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. 26, 2018

Filed:

Nov. 08, 2015
Applicant:

Wuhan Kaidi Engineering Technology Research Institute Co., Ltd., Wuhan, CN;

Inventors:

Dashan Wang, Wuhan, CN;

Dechen Song, Wuhan, CN;

Qianqian Liu, Wuhan, CN;

Shenke Zheng, Wuhan, CN;

Xiaodong Zhan, Wuhan, CN;

Jiaqi Jin, Wuhan, CN;

Yanfeng Zhang, Wuhan, CN;

Attorneys:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C10G 33/04 (2006.01); C10G 3/00 (2006.01); C10G 11/18 (2006.01); B01D 17/04 (2006.01); B01J 29/08 (2006.01); C10B 53/02 (2006.01); C10L 1/02 (2006.01); B01J 29/40 (2006.01);
U.S. Cl.
CPC ...
C10G 3/49 (2013.01); B01D 17/047 (2013.01); B01J 29/088 (2013.01); B01J 29/405 (2013.01); C10B 53/02 (2013.01); C10G 11/18 (2013.01); C10G 33/04 (2013.01); C10L 1/02 (2013.01); B01J 2229/186 (2013.01); B01J 2229/36 (2013.01); B01J 2229/42 (2013.01); C10G 2300/1011 (2013.01); Y02E 50/14 (2013.01); Y02P 30/20 (2015.11);
Abstract

A method for modifying bio-oil derived from biomass pyrolysis, the method including: 1) adding an inorganic salt and an organic demulsifier to a bio-oil; oscillating or stirring the resulting mixture, and resting the resulting mixture, to yield a lower layer being an aqueous solution and an upper layer being the bio-oil, and collecting the bio-oil; 2) employing a zeolite molecular sieve-loaded clay as a catalyst, and aging the catalyst using pure steam, to yield a modified catalyst; and 3) adding the modified catalyst obtained in 2) to a conventional catalytic cracking reactor, injecting the bio-oil obtained in 1) to the conventional catalytic cracking reactor using a piston pump, and allowing the bio-oil to react under a weight hourly space velocity (WHSV) of between 6 and 15 h, a temperature of between 380 and 700° C., and a pressure between 0.1 and 0.8 megapascal.


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