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:
Jun. 16, 2020

Filed:

Jun. 08, 2016
Applicant:

Petrochina Company Limited, Beijing, CN;

Inventors:

Shoutao Ma, Beijing, CN;

Xiaoqiao Huang, Beijing, CN;

Famin Sun, Beijing, CN;

Qingfeng Ma, Beijing, CN;

Fangming Xie, Beijing, CN;

Yongsheng Duan, Beijing, CN;

Xianjun Wu, Beijing, CN;

Fengxuan Li, Beijing, CN;

Dongmei Ge, Beijing, CN;

Endong Xia, Beijing, CN;

Ruifeng Li, Beijing, CN;

Ronglei Ji, Beijing, CN;

Liying Liu, Beijing, CN;

Lihong Qin, Beijing, CN;

Xiangbin Meng, Beijing, CN;

Chunming Dong, Beijing, CN;

Xuefeng Lu, Beijing, CN;

Rui Wang, Beijing, CN;

Tiegang Xu, Beijing, CN;

Shurong Ni, Beijing, CN;

Assignee:
Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C10G 45/58 (2006.01); C10M 177/00 (2006.01); C10G 67/02 (2006.01); C10L 1/08 (2006.01); C10M 101/02 (2006.01); C10G 45/72 (2006.01); C10G 69/02 (2006.01);
U.S. Cl.
CPC ...
C10G 45/58 (2013.01); C10G 45/72 (2013.01); C10G 67/02 (2013.01); C10G 69/02 (2013.01); C10L 1/08 (2013.01); C10M 101/02 (2013.01); C10M 177/00 (2013.01); C10G 2300/1011 (2013.01); C10G 2300/1055 (2013.01); C10G 2300/1062 (2013.01); C10G 2300/42 (2013.01); C10G 2400/04 (2013.01); C10G 2400/10 (2013.01); C10M 2203/1025 (2013.01); C10N 2220/022 (2013.01); C10N 2230/02 (2013.01);
Abstract

Provided are a liquid-phase hydroisomerization system and a process therefor and use thereof. The system comprises a gas-liquid mixer (), a hydroisomerization reactor () and a fractionating column (). An oil product and hydrogen are mixed as a liquid hydrogen-oil mixture, and are introduced into the hydroisomerization reactor for a hydroisomerization reaction, and after being fractionated, a target product is led out. A supplemental hydrogen-dissolving inner member is provided at least between a group of two adjacent catalyst bed layers in order to supplement hydrogen to the reactants. The process cancels a circulating hydrogen compressor, has a simple process flow, and can be applied to the production of a lubricant base oil by the hydroisomerization of a lubricant raw material or the production of a low freezing point diesel by the hydroisomerization of and the reduction in the freezing point of a diesel raw material.


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