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Inventor:
Vargas; Jose M.
Address:
Baton Rouge, LA
No. of patents:
6
Patents:












Patent Number Title Of Patent Date Issued
5663388 Process for converting aldehydes to acids September 2, 1997
A process for forming acids from aldehydes which comprises reacting an oxo aldehyde with water in the presence of an acid-forming catalyst and in the absence of hydrogen, and at a pressure of about 0.1 to 6.99 MPa and a temperature of about 93.degree. to 205.degree. C., thereby convertin
5399793 Hydrogenation catalyst for oxo alcohol process March 21, 1995
The hydrogenation steps and hydrofinishing steps of the cobalt catalyst oxo process for preparation of the alcohols by the hydroformylation of olefin are carried out using a catalyst containing Ni/Mo on alumina or silica alumina prepared by depositing an organic acid solution of Ni and M
5382715 Hydrogenation catalyst with low phosphorous content for oxo alcohol process January 17, 1995
The hydrogenation steps and hydrofinishing steps of the cobalt catalyst oxo process for preparation of the alcohols by the hydroformylation of olefin are carried out using a nickel-molybdenum catalyst on an alumina or silica alumina support which has a phosphorous content of O.1 wt. % to
5306848 Hydrogenation catalyst for oxo alcohol process April 26, 1994
The hydrogenation steps and hydrofinishing steps of the cobalt catalyst oxo process for the preparation of alcohols by the hydroformylation of olefin are carried out using a trimetallic catalyst composed of metal oxides, particularly nickel oxide, molybdenum oxide and cobalt oxide suppor
5059718 Oxo process for increasing yield of oxo alcohol October 22, 1991
Improved oxo process for preparing higher alcohols by hydrolyzing prior to hydrogenation a demetalled hydroformylation reaction product in the presence of an alumina catalyst having a surface area between 40 to about 60 m.sup.2 /g.
4888131 Synthesis gas preparation and catalyst therefor December 19, 1989
Synthesis gas is produced by the reaction of light hydrocarbons, primarily methane, in a fluid bed reaction zone of attrition resistant nickel on alpha-alumina catalyst, with steam and oxygen and the conversion level is preserved by limiting the loss of nickel from the reaction and there










 
 
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