265 - 266 |
International symposium on advances in hydroprocessing of oils fractions (ISHOF 2007) - Preface Ancheyta J, Fromenti GE |
267 - 271 |
Support effects in the hydrotreatment of model molecules Ramirez J, Sanchez-Minero F |
272 - 282 |
Genesis of new HDS catalysts through a careful control of the sulfidation of both Co and Mo atoms: Study of their activation under gas phase Frizi N, Blanchard P, Payen E, Baranek P, Rebeilleau M, Dupuy C, Dath JP |
283 - 291 |
Effect of the preparation method on the structural stability and hydrodesulfurization activity of NiMo/SBA-15 catalysts Rayo P, Rana MS, Ramirez J, Ancheyta J, Aguilar-Elguzabal A |
292 - 301 |
Deep HDS over NiMo/Zr-SBA-15 catalysts with varying MoO3 loading Gutierrez OY, Perez F, Fuentes GA, Bokhimi X, Klimova T |
302 - 308 |
Effect of Zr-SBA-15 support on catalytic functionalities of Mo, CoMo, NiMo hydrotreating catalysts Garg S, Soni K, Kumaran GM, Kumar M, Gupta JK, Sharma LD, Dhar GM |
309 - 319 |
Synthesis, characterization and catalytic properties of NiMo/Al2O3-MCM-41 catalyst for dibenzothiophene hydrodesulfurization Silva-Rodrigo R, Herndndez-Lpez F, Martinez-Juarez K, Castillo-Mares A, Banda JAM, Olivas-Sarabia A, Ancheyta J, Rana MS |
320 - 326 |
Transformation of thiophene, benzothiophene and dibenzothiophene over Pt/HMFI, Pt/HMOR and Pt/HFAU: Effect of reactant molecular dimensions and zeolite pore diameter over catalyst activity Contreras R, Cuevas-Garcia R, Ramirez J, Ruiz-Azuara L, Gutierrez-Alejandre A, Puente-Lee I, Castillo-Villalon P, Salcedo-Luna C |
327 - 336 |
CoMo/MgO-Al2O3 supported catalysts: An alternative approach to prepare HDS catalysts Trejo F, Rana MS, Ancheyta J |
337 - 344 |
Synthesis, characterization and evaluation of NiMo/SiO2-Al2O3 catalysts prepared by the pH-swing method Fernandez-Vargas C, Ramirez J, Gutierrez-Alejandre A, Sanchez-Minero F, Cuevas-Garcia R, Torres-Mancera P |
345 - 353 |
Surface characterization of Al2O3-SiO2 supported NiMo catalysts: An effect of support composition Leyva C, Rana MS, Ancheyta J |
354 - 360 |
Cyclohexene hydrogenation with molybdenum disulfide catalysts prepared by ex situ decomposition of ammonium thiomolybdate-cetyltrimethylammonium thiomolybdate mixtures Romero-Rivera R, Del Valle A, Alonso G, Flores E, Castillon F, Fuentes S, Cruz-Reyes J |
361 - 373 |
Life cycle of hydroprocessing catalysts and total catalyst management Eijsbouts S, Battiston AA, van Leerdam GC |
374 - 381 |
Effect of preparation methods and content of phosphorus on hydrotreating activity Maity SK, Flores GA, Ancheyta J, Rana MS |
382 - 388 |
Preparing and characterizing the active carbon produced by steam and carbon dioxide as a heavy oil hydrocracking catalyst support Fukuyama H, Terai S |
389 - 394 |
Hydro-treatment of a direct coal liquefaction residue and its components Li J, Yang JL, Liu ZY |
395 - 404 |
The usage of high metal feedstock for the determination of metal capacity of ARDS catalyst system by accelerated aging tests Marafi A, Almari M, Stanislaus A |
405 - 410 |
Study of accelerated deactivation of hydrotreating catalysts by vanadium impregnation method Maity SK, Ancheyta J, Alonso F, Vazquez JA |
411 - 420 |
Heavy crude oil hydroprocessing: A zeolite-based CoMo catalyst and its spent catalyst characterization Rana MS, Ancheyta J, Maity SK, Rayo P |
421 - 428 |
Preparation of heavy oil hydrotreating catalyst from spent residue hydroprocessing catalysts Marafi M, Stanislaus A |
429 - 438 |
Studies on the evolution of asphaltene structure during hydroconversion of petroleum residues Gauthier T, Danial-Fortain P, Merdrignac I, Guibard I, Quoineaud AA |
439 - 445 |
Hydroprocessing peculiarities of Fischer-Tropsch syncrude de Klerk A |
446 - 454 |
Kinetic modeling of the hydrotreatment of light cycle oil and heavy gas oil using the structural contributions approach Froment GF, Castaneda-Lopez LC, Marin-Rosas C |
455 - 461 |
Single-event-lumped-parameter hybrid (SELPH) model for non-ideal hydrocracking of n-octane Chavarria-Herrnandez JC, Ramfrez J, Baltanas MA |
462 - 470 |
Modelling and simulation of a gas-solids dispersion flow in a high-flux circulating fluidized bed (HFCFB) riser Bastos JCSC, Rosa LM, Mori M, Marini F, Maitignoni WP |
471 - 485 |
Hydrogenation of naphthalene on NiMo- Ni- and Ru/Al2O3 catalysts: Langmuir-Hinshelwood kinetic modelling Monteiro-Gezork ACA, Natividad R, Winterbottom JM |
486 - 491 |
Novel initiators for the synthesis of propylene oxide oligomers by anionic ring opening polymerization Cendejas G, Arreguin F, Flores C, Villalobos I, Flores E, Vazquez F |
492 - 500 |
Low-emission diesel production by upgrading LCO plus SR diesel fractions Tailleur RG |
501 - 508 |
Role of pore size analysis in development of zeolite reforming catalyst Kumar M, Saxena AK, Negi BS, Viswanadham N |
509 - 518 |
Sensitivity analysis of a light gas oil deep hydrodesulfurization process via catalytic distillation Rosales-Quintero A, Vargas-Villamil FD, Arce-Medina E |
519 - 526 |
Evaluation of the hydrodynamics of high-pressure ebullated beds based on dimensional similitude Sanchez JL, Ruiz RS, Alonso F, Ancheyta J |
527 - 536 |
Conversion of propylene into cyclohexane on PtGaZr/SiO2 catalyst Tailleur RG, Platin JB |