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:
Jan. 05, 2021

Filed:

Dec. 08, 2016
Applicant:

Usui Co., Ltd., Shizuoka, JP;

Inventors:

Tetsunobu Suzuki, Shizuoka, JP;

Hidetaka Ito, Shizuoka, JP;

Yoshiyuki Serizawa, Shizuoka, JP;

Assignee:

USUI CO., LTD., Shizuoka, JP;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
B01D 45/12 (2006.01); F02M 35/10 (2006.01); F02M 26/50 (2016.01); F02M 26/35 (2016.01); B01D 45/16 (2006.01); B04C 3/02 (2006.01); B04C 3/06 (2006.01); B04C 3/00 (2006.01); F02M 26/05 (2016.01); F02M 26/22 (2016.01); F02M 26/06 (2016.01);
U.S. Cl.
CPC ...
B01D 45/12 (2013.01); B01D 45/16 (2013.01); B04C 3/02 (2013.01); B04C 3/06 (2013.01); F02M 26/35 (2016.02); F02M 26/50 (2016.02); F02M 35/10 (2013.01); B04C 2003/006 (2013.01); F02M 26/05 (2016.02); F02M 26/06 (2016.02); F02M 26/22 (2016.02); Y02T 10/12 (2013.01);
Abstract

A swirling flow generator for gas-liquid separation includes a swirling flow generating ribbon for swirling a gas-liquid two-phase fluid flowing through a pipe to guide a liquid toward an inner surface of the pipe by centrifugal force. A terminal end of the swirling flow generating ribbon where the gas-liquid two-phase fluid is to flow out includes a first terminal edge and a second terminal edge. The first and second terminal edges connect a first terminal end point, a second terminal end point, and a middle terminal end point. The first terminal end point is in a first of radially outward ends and the second terminal end point is in a second of the radially outward ends. The middle terminal end point is closer to a side where the gas-liquid two-phase fluid is to flow in than the first and second terminal end points and is on an axial line.


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