1 - 2 |
Hydroprocessing of heavy oil fractions Ancheyta J, Rana MS, Furimsky E |
3 - 15 |
Hydroprocessing of heavy petroleum feeds: Tutorial Ancheyta J, Rana MS, Furimsky E |
16 - 23 |
Effect of nitrogen removal from light cycle oil on the hydrodesulphurization of dibenzothiophene, 4-methyldibenzothiophene and 4,6-dimethyldibenzothiophene Yang H, Chen JW, Briker Y, Szynkarczuk R, Ring Z |
24 - 32 |
Comparative study for heavy oil hydroprocessing catalysts at micro-flow and bench-scale reactors Rana MS, Ancheyta J, Rayo P |
33 - 41 |
Supported (NiMo, CoMo)-carbide, -nitride phases: Effect of atomic ratios and phosphorus concentration on the HDS of thiophene and dibenzothiophene Santillan-Vallejo LA, Melo-Banda JA, de la Torre AIR, Sandoval-Robles G, Dominguez JM, Montesinos-Castellanos A, de los Reyes-Heredia JA |
42 - 48 |
Effect of phosphorus on activity of hydrotreating catalyst of Maya heavy crude Maity SK, Ancheyta J, Rana MS, Rayo P |
49 - 53 |
First principles study of heavy oil organonitrogen adsorption on NiMoS hydrotreating catalysts Sun MY, Nelson AE, Adjaye J |
54 - 60 |
Analysis of the hydrotreatment of Maya heavy crude with NiMo catalysts supported on TiO2-Al2O3 binary oxides - Effect of the incorporation method of Ti Ramirez J, Rayo P, Gutierrez-Alejandre A, Ancheyta J, Rana MS |
61 - 68 |
Maya crude hydrodemetallization and hydrodesulfurization catalysts: An effect of TiO2 incorporation in Al2O3 Rana MS, Ancheyta J, Maity SK, Rayo P |
69 - 75 |
Long-term evaluation of NiMo/alumina-carbon black composite catalysts in hydroconversion of Mexican 538 degrees C+ vacuum residue Lopez-Salinas E, Espinosa JG, Hernandez-Cortez JG, Sanchez-Valente J, Nagira J |
76 - 92 |
Kinetic modeling of hydrocracking of heavy oil fractions: A review Ancheyta J, Sanchez S, Rodriguez MA |
93 - 98 |
Study of intra-particle diffusion effect on hydrodesulphurization of dibenzothiophenic compounds Chen JW, Yang H, Ring Z |
99 - 103 |
Kinetics of asphaltenes conversion during hydrotreating of Maya crude Trejo F, Ancheyta J |
104 - 111 |
Hydroconversion kinetics of Marlim vacuum residue de Almeida RM, Guirardello R |
112 - 119 |
Effects of organic nitrogen compounds on hydrotreating and hydrocracking reactions Sau M, Basak K, Manna U, Santra M, Verma RP |
120 - 127 |
Experimental and theoretical determination of the particle size of hydrotreating catalysts of different shapes Ancheyta J, Munoz JAD, Macias MJ |
128 - 134 |
Modelling of hydrodesulfurization catalysts II. Effects of catalyst pore structures on deactivation by metal deposits Oyekunle LO, Ikpekri OB, Jaiyeola A |
135 - 153 |
THERMIDOR: A new model for combined simulation of operations and optimization of catalysts in residues hydroprocessing units Toulhoat H, Hudebine D, Raybaud P, Guillaume D, Kressmann S |
154 - 161 |
Characterising high mass materials in heavy oil fractions by size exclusion chromatography and MALDI-mass spectrometry Millan M, Behrouzi M, Karaca F, Morgan TJ, Herod AA, Kandiyoti R |
162 - 166 |
Asphaltene characterization as function of time on-stream during hydroprocessing of Maya crude Ancheyta J, Centeno G, Trejo F, Speight JG |
167 - 177 |
Investigation of the mechanism of sediment formation in residual oil hydrocracking process through characterization of sediment deposits Stanislaus A, Hauser A, Marafi M |
178 - 184 |
Effect of hydrotreating conditions on Maya asphaltenes composition and structural parameters Trejo F, Ancheyta J, Centeno G, Marroquin G |
185 - 194 |
Catalyst pore plugging effects on hydrocracking reactions in an Ebullated bed reactor operation Tailleur RG, Caprioli L |
195 - 204 |
Estimating thermochemical properties of hydroprocessing reactions by molecular simulation and group contribution methods Rajagopal K, Ahon VR, Moreno E |
205 - 213 |
Pressure and temperature effects on the hydrodynamic characteristics of ebullated-bed systems Ruiz RS, Alonso F, Ancheyta J |
214 - 218 |
Process heat integration of a heavy crude hydrotreatment plant Munoz JAD, Alvarez A, Ancheyta J, Rodriguez MA, Marroquin G |