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:
Apr. 02, 2019

Filed:

Nov. 29, 2011
Applicants:

Wei Du, Beijing, CN;

Dehua Liu, Beijing, CN;

Luole Zhu, Beijing, CN;

Inventors:

Wei Du, Beijing, CN;

Dehua Liu, Beijing, CN;

Luole Zhu, Beijing, CN;

Assignee:

Tsinghua University, Beijing, CN;

Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C10G 3/00 (2006.01); C10L 1/02 (2006.01); C11C 3/00 (2006.01); C12P 7/64 (2006.01);
U.S. Cl.
CPC ...
C10G 3/00 (2013.01); C10L 1/026 (2013.01); C11C 3/003 (2013.01); C12P 7/649 (2013.01); C10L 2200/0476 (2013.01); C10L 2290/26 (2013.01); C10L 2290/548 (2013.01); Y02E 50/13 (2013.01); Y02P 30/20 (2015.11);
Abstract

The present invention provides a method for preparing biodiesel, comprising: adding oil and fat, short-chain alcohol, water, and liquid lipase into a single-stage or multi-stage enzyme reactor; then separating the reaction fluid into an enzyme-containing heavy phase and a light phase; recovering and reusing the enzyme in the heavy phase; using the light phase for subsequent conversion by immobilized lipase; flowing the light phase and the short-chain alcohol into single-stage or multi-stage enzyme reactor containing an immobilized lipase; performing online dehydration during the whole reaction process or part of the reaction process. In the method of the invention for preparing biodiesel, no preprocessing is required for the oil and fat feedstock in the earlier stage of catalysis process by liquid lipase, and the conversion ratio from oil and fat to biodiesel can reach more than 90%; in the later stage of catalysis process by immobilized lipase, by introducing an online dehydration during the whole process or part of the reaction process, the yield of biodiesel can exceed 98%, and the acid value of the product can be less than 0.5 mg KOH per gram of oil. The method thus has good economic and environmental benefits.


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