Hydrocracking of Maya crude oil in a slurry-phase batch reactor. II. Effect of catalyst load

Hugo Ortiz-Moreno; Jorge Ramírez; Felipe Sanchez-Minero; Rogelio Cuevas; Jorge Ancheyta

doi:10.1016/j.fuel.2014.03.050

Hydrocracking of Maya crude oil in a slurry-phase batch reactor. II. Effect of catalyst load

Hugo Ortiz-Moreno, Jorge Ramírez, Felipe Sanchez-Minero, Rogelio Cuevas, Jorge Ancheyta

Producción científica: Contribución a una revista › Artículo › revisión exhaustiva

60 Citas (Scopus)

Resumen

The effect of the catalyst load in slurry hydrocracking of heavy Maya crude oil was investigated at mild conditions (390 °C and 1400 H₂ psi).The catalyst load and operating time were varied in the intervals 0-1000 ppm Mo and 0-11 h respectively. The results allowed to establish the transformation routes of the different fractions under thermal or catalytic conditions. Under thermal conditions, the contributors to gas formation were found to be: Asphaltenes.

Idioma original	Inglés
Páginas (desde-hasta)	263-272
Número de páginas	10
Publicación	Fuel
Volumen	130
DOI	https://doi.org/10.1016/j.fuel.2014.03.050
Estado	Publicada - 15 ago. 2014
Publicado de forma externa	Sí

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title = "Hydrocracking of Maya crude oil in a slurry-phase batch reactor. II. Effect of catalyst load",

abstract = "The effect of the catalyst load in slurry hydrocracking of heavy Maya crude oil was investigated at mild conditions (390 °C and 1400 H2 psi).The catalyst load and operating time were varied in the intervals 0-1000 ppm Mo and 0-11 h respectively. The results allowed to establish the transformation routes of the different fractions under thermal or catalytic conditions. Under thermal conditions, the contributors to gas formation were found to be: Asphaltenes.",

keywords = "Asphaltene, Desulfurization, Heavy oil, Slurry hydrocracking, Vacuum residue",

author = "Hugo Ortiz-Moreno and Jorge Ram{\'i}rez and Felipe Sanchez-Minero and Rogelio Cuevas and Jorge Ancheyta",

note = "Funding Information: Hugo Ortiz-Moreno acknowledges PhD Grant from CONACyT, M{\'e}xico. We thank Ivan Puente-Lee for the TEM and microanalysis work and Ciro Eliseo M{\'a}rquez Herrera for Plasma spectroscopy work.",

year = "2014",

month = aug,

day = "15",

doi = "10.1016/j.fuel.2014.03.050",

language = "Ingl{\'e}s",

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pages = "263--272",

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T1 - Hydrocracking of Maya crude oil in a slurry-phase batch reactor. II. Effect of catalyst load

AU - Ortiz-Moreno, Hugo

AU - Ramírez, Jorge

AU - Sanchez-Minero, Felipe

AU - Cuevas, Rogelio

AU - Ancheyta, Jorge

N1 - Funding Information: Hugo Ortiz-Moreno acknowledges PhD Grant from CONACyT, México. We thank Ivan Puente-Lee for the TEM and microanalysis work and Ciro Eliseo Márquez Herrera for Plasma spectroscopy work.

PY - 2014/8/15

Y1 - 2014/8/15

N2 - The effect of the catalyst load in slurry hydrocracking of heavy Maya crude oil was investigated at mild conditions (390 °C and 1400 H2 psi).The catalyst load and operating time were varied in the intervals 0-1000 ppm Mo and 0-11 h respectively. The results allowed to establish the transformation routes of the different fractions under thermal or catalytic conditions. Under thermal conditions, the contributors to gas formation were found to be: Asphaltenes.

AB - The effect of the catalyst load in slurry hydrocracking of heavy Maya crude oil was investigated at mild conditions (390 °C and 1400 H2 psi).The catalyst load and operating time were varied in the intervals 0-1000 ppm Mo and 0-11 h respectively. The results allowed to establish the transformation routes of the different fractions under thermal or catalytic conditions. Under thermal conditions, the contributors to gas formation were found to be: Asphaltenes.

KW - Asphaltene

KW - Desulfurization

KW - Heavy oil

KW - Slurry hydrocracking

KW - Vacuum residue

UR - http://www.scopus.com/inward/record.url?scp=84900464924&partnerID=8YFLogxK

U2 - 10.1016/j.fuel.2014.03.050

DO - 10.1016/j.fuel.2014.03.050

M3 - Artículo

SN - 0016-2361

VL - 130

SP - 263

EP - 272

JO - Fuel

JF - Fuel

ER -

Hydrocracking of Maya crude oil in a slurry-phase batch reactor. II. Effect of catalyst load

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