Filtros : "PC-SAFT" Limpar

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  • Source: Journal of solution chemistry. Unidade: EEL

    Assunto: ENGENHARIA QUÍMICA

    Acesso à fonteDOIHow to cite
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    • ABNT

      BACICHETI, Jacqueline Mansano Ortega et al. Phase Equilibria of {Carbon Dioxide-+-Acetone-+-Dimethyl Sulfoxide} Systems: Experimental Data and Thermodynamic Modeling. Journal of solution chemistry, v. 51, p. 1292-1309, 2022Tradução . . Disponível em: https://doi.org/10.1007/s10953-022-01196-6. Acesso em: 05 jan. 2026.
    • APA

      Bacicheti, J. M. O., Oliveira, J. A., Barros, T. V., Pinto, L. F., Castillo, P. F. A., Cabral, V. F., & Cardozo-Filho, L. (2022). Phase Equilibria of {Carbon Dioxide-+-Acetone-+-Dimethyl Sulfoxide} Systems: Experimental Data and Thermodynamic Modeling. Journal of solution chemistry, 51, 1292-1309. doi:10.1007/s10953-022-01196-6
    • NLM

      Bacicheti JMO, Oliveira JA, Barros TV, Pinto LF, Castillo PFA, Cabral VF, Cardozo-Filho L. Phase Equilibria of {Carbon Dioxide-+-Acetone-+-Dimethyl Sulfoxide} Systems: Experimental Data and Thermodynamic Modeling [Internet]. Journal of solution chemistry. 2022 ;51 1292-1309.[citado 2026 jan. 05 ] Available from: https://doi.org/10.1007/s10953-022-01196-6
    • Vancouver

      Bacicheti JMO, Oliveira JA, Barros TV, Pinto LF, Castillo PFA, Cabral VF, Cardozo-Filho L. Phase Equilibria of {Carbon Dioxide-+-Acetone-+-Dimethyl Sulfoxide} Systems: Experimental Data and Thermodynamic Modeling [Internet]. Journal of solution chemistry. 2022 ;51 1292-1309.[citado 2026 jan. 05 ] Available from: https://doi.org/10.1007/s10953-022-01196-6
  • Source: Fluid phase equilibria. Unidade: EEL

    Assunto: EQUILÍBRIO SÓLIDO-LÍQUIDO

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    • ABNT

      BERNARDI, Fabiele et al. Xylitol solubility in DMF + ethylene glycol or 1,2-propylene glycol: Measurement and modeling with PC-SAFT and CPA equations of state and UNIFAC activity coefficient model. Fluid phase equilibria, v. 519, p. 112651-, 2020Tradução . . Disponível em: https://doi.org/10.1016/j.fluid.2020.112651. Acesso em: 05 jan. 2026.
    • APA

      Bernardi, F., Galvão, A. C., Castillo, P. F. A., Robazza, W. S., & Coleti, D. F. H. (2020). Xylitol solubility in DMF + ethylene glycol or 1,2-propylene glycol: Measurement and modeling with PC-SAFT and CPA equations of state and UNIFAC activity coefficient model. Fluid phase equilibria, 519, 112651-. doi:10.1016/j.fluid.2020.112651
    • NLM

      Bernardi F, Galvão AC, Castillo PFA, Robazza WS, Coleti DFH. Xylitol solubility in DMF + ethylene glycol or 1,2-propylene glycol: Measurement and modeling with PC-SAFT and CPA equations of state and UNIFAC activity coefficient model [Internet]. Fluid phase equilibria. 2020 ; 519 112651-.[citado 2026 jan. 05 ] Available from: https://doi.org/10.1016/j.fluid.2020.112651
    • Vancouver

      Bernardi F, Galvão AC, Castillo PFA, Robazza WS, Coleti DFH. Xylitol solubility in DMF + ethylene glycol or 1,2-propylene glycol: Measurement and modeling with PC-SAFT and CPA equations of state and UNIFAC activity coefficient model [Internet]. Fluid phase equilibria. 2020 ; 519 112651-.[citado 2026 jan. 05 ] Available from: https://doi.org/10.1016/j.fluid.2020.112651
  • Source: XI Iberoamerican Conference on Phase Equilibria and Fluid Properties for Process Design - EQUIFASE. Unidade: EEL

    Assunto: LÍQUIDOS IÔNICOS

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    • ABNT

      IGARASHI, Edson Massakazu de Souza e CASTILLO, Pedro Felipe Arce. Thermodynamic modeling of the fluid phase behavior of CO2 + IL (pyrrolidinium and phosphonium) at high pressures. 2018, Anais.. Cordoba: Universidad Nacional de Cordoba, 2018. p. 79-80. Disponível em: https://drive.google.com/file/d/16yPSoyXuKvCuBFv-O7dYN6_A-Mt9KLrH/view. Acesso em: 05 jan. 2026.
    • APA

      Igarashi, E. M. de S., & Castillo, P. F. A. (2018). Thermodynamic modeling of the fluid phase behavior of CO2 + IL (pyrrolidinium and phosphonium) at high pressures. In XI Iberoamerican Conference on Phase Equilibria and Fluid Properties for Process Design - EQUIFASE (p. 79-80). Cordoba: Universidad Nacional de Cordoba. Recuperado de https://drive.google.com/file/d/16yPSoyXuKvCuBFv-O7dYN6_A-Mt9KLrH/view
    • NLM

      Igarashi EM de S, Castillo PFA. Thermodynamic modeling of the fluid phase behavior of CO2 + IL (pyrrolidinium and phosphonium) at high pressures [Internet]. XI Iberoamerican Conference on Phase Equilibria and Fluid Properties for Process Design - EQUIFASE. 2018 ;79-80.[citado 2026 jan. 05 ] Available from: https://drive.google.com/file/d/16yPSoyXuKvCuBFv-O7dYN6_A-Mt9KLrH/view
    • Vancouver

      Igarashi EM de S, Castillo PFA. Thermodynamic modeling of the fluid phase behavior of CO2 + IL (pyrrolidinium and phosphonium) at high pressures [Internet]. XI Iberoamerican Conference on Phase Equilibria and Fluid Properties for Process Design - EQUIFASE. 2018 ;79-80.[citado 2026 jan. 05 ] Available from: https://drive.google.com/file/d/16yPSoyXuKvCuBFv-O7dYN6_A-Mt9KLrH/view
  • Source: Equifase 2018. Unidade: EEL

    Assunto: BIODIESEL

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    • ABNT

      FREIRE, Nian Vieira e CASTILLO, Pedro Felipe Arce. Thermodynamic modeling of the fluid phase behavior of binary systems involving biodiesel components at low and high pressures with the Group-Contribution Volume Translated Peng-Robinson and the PC-SAFT equations of state. 2018, Anais.. Cordoba: Universidad Nacional de Cordoba, 2018. p. 69-70. Disponível em: https://drive.google.com/file/d/16yPSoyXuKvCuBFv-O7dYN6_A-Mt9KLrH/view. Acesso em: 05 jan. 2026.
    • APA

      Freire, N. V., & Castillo, P. F. A. (2018). Thermodynamic modeling of the fluid phase behavior of binary systems involving biodiesel components at low and high pressures with the Group-Contribution Volume Translated Peng-Robinson and the PC-SAFT equations of state. In Equifase 2018 (p. 69-70). Cordoba: Universidad Nacional de Cordoba. Recuperado de https://drive.google.com/file/d/16yPSoyXuKvCuBFv-O7dYN6_A-Mt9KLrH/view
    • NLM

      Freire NV, Castillo PFA. Thermodynamic modeling of the fluid phase behavior of binary systems involving biodiesel components at low and high pressures with the Group-Contribution Volume Translated Peng-Robinson and the PC-SAFT equations of state [Internet]. Equifase 2018. 2018 ; 69-70.[citado 2026 jan. 05 ] Available from: https://drive.google.com/file/d/16yPSoyXuKvCuBFv-O7dYN6_A-Mt9KLrH/view
    • Vancouver

      Freire NV, Castillo PFA. Thermodynamic modeling of the fluid phase behavior of binary systems involving biodiesel components at low and high pressures with the Group-Contribution Volume Translated Peng-Robinson and the PC-SAFT equations of state [Internet]. Equifase 2018. 2018 ; 69-70.[citado 2026 jan. 05 ] Available from: https://drive.google.com/file/d/16yPSoyXuKvCuBFv-O7dYN6_A-Mt9KLrH/view
  • Source: XI Iberoamerican ConferenceE on phase equilibria and fluid properties for process design - EQUIFASE 2018. Unidade: EEL

    Subjects: EQUILÍBRIO LÍQUIDO-LÍQUIDO, LÍQUIDOS IÔNICOS

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    • ABNT

      CASTILLO, Pedro Felipe Arce. Fluid phase behavior of the Liquid-Liquid Equilibrium of ternary systems involving ionic liquids (solvent) and organic compounds: PC-SAFT equation vs Artificial Neural Networks. 2018, Anais.. Cordoba: Universidad Nacional de Cordoba, 2018. p. 67-68. Disponível em: https://drive.google.com/file/d/16yPSoyXuKvCuBFv-O7dYN6_A-Mt9KLrH/view. Acesso em: 05 jan. 2026.
    • APA

      Castillo, P. F. A. (2018). Fluid phase behavior of the Liquid-Liquid Equilibrium of ternary systems involving ionic liquids (solvent) and organic compounds: PC-SAFT equation vs Artificial Neural Networks. In XI Iberoamerican ConferenceE on phase equilibria and fluid properties for process design - EQUIFASE 2018 (p. 67-68). Cordoba: Universidad Nacional de Cordoba. Recuperado de https://drive.google.com/file/d/16yPSoyXuKvCuBFv-O7dYN6_A-Mt9KLrH/view
    • NLM

      Castillo PFA. Fluid phase behavior of the Liquid-Liquid Equilibrium of ternary systems involving ionic liquids (solvent) and organic compounds: PC-SAFT equation vs Artificial Neural Networks [Internet]. XI Iberoamerican ConferenceE on phase equilibria and fluid properties for process design - EQUIFASE 2018. 2018 ;67-68.[citado 2026 jan. 05 ] Available from: https://drive.google.com/file/d/16yPSoyXuKvCuBFv-O7dYN6_A-Mt9KLrH/view
    • Vancouver

      Castillo PFA. Fluid phase behavior of the Liquid-Liquid Equilibrium of ternary systems involving ionic liquids (solvent) and organic compounds: PC-SAFT equation vs Artificial Neural Networks [Internet]. XI Iberoamerican ConferenceE on phase equilibria and fluid properties for process design - EQUIFASE 2018. 2018 ;67-68.[citado 2026 jan. 05 ] Available from: https://drive.google.com/file/d/16yPSoyXuKvCuBFv-O7dYN6_A-Mt9KLrH/view
  • Source: Anais do X Congresso Brasileiro do Termodinâmica Aplicada (CBTermo). Unidade: EEL

    Assunto: BIODIESEL

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    • ABNT

      IGARASHI, Edson Massakazu de Souza e FREIRE, Nian Vieira e ARCE, Pedro F. Modelagem e simulação termodinâmica do equilíbrio de fases de sistemas binários contendo componentes do biodiesel a baixas e altas pressões. 2016, Anais.. Nova riburgo-RJ: UERJ, 2016. p. 1-8. Disponível em: http://www.cbtermo2019.uerj.br/arquivos/AnaisCBTermo2019.pdf. Acesso em: 05 jan. 2026.
    • APA

      Igarashi, E. M. de S., Freire, N. V., & Arce, P. F. (2016). Modelagem e simulação termodinâmica do equilíbrio de fases de sistemas binários contendo componentes do biodiesel a baixas e altas pressões. In Anais do X Congresso Brasileiro do Termodinâmica Aplicada (CBTermo) (p. 1-8). Nova riburgo-RJ: UERJ. Recuperado de http://www.cbtermo2019.uerj.br/arquivos/AnaisCBTermo2019.pdf
    • NLM

      Igarashi EM de S, Freire NV, Arce PF. Modelagem e simulação termodinâmica do equilíbrio de fases de sistemas binários contendo componentes do biodiesel a baixas e altas pressões [Internet]. Anais do X Congresso Brasileiro do Termodinâmica Aplicada (CBTermo). 2016 ;1-8.[citado 2026 jan. 05 ] Available from: http://www.cbtermo2019.uerj.br/arquivos/AnaisCBTermo2019.pdf
    • Vancouver

      Igarashi EM de S, Freire NV, Arce PF. Modelagem e simulação termodinâmica do equilíbrio de fases de sistemas binários contendo componentes do biodiesel a baixas e altas pressões [Internet]. Anais do X Congresso Brasileiro do Termodinâmica Aplicada (CBTermo). 2016 ;1-8.[citado 2026 jan. 05 ] Available from: http://www.cbtermo2019.uerj.br/arquivos/AnaisCBTermo2019.pdf

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