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:
Feb. 07, 2023

Filed:

Oct. 26, 2018
Applicants:

China Petroleum & Chemical Corporation, Beijing, CN;

Research Institute of Petroleum Processing, Sinopec, Beijing, CN;

Inventors:

Yunfei Bi, Beijing, CN;

Guofu Xia, Beijing, CN;

Mingfeng Li, Beijing, CN;

Qinghe Yang, Beijing, CN;

Weiguo Huang, Beijing, CN;

Qingzhou Guo, Beijing, CN;

Wenxiu Fang, Beijing, CN;

Luqiang Wang, Beijing, CN;

Hongbao Li, Beijing, CN;

Honghui Li, Beijing, CN;

Jie Gao, Beijing, CN;

Attorneys:
Primary Examiner:
Int. Cl.
CPC ...
B01J 29/04 (2006.01); C01B 39/04 (2006.01); B01J 29/40 (2006.01); B01J 29/70 (2006.01); B01J 29/72 (2006.01); B01J 29/74 (2006.01); C01B 39/46 (2006.01); C01B 39/12 (2006.01); B01J 6/00 (2006.01); C01B 39/10 (2006.01); C01B 39/54 (2006.01); C01B 39/06 (2006.01); B01J 37/03 (2006.01); B01J 37/02 (2006.01); B01J 37/10 (2006.01); B01J 35/10 (2006.01); B01J 37/00 (2006.01); B01J 35/00 (2006.01); B01J 29/76 (2006.01); B01J 29/85 (2006.01); B01J 29/86 (2006.01); B01J 29/87 (2006.01); B01J 29/88 (2006.01); C07C 5/22 (2006.01); C10G 45/64 (2006.01); C10G 45/60 (2006.01); C10G 45/62 (2006.01);
U.S. Cl.
CPC ...
C01B 39/04 (2013.01); B01J 6/001 (2013.01); B01J 29/041 (2013.01); B01J 29/042 (2013.01); B01J 29/043 (2013.01); B01J 29/044 (2013.01); B01J 29/405 (2013.01); B01J 29/7007 (2013.01); B01J 29/7042 (2013.01); B01J 29/7057 (2013.01); B01J 29/7084 (2013.01); B01J 29/7092 (2013.01); B01J 29/7096 (2013.01); B01J 29/7215 (2013.01); B01J 29/7261 (2013.01); B01J 29/7269 (2013.01); B01J 29/7284 (2013.01); B01J 29/7292 (2013.01); B01J 29/7461 (2013.01); B01J 29/7615 (2013.01); B01J 29/7684 (2013.01); B01J 29/85 (2013.01); B01J 29/86 (2013.01); B01J 29/87 (2013.01); B01J 29/88 (2013.01); B01J 35/002 (2013.01); B01J 35/109 (2013.01); B01J 35/1014 (2013.01); B01J 35/1019 (2013.01); B01J 35/1057 (2013.01); B01J 35/1061 (2013.01); B01J 35/1066 (2013.01); B01J 37/0018 (2013.01); B01J 37/0203 (2013.01); B01J 37/031 (2013.01); B01J 37/036 (2013.01); B01J 37/10 (2013.01); C01B 39/065 (2013.01); C01B 39/10 (2013.01); C01B 39/12 (2013.01); C01B 39/46 (2013.01); C01B 39/54 (2013.01); C07C 5/22 (2013.01); C07C 5/222 (2013.01); C07C 5/2206 (2013.01); C07C 5/2213 (2013.01); C10G 45/60 (2013.01); C10G 45/62 (2013.01); C10G 45/64 (2013.01); B01J 2229/20 (2013.01); B01J 2229/40 (2013.01); B01J 2229/42 (2013.01);
Abstract

A molecular sieve has a silica/alumina molar ratio of 100-300, and has a mesopore structure. One closed hysteresis loop appears in the range of P/P=0.4-0.99 in the low temperature nitrogen gas adsorption-desorption curve, and the starting location of the closed hysteresis loop is in the range of P/P=0.4-0.7. The catalyst formed from the molecular sieve as a solid acid not only has a good capacity of isomerization to reduce the freezing point, but also can produce a high yield of the product with a lower pour point. The process for preparing the catalyst involves steps including crystallization, filtration, calcination, and hydrothermal treatment.


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