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:
Oct. 06, 2020

Filed:

Nov. 25, 2015
Applicants:

China Petroleum & Chemical Corporation, Beijing, CN;

Fushun Research Institute of Petroleum and Petrochemicals, Sinopec Corp., Fushun, Liaoning, CN;

Inventors:

Shumei Zhang, Liaoning, CN;

Feng Zhou, Liaoning, CN;

Kai Qiao, Liaoning, CN;

Qingtong Zhai, Liaoning, CN;

Chunmei Wang, Liaoning, CN;

Attorneys:
Primary Examiner:
Int. Cl.
CPC ...
B01J 21/00 (2006.01); B01J 21/12 (2006.01); B01J 37/02 (2006.01); C07C 1/24 (2006.01); C07C 1/20 (2006.01); B01J 35/00 (2006.01); C07C 11/09 (2006.01);
U.S. Cl.
CPC ...
B01J 21/12 (2013.01); B01J 35/00 (2013.01); B01J 35/0006 (2013.01); B01J 37/02 (2013.01); C07C 1/20 (2013.01); C07C 1/24 (2013.01); C07C 11/09 (2013.01);
Abstract

The present invention relates to the field of isobutylene preparation. Disclosed are a catalyst and preparation method thereof, and method for preparing isobutylene by applying the same; the catalyst has a core-shell structure, the core an amorphous silica-alumina particle and/or an aggregate molding thereof, and the shell aluminum oxide comprising silicon and tin; the weight ratio of aluminum oxide comprising silicon and tin to amorphous silica-alumina is 1:60-1:3; in the aluminum oxide comprising silicon and tin, on basis of the weight of aluminum oxide comprising silicon and tin, the content of silicon is 0.5-2 wt %, and of tin is 0.2-1 wt %. The catalyst of the present invention is used to catalyze a mixture of MTBE and TBA to prepare isobutylene, enabling the MTBE cleavage and TBA dehydration reactions to be conducted simultaneously to generate isobutylene, achieving higher conversion rates of TBA and MTBE, and higher selectivity for generating isobutylene.


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