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. 22, 2020

Filed:

Mar. 27, 2018
Applicant:

Cameron Solutions, Inc., Houston, TX (US);

Inventors:

Marcus D. Sprenkel, Houston, TX (US);

Gary W. Sams, Spring, TX (US);

S. Pavankumar B. Mandewalkar, Houston, TX (US);

Luis Eduardo Caires Fernandez, Cypress, TX (US);

Assignee:

CAMERON SOLUTIONS, INC., Houston, TX (US);

Attorneys:
Primary Examiner:
Int. Cl.
CPC ...
C10G 32/02 (2006.01); C10G 53/02 (2006.01); B01D 1/00 (2006.01); B01D 1/30 (2006.01); B01D 17/02 (2006.01); B01D 19/00 (2006.01); B01D 21/26 (2006.01); B03C 11/00 (2006.01); C10G 7/00 (2006.01); C10G 31/10 (2006.01); C10G 33/02 (2006.01); C10G 33/06 (2006.01);
U.S. Cl.
CPC ...
C10G 32/02 (2013.01); B01D 1/0094 (2013.01); B01D 1/305 (2013.01); B01D 17/02 (2013.01); B01D 17/0217 (2013.01); B01D 19/0036 (2013.01); B01D 21/267 (2013.01); B03C 11/00 (2013.01); C10G 7/00 (2013.01); C10G 31/10 (2013.01); C10G 33/02 (2013.01); C10G 33/06 (2013.01); C10G 53/02 (2013.01); B03C 2201/02 (2013.01); C10G 2300/208 (2013.01);
Abstract

A system and method for dehydrating crude oil on a floating production storage and offloading installation include a separator vessel to receive an incoming produced water stream, followed by a flash vessel, a treatment block, a crude oil storage tank, and an electrostatic treater. The treatment block includes a low pressure degasser followed by a compact electrostatic separator pre-treater or a compact electrostatic separator pre-treater followed by a low pressure degasser. The flash vessel and/or the low pressure degasser may employ an inlet cyclonic distributor and demisting cyclones, while the electrostatic treater may employ DUAL FREQUENCY® technology. The separator vessel may be a single horizontal two-phase separator/degasser or two vertical two-phase separator/degassers that operate in parallel with each receiving approximately 50 percent of the incoming produced water stream. The final outlet stream preferably contains no more than 0.5 BS&W and 285 milligrams per liter salt.


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