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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: 16 jun. 2025.
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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 2025 jun. 16 ] 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 2025 jun. 16 ] Available from: https://doi.org/10.1016/j.compchemeng.2017.06.006
  • 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: 16 jun. 2025.
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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 2025 jun. 16 ] 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 2025 jun. 16 ] 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: 16 jun. 2025.
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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 2025 jun. 16 ] Available from: https://doi.org/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 2025 jun. 16 ] Available from: https://doi.org/10.1016/j.compchemeng.2010.06.017
  • Source: Computers and Chemical Engineering. Unidade: EP

    Subjects: 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: 16 jun. 2025.
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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 2025 jun. 16 ] 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 2025 jun. 16 ] 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: 16 jun. 2025.
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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
    • NLM

      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 2025 jun. 16 ] 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 2025 jun. 16 ] 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: 16 jun. 2025.
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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 2025 jun. 16 ] 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 2025 jun. 16 ] 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: 16 jun. 2025.
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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 2025 jun. 16 ] 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 2025 jun. 16 ] Available from: https://doi.org/10.1016/s1570-7946(04)80215-3
  • Source: Computers and Chemical Engineering. Unidade: EP

    Subjects: 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: 16 jun. 2025.
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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 2025 jun. 16 ] 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 2025 jun. 16 ] Available from: https://doi.org/10.1016/j.compchemeng.2003.12.001
  • 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: 16 jun. 2025.
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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 2025 jun. 16 ] 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 2025 jun. 16 ] Available from: https://doi.org/10.1016/s0098-1354(03)00171-6
  • Source: Computers and Chemical Engineering. Unidade: EP

    Subjects: 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: 16 jun. 2025.
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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 2025 jun. 16 ] 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 2025 jun. 16 ] Available from: https://doi.org/10.1016/j.compchemeng.2003.09.018
  • 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: 16 jun. 2025. , 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 2025 jun. 16 ]
    • Vancouver

      Pinto JM, Crisalle OD. The 2nd Pan American Workshop on Process Systems Engineering..[Prefácio]. Computers and Chemical Engineering. 2003 ; 27 1041.[citado 2025 jun. 16 ]
  • 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: 16 jun. 2025.
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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 2025 jun. 16 ] 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 2025 jun. 16 ] 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: 16 jun. 2025.
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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 2025 jun. 16 ] 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 2025 jun. 16 ] Available from: https://doi.org/10.1016/s0098-1354(03)00040-1
  • Source: Computers and Chemical Engineering. Unidade: EP

    Subjects: DERIVADOS DE PETRÓLEO, 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: 16 jun. 2025.
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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 2025 jun. 16 ] 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 2025 jun. 16 ] 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: 16 jun. 2025.
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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 2025 jun. 16 ] 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 2025 jun. 16 ] 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: 16 jun. 2025.
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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 2025 jun. 16 ] 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 2025 jun. 16 ] 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: 16 jun. 2025.
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      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
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      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 2025 jun. 16 ] 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 2025 jun. 16 ] 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: 16 jun. 2025.
    • 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 2025 jun. 16 ] 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 2025 jun. 16 ] 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: 16 jun. 2025.
    • 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 2025 jun. 16 ] 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 2025 jun. 16 ] Available from: https://doi.org/10.1016/s0098-1354(00)00524-x
  • Source: Computers and Chemical Engineering. Unidade: EP

    Subjects: PROCESSOS QUÍMICOS (OTIMIZAÇÃO), POLUIÇÃO DA ÁGUA, LODO ATIVADO

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    • ABNT

      GOUVEIA, R. e PINTO, José Maurício. Optimal operating policies in activated sludge treatment plants. Computers and Chemical Engineering, p. 5863-5866, 1999Tradução . . Disponível em: https://doi.org/10.1016/s0098-1354(99)80212-9. Acesso em: 16 jun. 2025.
    • APA

      Gouveia, R., & Pinto, J. M. (1999). Optimal operating policies in activated sludge treatment plants. Computers and Chemical Engineering, 5863-5866. doi:10.1016/s0098-1354(99)80212-9
    • NLM

      Gouveia R, Pinto JM. Optimal operating policies in activated sludge treatment plants [Internet]. Computers and Chemical Engineering. 1999 ; 5863-5866.[citado 2025 jun. 16 ] Available from: https://doi.org/10.1016/s0098-1354(99)80212-9
    • Vancouver

      Gouveia R, Pinto JM. Optimal operating policies in activated sludge treatment plants [Internet]. Computers and Chemical Engineering. 1999 ; 5863-5866.[citado 2025 jun. 16 ] Available from: https://doi.org/10.1016/s0098-1354(99)80212-9

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