Zepeda Valencia, Ivonne Gabriela | CINVESTAV |
Morles Díaz, América | CINVESTAV |
Sanchez, Arturo | CINVESTAV |
Resumen: This paper presents a design of a backstepping control for the hemicellulose fraction existent in lignocellulosic materials used at the first stage of the process of biofuels productions called pretreatment, which is carried out in a continuous tubular reactor. The nonlinear backstepping controller designed regulates the hemicellulose fraction at the output of the process to a desired value. Local asymptotic stability is guaranteed by the proposed Lyapunov functions. The control is successfully validated in simulations employing real data from the continuous tubular reactor process.
¿Cómo citar?
Gabriela Zepeda, América Morales & Arturo Sánchez. Backstepping Control of the Hemicellulose Fraction of Lignocellulosic Biomass in a Pretreatment Continuous Tubular Reactor for Biofuels Production. Memorias del Congreso Nacional de Control Automático, pp. 231-236, 2018.
Palabras clave
hemicellulose fraction, backstepping control, lignocellulosic biomass, pretreatment reactor
Referencias
- Abdelkarim, A., Jouili, K., and Braiek, N.B. (2016). Global Stabilization of Switched Nonlinear Systems Using Backstepping Approach: Applications to Chemical Processes, 655–668. Springer International Publishing.
- Alvira, P., Tomás-Pejó, E., Ballesteros, M., and Negro, M. (2010). Pretreatment technologies for an efficient bioethanol production process based on enzymatic hydrolysis: A review. Bioresource Technology, 101(13), 4851 – 4861.
- Biswas, P. and Samanta, A.N. (2013). Backstepping control of polymerization reactor. IEEE, 1–5.
- Bosković, D.M. and Krstić, M. (2002). Backstepping control of chemical tubular reactors. Computers and Chemical Engineering, 26(7), 1077 – 1085.
- Cajíca, I.J. and Sanchez, A. (2018). Mass flow dynamic modeling and residence time control of a continuous tubular reactor for biomass pretreatment. ASC sustainable chemistry and en engineering journal.
- González-Figueredo, C., Sánchez, A., Díaz, G., Rodríguez, F., Flores, R., Ceballos, M., Puente, R., and Ruiz, H. (2015). Dynamic modelling and experimental validation of a pilot-scale tubular continuous reactor for the autohydrolysis of lignocellulosic materials. Elsevier, 37, 431 – 436.
- Hua, C., Liu, P.X., and Guan, X. (2009). Backstepping control for nonlinear systems with time delays and applications to chemical reactor systems. IEEE Transactions on Industrial Electronics, 56(9), 3723–3732.
- Koppram, R., Tomás-Pejó, E., Xiros, C., and Olsson, L. (2014). Lignocellulosic ethanol production at highgravity: challenges and perspectives. Trends in Biotechnology, 32(1), 46 – 53.
- Krstic, M., Kanellakopoulos, I., and Kokotovic, P. (1992). Adaptive nonlinear control with overparametrization. Systems and Control Letters, 19, 177–185.
- Mosier, N., Wyman, C., Dale, B., Elander, R., Lee, Y., Holtzapple, M., and Ladisch, M. (2005). Features of promising technologies for pretreatment of lignocellulosic biomass. Bioresource Technology, 96(6), 673 – 686.
- Rodríguez, F. (2018). Modelado dinámico de la depolimerización de xilanos de biomasa lignocelulósica en un reactor de pretratamiento tubular continuo. Tesis de doctorado, CINVESTAV Unidad Guadalajara.
- Smyshlyaev, A. and Krstić, M. (2004). Output feedback boundary control by backstepping and application to chemical tubular reactor. American control conference, 1, 261–266 vol.1.
- Zhao, Z., Capparella, T., Ferrio, J., Wassick, J.M., and Ydstie, B.E. (2017). Passivity-based backstepping control of a semi-batch reactor. IFAC-PapersOnLine, 50(1), 13741 – 13746.