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:
May. 18, 2010

Filed:

Jun. 27, 2006
Applicants:

Sun Choi, Daejeon, KR;

Yong Seung Kim, Daejeon, KR;

Deuk Soo Park, Gyeonggi-do, KR;

Suk Joon Kim, Daejeon, KR;

IL MO Yang, Seoul, KR;

Hee Young Kim, Daejeon, KR;

Yong Ki Park, Daejeon, KR;

Chul Wee Lee, Daejeon, KR;

Won Choon Choi, Daejeon, KR;

Kwang an Ko, Gwangju, KR;

NA Young Kang, Chungcheongnam-do, KR;

Inventors:

Sun Choi, Daejeon, KR;

Yong Seung Kim, Daejeon, KR;

Deuk Soo Park, Gyeonggi-do, KR;

Suk Joon Kim, Daejeon, KR;

Il Mo Yang, Seoul, KR;

Hee Young Kim, Daejeon, KR;

Yong Ki Park, Daejeon, KR;

Chul Wee Lee, Daejeon, KR;

Won Choon Choi, Daejeon, KR;

Kwang An Ko, Gwangju, KR;

Na Young Kang, Chungcheongnam-do, KR;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C07C 4/02 (2006.01); C10G 11/02 (2006.01); B01J 29/06 (2006.01); B01J 27/182 (2006.01);
U.S. Cl.
CPC ...
Abstract

Disclosed is a process for producing light olefins from hydrocarbon feedstock. The process is characterized in that a porous molecular sieve catalyst consisting of a product obtained by evaporating water from a raw material mixture comprising a molecular sieve with a framework of Si—OH—Al— groups, a water-insoluble metal salt, and a phosphate compound, is used to produce light olefins, particularly ethylene and propylene, from hydrocarbon, while maintaining excellent selectivity to light olefins. According to the process, by the use of a specific catalyst with hydrothermal stability, light olefins can be selectively produced in high yield with high selectivity from hydrocarbon feedstock, particularly full-range naphtha. In particular, the process can maintain higher cracking activity than the reaction temperature required in the prior thermal cracking process for the production of light olefins, and thus, can produce light olefins with high selectivity and conversion from hydrocarbon feedstock.


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