Iván Peréz-Gallegos | Universidad Veracruzana-Región Xalapa |
Victor M. Rivera | Universidad Veracruzana-Región Xalapa |
Eliseo Hernandez-Martinez | Universidad Veracruzana-Región Xalapa |
Claudio B.-Arroyo | Universidad de Guadalajaraa |
https://doi.org/10.58571/CNCA.AMCA.2022.088
Resumen: In this work, a methodology for the integration of design and control methods for distillation columns through dynamic optimization tools is proposed. For this, a dynamic model of the distillation column that can be adapted to different mixtures (binary and multicomponent) is established. The proposal focuses on defining an objective function to simultaneously maximize the performance in the mixture separation under the lowest energy consumption. The design variables (i.e., number of trays and feeding stage), as well as the controller parameters, are considered as decision variables. The results obtained show that it is possible to improve the overall performance of the distillation column, compared to traditional strategies.
¿Cómo citar?
Iván Peréz-Gallegos, Claudio B.-Arroyo, Victor M. Rivera & Eliseo Hernandez-Martinez. Integration of design and control for distillation columns through dynamic optimization. Memorias del Congreso Nacional de Control Automático, pp. 469-473, 2022. https://doi.org/10.58571/CNCA.AMCA.2022.088
Palabras clave
Control de Procesos; Control Óptimo; Sistemas de Parámetros Distribuidos
Referencias
- Henley, E.J., & Seader, J.D. (1990) Operaciones de separación por etapas de equilibrio en ingeniería química. México: Reverte.
- Treybal R.E. (1988). Operaciones de transferencia de masa. México: Mc Graw Hill
- Smith, C.A., & Corripio, A.B. (1991). Control automático de procesos. Teoría y práctica. México: Editorial Limusa.
- Jiang, Z., & Agrawal, R. (2019). Process intensification in multicomponent distillation: A review. Chemical Engineering Research and Design, 147, 122-145.
- Lecuona, N. E. S., Aldaco, A. T., Leyte, R. L., & González, E. V. T. (2017) Estudios de los consumos de energía en un sistema de evaporación con compresión y re-compresión. 13º Congreso Iberoamericano de Ingeniería Mecánica.
- Cui, C., Zhang, X., Lyu, H., Wang, S., Sun, J., Qu, Y., & Zhang, Q. (2021). Process intensification in ternary distillation via comparative grassroots and retrofit designs. Chemical Engineering and Processing-Process Intensification, 164, 108423.
- Salas-Aguilar, C. L., Bonilla-Petriciolet, A., & Jaime-Leal, J. E. (2018). Optimización multi-bjetivo del desempeño y consumo energético de procesos de destilación intensificados para sistemas cuaternarios. Afinidad, 75(582).
- Gutiérrez G, De Prada C (2003). Diseño Integrado y Síntesis de Procesos Químicos. Universidad de Valladolid. España. 1-6.
- Biasi, L. C., Romano, A. L., Zemp, R. J., Heinkenschloss, M., Batista, F. R., & Meirelles, A. J. (2021). Distillation Columns with Multiple Phase Divisions: How They Improve Thermodynamic Efficiency and Decrease Energy Consumption. Industrial & Engineering Chemistry Research, 60(43), 15690-15705.
- Luyben, W. L. (2012). Principles and case studies of simultaneous design. John Wiley & Sons.
- Skogestad, S. (2003). Simple analytic rules for model reduction and PID controller tuning. Journal of process control, 13(4), 291-309.