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:
Jan. 02, 2018

Filed:

Oct. 13, 2015
Applicants:

China Petroleum & Chemical Corporation, Beijing, CN;

Shanghai Research Institute of Petrochemical Technology, Sinopec, Shanghai, CN;

Inventors:

Jun Xu, Shanghai, CN;

Songyuan Gu, Shanghai, CN;

Siqing Zhong, Shanghai, CN;

Yongming Jin, Shanghai, CN;

Zhinan Yu, Shanghai, CN;

Guozhen Qi, Shanghai, CN;

Xiaohong Li, Shanghai, CN;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
B01J 8/24 (2006.01); B01J 8/26 (2006.01); B01J 8/00 (2006.01); C07C 1/20 (2006.01); C10G 11/18 (2006.01);
U.S. Cl.
CPC ...
B01J 8/0015 (2013.01); B01J 8/0055 (2013.01); B01J 8/26 (2013.01); C07C 1/20 (2013.01); C10G 11/182 (2013.01); B01J 2208/00752 (2013.01); B01J 2208/00938 (2013.01); B01J 2208/00991 (2013.01); C07C 2529/40 (2013.01); C07C 2529/85 (2013.01); Y02P 20/52 (2015.11); Y02P 30/42 (2015.11);
Abstract

Device for use in a fluidized bed reactor includes a gas-solid separator communicated with an outlet of the fluidized bed reactor; a vertically arranged damper, a solid outlet of the gas-solid separator communicated with a lower region of the damper, a gas outlet of the gas-solid separator communicated with an upper region of the damper; a fine gas-solid separator, an inlet of the fine gas-solid separator communicated with the upper region of the damper, and a solid outlet of the fine gas-solid separator communicated with the lower region of the damper. Product from the fluidized bed reactor is fed into the preliminary gas-solid separator, most solid catalysts separated and fed into the lower region; the product entraining the rest catalysts is fed into the upper region, and into the fine gas-solid separator, the rest catalysts fed into the lower region; and final product is obtained from the fine gas-solid separator.


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