Instituto Mexicano Del Petroleo

Alicia Del Rayo Jaramillo Jacob

Federico Jesus Jimenez Cruz

Maria Del Carmen Martinez Guerrero

Florentino Rafael Murrieta Guevara

Javier Esteban Rodriguez Rodriguez

Luis Carlos Castaneda Lopez

Rogelio Hernandez Suarez

Celia Marin Rosas

Maria Teresa Gómez Pérez

María Del Rosario Socorro Luna Ramírez

Gonzalo Hernández Tapia

Blanca Lucía Medellín Rivera

Maria Teresa Cortez De La Paz

Leonardo Díaz Garcia

MARÍA Del Carmen MARTÍNEZ Guerrero

Rogelio HERNÁNDEZ SUÁREZ

Javier Esteban RODRÍGUEZ RODRÍGUEZ

Luis Carlos CASTAÑEDA LÓPEZ

Federico JESÚS JIMÉNEZ Cruz

Celia MARÍN Rosas

The present invention is an in-situ cleaning procedure for the recovery of catalytic activity of a based alumina HDS catalyst, molybdenum, nickel coated coke and contaminants and it has an HDS activity seriously diminished. The catalyst under study had between 13 and 18 wt % total carbon. Reformate, half the total volume, industrial toluene=35 volume % and Iso-propylic alcohol, 15 volume %, in order to reactivate a deactivated catalyst, a solvent mixture with the following volumetric ratio is prepared. Or it can also be used only reformate (100% volume). The solvent mixture is passed using a LHSV of 2 hr&#x2212;1 for 72 hours at 50&#xb0; C. or also using a recirculating three 24-hour cycles at 50&#xb0; C. Option lasts 24 hours pure reformate LHSV=2h&#x2212;1 to 50&#xb0; C. The washed catalyst is fed back to the load reaction conditions maintained for 36 hours at 340&#xb0; C., to initiate HDS activity balances. During this treatment oxides of molybdenum and nickel in the active phase are re-sulfided by increasing the HDS activity. The In-Situ Cleaning procedure to reactivate deactivated hydrotreating catalysts used to partially remove the carbon and increase the active phase of molybdenum di-sulphide, and also retrieve specific area, and hydrogenation sites that promote higher hydrodesulfurization activity of gasoil after this treatment.

In-situ washing procedure to recover the catalytic activity of a deactivated hydrodesulfurization catalyst

The present invention relates to the production of biodiesel and alkyl esters by the transesterification of triglyceride esters, with alcohols in heterogeneous phase in the presence of heterogeneous catalysts, with yields higher than 80%, at a temperature from 0 to 300&#xb0; C., residence time from 20 minutes to 20 h, space velocity of 0.1 to 10 h, pressure of 25-100 kg/cm(24.5-98.07 bar), methanol/oil molar ratio of 10 to 40 and catalyst concentration of 0.001 to 20 weight % based on tri-, di- or monoglyceride. The method produces biodiesel and alkyl esters by transesterification of tri-, di- or mono-glycerides, from palm, jatropha, castor, soybean and sunflower oils, wherein the alcohoxyls RO, RO and RO of the glycerides are Cto Cand a C-Calcohol, such as methanol, in an alcohol:oil ratio from 3:1 to 50:1. The transesterification reaction produces biodiesel while avoiding loss of catalyst, contaminating liquid effluents and eliminating undesirable hydrolysis of triglycerides, diglycerides and monoglycerides into free fatty acids and saponification that generate soaps.

Use of heterogeneous acid catalysts based on mixed metal salts to produce biodiesel

The present invention relates to heterogeneous acid catalysts comprising or consisting of mixed metal salts, of lithium and aluminum phosphates and sulfates, and combinations with metallic cations, such as magnesium, titanium, zinc, zirconium and gallium, to provide adequate Lewis acidity; organic or inorganic porosity promoters, such as polysaccharides; and agglomerates, such as clays, kaolin and metal oxides of the type MO, where; M=Al, Mg, Sr, Zr or Ti, and other metals of groups IA, IIA and IVB, x=1 or 2 and y=2 or 3, for the formation of particles. A process is disclosed for obtaining from the catalyst by the hydrolysis of aluminum lithium hydride with water and oxygenated solvent, such as an ether. The catalysts are used in batch reactor and continuous flow systems in reactions that require moderate Lewis acidity, such as refining, petrochemical and general chemistry, including the transesterification of glycerides to produce alkyl esters.

Process for obtaining heterogeneous acid catalysts based on mixed metal salts and use thereof

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Mexico City, Mexico

Alicia Del Rayo Jaramillo Jacob