The patent badge is an abbreviated version of the USPTO patent document. The patent badge does contain a link to the full patent document.

The patent badge is an abbreviated version of the USPTO patent document. The patent badge covers the following: Patent number, Date patent was issued, Date patent was filed, Title of the patent, Applicant, Inventor, Assignee, Attorney firm, Primary examiner, Assistant examiner, CPCs, and Abstract. The patent badge does contain a link to the full patent document (in Adobe Acrobat format, aka pdf). To download or print any patent click here.

Date of Patent:
Dec. 02, 2014

Filed:

Jun. 22, 2010
Applicants:

Avelino Corma, Valencia, ES;

Cristina Martinez, Valencia, ES;

Eric J. Doskocil, Oswego, IL (US);

George Yaluris, Park Ridge, IL (US);

Inventors:

Avelino Corma, Valencia, ES;

Cristina Martinez, Valencia, ES;

Eric J. Doskocil, Oswego, IL (US);

George Yaluris, Park Ridge, IL (US);

Assignee:
Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C07C 2/12 (2006.01); B01J 29/70 (2006.01); B01J 29/06 (2006.01); B01J 35/10 (2006.01); C10G 50/00 (2006.01); C10L 1/08 (2006.01);
U.S. Cl.
CPC ...
B01J 29/7042 (2013.01); B01J 29/06 (2013.01); B01J 35/1061 (2013.01); C10G 50/00 (2013.01); C10L 1/08 (2013.01); B01J 2229/16 (2013.01); B01J 2229/22 (2013.01); B01J 2229/38 (2013.01); C10G 2400/04 (2013.01); C10G 2300/4018 (2013.01); C10G 2300/1088 (2013.01); C10G 2300/70 (2013.01);
Abstract

Disclosed is a process for producing a hydrocarbon fraction rich in components boiling in the range typical for diesel fuel comprising contacting a feedstock comprising one or more Cto Calkenes with a modified zeolite catalyst having a one-dimensional micropore structure consisting of channels made from rings containing between 8 and 12 silicon/aluminum atoms at a temperature in the range 100 to 500° C. and pressure in the range 0.1 to 200 bar characterized in that the modified zeolite catalyst is one which has been prepared by treating a corresponding zeolite precursor with an alkaline solution. The alkaline solution used to treat the zeolite precursor can be for example aqueous sodium hydroxide solution. Relative to equivalent untreated zeolites the modified zeolite catalysts described show improved catalyst life and selectivity to hydrocarbons boiling in the range 250 to 350° C.


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