Juan Hernández Espinosa | Tecnológico Nacional de México, Instituto Tecnológico de Orizaba |
Galo R. Urrea-García | Tecnológico Nacional de México, Instituto Tecnológico de Orizaba |
Guadalupe Luna Solano | Tecnológico Nacional de México, Instituto Tecnológico de Orizaba |
Denis Cantú-Lozano | Tecnológico Nacional de México, Instituto Tecnológico de Orizaba |
Resumen: The design and evaluation of a variable control structure to regulate the outlet concentration of a tubular reactor, affected by disturbances in the feed, together with a variation in the activation energy parameter, is presented. In the tubular reactor, the o-xylene oxidation process is carried out for the production of phthalic anhydride. The control scheme used consists of a primary loop to regulate the concentration at the reactor outlet and two secondary loops to control the temperature at two different points along the reactor, the input signal in the secondary controller is a combination of two measurements multiplied by a weighting factor. The variable control structure was compared with conventional control schemes, evaluated face disturbances in the reactor feed together with a variation in activation energy, determining that the variable control scheme adapts to the disturbances present in the process, highlighting the dynamic adjustment the weighting factor and quick response of the cooling medium.
¿Cómo citar?
Juan Hernández Espinosa, Galo R. Urrea-García, Guadalupe Luna Solano & Denis Cantú-Lozano. Adaptable Control Structure to Uncertainty Factors in a Tubular Reactor. Memorias del Congreso Nacional de Control Automático, pp. 1-6, 2020.
Palabras clave
Tubular reactor, hot spot, weighting factor, cooling medium, variable control
Referencias
- Anastasov, A.I., (2005). The behaviour of a low-productive non-pretreated V2O5-TiO2 (anatase) catalyst for oxidation of o-xylene to phthalic anhydride. Chemical Engineering Journal, 109, 57-66.
- González-Alatorre, G., Serrato-Joya, A., Sámano-Heras, C. A., Alvizar-Gómez, J. C., Rocha-Patiño, J. (2004). Nitrosacion de la dimetilurea en un reactor tubular que opera isotermicamente en estado estacionario y suponiendo flujo piston. Revista Mexicana de Ingenieria Quimica, Volume 3, pp. 249-256.
- Grimholt, C. and Skogestad, S. (2018). Optimal PI and PID control of first-order plus delay processes and evaluation of the original and improved SIMC rules. Journal of Process Control. 70, 36-46.
- Hernandez, M, E., Puebla, H., Álvarez, R, J. (2010). Cascade control scheme for tubular reactors with multiple temperature measurements. international journal of chemical reactor engineering, 8(1), 1542– 6580.
- Hua, X. y Jutan, A. (2000). Nonlinear inferential cascade control of exothermic fixed bed reactors. AIChE Journal, 46(5), 980-996.
- Jesus, J. M., Santana, P. L., Silva, F. V. (2013). Different approaches in concentration-temperature cascade control of a fixed bed reactor for the phthalic anhydride synthesis. Chemical Engineering Transactions, 32, 1387–1392.
- Loncar, D., Ban, M., Horvat, K. (2010). “Mathematical model and simulation of the dynamics of the lowdensity polyethylene polymerizat ion process in the tubular reactor”, Strojarstvo 52 (3) 315-325 (2010).
- Ojeda, T. J. C., Dobrosz. G. I., Gómez. G. M. A. (2014). Evaluación de la sensibilidad paramétrica del proceso de síntesis de la ciclonita en un reactor por lotes. Revista EIA, 11(21),123-132
- Ramírez, C. C. E., Moguel, C. J., Puebla, H., Hernandez, M. E. (2016). A study of temperature sensor location based on fractal analysis for cascade control schemes in tubular reactors. Chemical Engineering Science, 141, 195–204.
- Thiagalingam, I., Dallet, M., Bennaceur, I., Cadalen, S., Sagaut, P. (2015). Exact non-local expression for the wall heat transfer coefficient in tubular catalytic reactors. International journal of heat and fluid flow, 54, 97-106.
- Urrea, R., Alvarez, J., & Alvarez-Ramirez, J. (2008). Linear Pi Temperature-Concentration Cascade Control for Tubular Reactors. Chemical Engineering Communications, 195(7), 803–820.
- Urrea-García, G. R., Reséndiz-Camacho, S., Álvarez Ramírez, J., & Luna-Solano, G. (2015). Variable Cascade Control Structure for Tubular Reactors. Chemical Engineering & Technology, 38(3), 521–529.
- Wu, Wei. and Chen, Chao-Wei. (2007). MeasurementBased Optimization and Predictive Control for an Exothermic Tubular Reactor System. Ind. Eng. Chem. Res. 46, 2064-2076.