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:
Nov. 04, 2025

Filed:

May. 04, 2023
Applicant:

Schlumberger Technology Corporation, Sugar Land, TX (US);

Inventors:

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

Dominic Vincent Perroni, Sugar Land, TX (US);

Prasanna Nirgudkar, Sugar Land, TX (US);

Florence Binet, Houston, TX (US);

Rod William Shampine, Sugar Land, TX (US);

Assignee:
Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
B01D 11/04 (2006.01); B01D 15/20 (2006.01); B01D 15/36 (2006.01); B01D 61/02 (2006.01); B01D 61/04 (2006.01); B01D 61/44 (2006.01); B01D 61/58 (2006.01); C22B 3/22 (2006.01); C22B 3/24 (2006.01); C22B 26/12 (2006.01); C22C 24/00 (2006.01); C25C 1/02 (2006.01);
U.S. Cl.
CPC ...
B01D 11/0415 (2013.01); B01D 15/203 (2013.01); B01D 15/361 (2013.01); B01D 61/026 (2022.08); B01D 61/04 (2013.01); B01D 61/44 (2013.01); B01D 61/58 (2013.01); C22B 3/22 (2013.01); C22B 3/24 (2013.01); C22B 26/12 (2013.01); C22C 24/00 (2013.01); C25C 1/02 (2013.01); B01D 2311/04 (2013.01); B01D 2315/24 (2022.08); B01D 2317/022 (2013.01); B01D 2317/025 (2013.01);
Abstract

Described herein are methods of recovering lithium from dilute lithium sources. The methods include extracting lithium from an extraction feed using direct lithium extraction in an extraction stage to yield a lithium intermediate, performing one or more concentration operations, each concentration operation concentrating an input stream to yield an output feed, wherein the input stream is obtained from the lithium intermediate and/or the extraction feed is obtained from the output feed. At least one of the concentration operations includes a membrane separation operation having a plurality of reactors in series each having a semi-permeable membrane, such as a counter-flow reverse osmosis operation. Methods may also include generating a low TDS stream as a permeate from any of the one or more concentration operations, wherein the low TDS stream is recycled or used as fresh water.


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