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:
May. 14, 2019

Filed:

Nov. 20, 2017
Applicant:

Beijing Huashi United Energy Technology and Development Co., Ltd, Beijing, CN;

Inventors:

Ke Lin, Beijing, CN;

Lin Li, Beijing, CN;

Lixin Guo, Beijing, CN;

Yongjun Cui, Beijing, CN;

Lilong Jiang, Beijing, CN;

Attorneys:
Primary Examiner:
Int. Cl.
CPC ...
C10G 1/06 (2006.01);
U.S. Cl.
CPC ...
C10G 1/065 (2013.01); C10G 2300/1014 (2013.01); C10G 2300/44 (2013.01); Y02P 30/20 (2015.11);
Abstract

The present invention relates to the field of biological energy, in particular to a biomass liquefaction process and fuel oil and chemical raw materials prepared by the same. The biomass liquefaction process comprises the following steps: preparing a slurry comprising a first catalyst and a biomass; performing a first hydrogenation reaction by introducing hydrogen to the slurry to obtain a first stage hydrogenation product; performing a second hydrogenation reaction by adding a second catalyst and introducing hydrogen into the first stage hydrogenation product to obtain a second stage hydrogenation product; and subjecting the second stage hydrogenation product to separation operation to obtain a fuel oil and chemical raw material; wherein the first hydrogenation reaction is controlled to have a reaction pressure of 13-25 MPa and a reaction temperature of 200-350° C., and the second hydrogenation reaction is controlled to have a reaction pressure of 13-25 MPa and a reaction temperature of 380-480° C. The present invention provides a biomass liquefaction process with high reaction efficiency and high liquid yield without coke generation.


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