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:
Dec. 19, 2017

Filed:

Mar. 27, 2013
Applicants:

Japan Oil, Gas and Metals National Corporation, Tokyo, JP;

Inpex Corporation, Tokyo, JP;

Jx Nippon Oil & Energy Corporation, Tokyo, JP;

Japan Petroleum Exploration Co., Ltd., Tokyo, JP;

Cosmo Oil Co., Ltd., Tokyo, JP;

Nippon Steel & Sumikin Engineering Co., Ltd., Tokyo, JP;

Inventors:

Takuya Niitsuma, Tokyo, JP;

Marie Iwama, Tokyo, JP;

Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C10G 67/00 (2006.01); C10L 1/06 (2006.01); C10L 10/16 (2006.01); C10L 10/14 (2006.01); C10G 65/14 (2006.01); C10L 1/08 (2006.01); C10G 45/58 (2006.01); C10G 47/00 (2006.01); C10G 2/00 (2006.01);
U.S. Cl.
CPC ...
C10G 67/00 (2013.01); C10G 2/30 (2013.01); C10G 45/58 (2013.01); C10G 47/00 (2013.01); C10G 65/14 (2013.01); C10L 1/06 (2013.01); C10L 1/08 (2013.01); C10L 10/14 (2013.01); C10L 10/16 (2013.01); C10G 2300/1022 (2013.01); C10G 2300/4081 (2013.01); C10L 2200/0492 (2013.01); C10L 2270/026 (2013.01); C10L 2290/10 (2013.01);
Abstract

Provided is a hydrotreating step (A) containing a hydroisomerization step (A1) that obtains a hydroisomerized oil (a1) by bringing a FT synthesis oil into contact with a hydroisomerization catalyst and/or a hydrocracking step (A2) that obtains a hydrocracked oil (a2) by bringing it into contact with a hydrocracking catalyst, and a fractionation step (B) that transfers at least a portion of the hydrotreated oil (a) composed of the hydroisomerized oil (a1) and/or the hydrocracked oil (a2) to a fractionator and, at the very least, obtains a middle distillate (b1) with a 5% distillation point of 130 to 170° C. and a 95% distillation point of 240 to 300° C., and a heavy oil (b2) that is heavier than the middle distillate (b1).


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