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:
Sep. 29, 2020

Filed:

Mar. 05, 2019
Applicant:

China University of Petroleum (East China), Qingdao, CN;

Inventors:

Yingyun Qiao, Qingdao, CN;

Yuanyu Tian, Qingdao, CN;

Youqing Wu, Shanghai, CN;

Huawei Zhang, Qingdao, CN;

Peijie Zong, Qingdao, CN;

Jie Li, Qingdao, CN;

Xue Ming, Qingdao, CN;

Yuan Jiang, Qingdao, CN;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C10J 3/54 (2006.01); C10J 3/56 (2006.01); C10J 3/84 (2006.01); C10J 3/66 (2006.01);
U.S. Cl.
CPC ...
C10J 3/54 (2013.01); C10J 3/56 (2013.01); C10J 3/66 (2013.01); C10J 3/84 (2013.01); C10J 2200/36 (2013.01); C10J 2300/0916 (2013.01); C10J 2300/0923 (2013.01); C10J 2300/0986 (2013.01); C10J 2300/0993 (2013.01); C10J 2300/1606 (2013.01); C10J 2300/1662 (2013.01);
Abstract

The invention provides a method of biomass grading pyrolysis gasification in a circulating fluidized bed comprising: feeding biomass into the lower-middle part of a carrying fluidized bed, mixing with high temperature synthesis gas and heat carrier from a turbulent fluidized bed, heating the biomass to carry out a pyrolysis reaction, and carrying the pyrolysis product upward; subjecting the cracked oil and gas to a gaseous phase catalytic cracking in an upper-middle part of the carrying fluidized bed, cracking the tar into methane, ethane and the like; subjecting the heat carrier, semi-coke and fuel gas after the reaction to the multi-stage of gas-solid separation, a large particle carrier and semi-coke following a first-level separation are used as the fuel gas cracking catalyst and the filter material for filtering and removing dust, and enter into a moving bed filter to separate out an ultra-fine ash and subsequently return to the turbulent fluidized bed so as to perform gasification reaction, the ultra-fine ash is delivered to the outside as a silicon-potash fertilizer product; the medium and small particle carrier and semi-coke separated from a second-level separation are directly recycled to the turbulent fluidized bed, the fine particles separated from a third-level separation is discharged to the outside as a silicon-potash fertilizer product, the moving bed filter further catalytically cracks a small amount of tar in the fuel gas into methane and ethane and removes the ultra-fine ash simultaneously, the purified fuel gas is delivered to the outside as a product.


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