto JM, Joly M, Moro LFL. Planning and scheduling models for refinery operations [Internet]. Computers and Chemical Engineering. 2000 ; 24( 9/10): 2259-2276.[citado 2024 jun. 05 ] Available from: https://doi.org/10.1016/s0098-1354(00)00571-8
    • Vancouver

      Pinto JM, Joly M, Moro LFL. Planning and scheduling models for refinery operations [Internet]. Computers and Chemical Engineering. 2000 ; 24( 9/10): 2259-2276.[citado 2024 jun. 05 ] Available from: https://doi.org/10.1016/s0098-1354(00)00571-8
  • Source: Computers and Chemical Engineering. Unidade: EP

    Subjects: PROCESSOS QUÍMICOS, TRATAMENTO DE ÁGUAS RESIDUÁRIAS, REFINARIAS

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    • ABNT

      ZANIN, Antônio Carlos e GOUVÊA, Míriam Tvrzská de e ODLOAK, Darci. Industrial implementation of a real-time optimization strategy for maximizing production of LPG in a FCC unit. Computers and Chemical Engineering, v. 24, n. 2/7, p. 525-531, 2000Tradução . . Disponível em: https://doi.org/10.1016/s0098-1354(00)00524-x. Acesso em: 05 jun. 2024.
    • APA

      Zanin, A. C., Gouvêa, M. T. de, & Odloak, D. (2000). Industrial implementation of a real-time optimization strategy for maximizing production of LPG in a FCC unit. Computers and Chemical Engineering, 24( 2/7), 525-531. doi:10.1016/s0098-1354(00)00524-x
    • NLM

      Zanin AC, Gouvêa MT de, Odloak D. Industrial implementation of a real-time optimization strategy for maximizing production of LPG in a FCC unit [Internet]. Computers and Chemical Engineering. 2000 ; 24( 2/7): 525-531.[citado 2024 jun. 05 ] Available from: https://doi.org/10.1016/s0098-1354(00)00524-x
    • Vancouver

      Zanin AC, Gouvêa MT de, Odloak D. Industrial implementation of a real-time optimization strategy for maximizing production of LPG in a FCC unit [Internet]. Computers and Chemical Engineering. 2000 ; 24( 2/7): 525-531.[citado 2024 jun. 05 ] Available from: https://doi.org/10.1016/s0098-1354(00)00524-x

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