Instituto Mexicano Del Petroleo

Maria Del Rosario Socorro Luna Ramirez

Blanca Lucia Medellin Rivera

Jorge Arturo Aburto Anell

Edith Meneses Ruiz

Javier Esteban Rodriguez Rodriguez

Rogelio Hernandez Suarez

Roberto Garcia De Leon

Agapito Alberto Neri Gomez

Luis Felipe Ramirez Verduzco

Myriam Adela Amezcua Allieri

Guadalupe Hayde Moreno Vasquez

Leonardo Diaz Garcia

Gonzalo Hernandez Tapia

Lucia Medellin Rivera

The present invention deals with a process for catalytic cracking of hydrocarbons comprising vacuum gas oil, hydrotreated vacuum gas oil, unconventional light crude oil, preferably unconventional light crude oil type shale/tight oil and its blends with conventional vacuum gas oil, in order to generate products of major commercial value in the field of fuels, getting improved gasoline and coke yield, as well as the procedure for the preparation of a catalyst with essential physical properties of density and particle size to uphold it in a fluidized bed under the operation conditions in the catalyst evaluation unit at micro level, wherein the catalyst particles achieve a catalytic performance similar to fluidized microspheres in a reactor, without appreciable generation of fine particles.

Process and zeolitic catalyst for the catalytic cracking of unconventional light crude oil type shale/tight oil and its blends with vacuum gas oil

The present disclosure relates to a process for the hydrodeoxygenation of vegetable oils or animal fats to produce green diesel, which comprises contacting the vegetable oil or animal fat with a Nickel-Molybdenum or Cobalt-Molybdenum catalyst supported on alumina-titania or titania, respectively; in a fixed bed reactor in the presence of hydrogen. The process involves hydrocracking, hydrogenation, decarboxylation, decarbonylation, carried out in a fixed bed reactor at temperature of about 270&#xb0; C. to about 360&#xb0; C., pressure of about 40 kg/cmto about 60 kg/cm, liquid hourly space velocity (LHSV) between about 0.8 hto about 3.0 h, and H/oil ratio of about 2,700 ft/bbl to about 7,000 ft/bbl, that allows to obtain a conversion up to 99% and up to 92.7% yield on green diesel.

Hydrodeoxigenation process of vegetable oils for obtaining green diesel

Growing community of inventors

Mexico City, Mexico

Maria Del Rosario Socorro Luna Ramirez