Rafael Maya Yescas
Rafael Maya Yescas
Facultad de Ingeniería Química, Universidad
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Cited by
Cited by
The fluidized-bed catalytic cracking unit building its future environment
G Jiménez-García, R Aguilar-López, R Maya-Yescas
Fuel 90 (12), 3531-3541, 2011
State estimation for nonlinear systems under model uncertainties: a class of sliding-mode observers
R Aguilar-López, R Maya-Yescas
Journal of Process Control 15 (3), 363-370, 2005
Temperature control in catalytic cracking reactors via a robust PID controller
R Aguilar, A Poznyak, R Martı́nez-Guerra, R Maya-Yescas
Journal of Process Control 12 (6), 695-705, 2002
State estimation for partially unknown nonlinear systems: a class of integral high gain observers
R Aguilar, R Martínez-Guerra, R Maya-Yescas
IEE Proceedings-Control Theory and Applications 150 (3), 240-244, 2003
Robust PI2 controller for continuous bioreactors
R Aguilar, J González, M Barrón, R Martınez-Guerra, R Maya-Yescas
Process Biochemistry 36 (10), 1007-1013, 2001
Polyphenolic content and bactericidal effect of Mexican Citrus limetta and Citrus reticulata
AA Damián-Reyna, JC González-Hernández, R Maya-Yescas, ...
Journal of food science and technology 54, 531-537, 2017
Heterogeneous acid conversion of a tricaprylin-palmitic acid mixture over Al-SBA-15 catalysts: Reaction study for biodiesel synthesis
DA Cabrera-Munguia, H González, A Gutiérrez-Alejandre, JL Rico, ...
Catalysis today 282, 195-203, 2017
Catalyst activity decay due to pore blockage during catalytic cracking of hydrocarbons
G Jiménez-García, H de Lasa, R Quintana-Solórzano, R Maya-Yescas
Fuel 110, 89-98, 2013
Effect of hydrotreating FCC feedstock on product distribution
D Salazar-Sotelo, R Maya-Yescas, E Mariaca-Domínguez, ...
Catalysis today 98 (1-2), 273-280, 2004
Controllability assessment approach for chemical reactors: nonlinear control affine systems
R Maya-Yescas, R Aguilar
Chemical Engineering Journal 92 (1-3), 69-79, 2003
Synthesis, characterization and catalytic activity during hydrodesulphurization of dibenzothiophene of NiMoW catalysts supported on AlTi mixed oxides modified with MgO
ME Cervantes-Gaxiola, M Arroyo-Albiter, R Maya-Yescas, JL Rico-Cerda, ...
Fuel 100, 57-65, 2012
Approach to the analysis of the dynamics of industrial FCC units
R Maya-Yescas, D Bogle, F López-Isunza
Journal of Process Control 8 (2), 89-100, 1998
Effect of modelling pressure gradient in the simulation of industrial FCC risers
E León-Becerril, R Maya-Yescas, D Salazar-Sotelo
Chemical Engineering Journal 100 (1-3), 181-186, 2004
Reactions analysis during the synthesis of pseudo-boehmite as precursor of gamma-alumina
G Toledo-Chávez, JC Paniagua-Rodríguez, J Zárate-Medina, ...
Catalysis Today 271, 207-212, 2016
Optimization and controllability analysis of thermally coupled reactive distillation arrangements with minimum use of reboilers
M Vázquez-Ojeda, JG Segovia-Hernández, S Hernández, ...
Industrial & engineering chemistry research 51 (17), 5856-5865, 2012
Design study of the control of a reactive thermally coupled distillation sequence for the esterification of fatty organic acids
S Hernandez, JG Segovia-Hernandez, L Juarez-Trujillo, ...
Chemical Engineering Communications 198 (1), 1-18, 2010
Tracking catalyst activity during fluidized-bed catalytic cracking
G Jimenez-Garcia, R Aguilar-López, E León-Becerril, R Maya-Yescas
Industrial & Engineering Chemistry Research 48 (3), 1220-1227, 2009
Modelling catalyst deactivation by external coke deposition during fluid catalytic cracking
G Jiménez-García, R Quintana-Solórzano, R Aguilar-López, ...
International Journal of Chemical Reactor Engineering 8 (1), 2010
Enhancement of dibenzothiophene hydrodesulphurization via hydrogenation route on NiMoW catalyst supported on HMS modified with Ti
PJ Vázquez-Salas, R Huirache-Acuña, TA Zepeda, G Alonso-Núñez, ...
Catalysis Today 305, 65-74, 2018
Simulation of syngas production from lignin using guaiacol as a model compound
NE Rodríguez-Olalde, EA Mendoza-Chávez, AJ Castro-Montoya, ...
Energies 8 (7), 6705-6714, 2015
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