Energy Efficient Process for Concentrating and Recovering Lithium from a Lithium Containing Brine

Patent metadata

Field	Value
Publication number	US-2022364202-A1
Application number	US-202017762446-A
Country	US
Kind code	A1
Filing date	Aug 31, 2020
Priority date	Sep 25, 2019
Publication date	Nov 17, 2022
Grant date	—

Abstract

A system and process for concentrating a lithium stream is disclosed. The lithium stream is directed to a reverse osmosis unit which produces a concentrate containing lithium compounds. The RO concentrate is directed through two pressure retarded osmosis (PRO) modules connected in series. The two PRO modules further concentrate the RO concentrate and at the same time yield a diluted brine that is effective to drive an energy recovery device. The RO concentrate leaving the PRO modules is directed to an osmotically assisted reverse osmosis (OARO) module which also further concentrates the RO concentrate.

First claim

1 - 4 . (canceled)

5 . A method of purifying and concentrating lithium in a lithium containing stream comprising:
a. directing the lithium containing stream to a reverse osmosis (RO) unit and concentrating the lithium containing stream by producing a permeate and an RO concentrate containing lithium; b. further concentrating the RO concentrate by:
(i) directing the RO concentrate into and through a low pressure side of at least two pressure retarded osmosis (PRO) modules with each containing a lithium selective membrane;
(ii) pressurizing two brine streams each having a dissolved solids concentration greater than the RO concentrate and directing each of the two brine streams into and through a high pressure side of a respective PRO module;
(iii) utilizing the osmotic strength of the brine streams to force water across the lithium selective membranes of the PRO modules, further concentrating the RO concentrate and diluting the brine streams;
c. after further concentrating the RO concentrate in the two PRO modules:
i. pressurizing the RO concentrate and directing the RO concentrate into and through a high pressure side of an osmotically assisted reverse osmosis (OARO) module having a lithium selective membrane and producing a product stream containing lithium;
ii. recycling at least a portion of the product stream into and through a low pressure side of the OARO module to produce an OARO dilute;
iii. concentrating the RO concentrate and diluting the product stream passing through the OARO module as water associated with the RO concentrate passes from the high pressure side of the OARO module through the lithium selective membrane into the low pressure side of the OARO; and
e. recycling the OARO dilute to at least one of the PRO modules.

6 . The method of claim 5 further including utilizing the diluted brine streams to drive a hydro-turbine or a pressure exchanger.

7 . The method of claim 5 wherein the brine streams directed through the high pressure side of the two PRO modules originates as an effluent from a continuous ion exchange unit employed to extract lithium from a lithium source.

8 . The method of claim 5 further including:
directing a lithium source stream over lithium selective adsorption media and extracting lithium from the lithium source stream onto the media;
desorbing the lithium by directing an eluent over the media to yield an eluate containing lithium; and
wherein the eluate constitutes the lithium containing stream that is directed to the RO unit.

9 . The method of claim 5 including utilizing the diluted brine streams to produce electricity or energy.

10 . A method of concentrating a lithium-containing stream comprising:
directing the lithium-containing stream to a reverse osmosis (RO) unit and concentrating the lithium-containing stream to produce a permeate and an RO concentrate containing lithium; further concentrating the RO concentrate by directing the RO concentrate into and through a low pressure side of a pressure retarded osmosis (PRO) module containing a lithium selective membrane; pressurizing a brine stream having a dissolved solids concentration greater than the dissolved solids concentration of the RO concentrate passing through the low pressure side of the PRO module and directing the brine stream into and through a high pressure side of the PRO module; utilizing the osmotic strength of the brine stream to force water from the RO concentrate across the lithium selective membrane of the PRO module so as to further concentrate the RO concentrate and in the process diluting the brine stream; after further concentrating the RO concentrate in the PRO module, pressurizing the RO concentrate and directing the RO concentrate into and through a high pressure side of an osmotically assisted reverse osmosis (OARO) module having a lithium selective membrane and producing a product stream containing lithium; recycling at least a portion of the product stream into and through a low pressure side of the OARO module to produce an OARO dilute; and further concentrating the RO concentrate and diluting the product stream passing through the OARO module as water associated with the RO concentrate passes from the high pressure side of the OARO module through the lithium selective membrane into the low pressure side of the OARO.

11 . The method of claim 10 including recycling at least a portion of the OARO dilute to the PRO module.

12 . The method of claim 10 wherein the brine stream directed through the high pressure side of the PRO module originates as an effluent from an ion exchange unit employed to extract lithium from a lithium source.

13 . The method of claim 10 further including:
directing a lithium source stream over a lithium selective adsorption media and extracting lithium from the lithium source stream onto the media;
desorbing the lithium from the media by directing an eluent over the media to yield an eluate containing lithium; and
wherein the eluate constitutes the lithium-containing stream that is directed to the RO unit.

14 . The method of claim 13 wherein the lithium is extracted from the lithium source stream in a lithium capture unit which produces the brine stream that is directed through the high pressure side of the PRO module.

15 . The method of claim 10 wherein there is provided two PRO modules connected in series and the method includes directing the RO concentrate through the low pressure side of each of the PRO modules and wherein there is provided two brine streams with each brine stream being directed through the high pressure side of one of the PRO modules.

16 . The method of claim 10 including flowing the RO concentrate and brine in counterflow directions through the PRO module.

17 . The method of claim 10 wherein the brine stream passing through the high pressure side of the PRO module is diluted and wherein the diluted brine stream leaving the PRO module is utilized to drive an energy recovery device.

Assignees

• Veolia Water Solutions & Tech

Inventors

• Blohm Kurt
• Leparc Jérôme
• Lemaitre Isabelle

Classifications

• C22B3/22

  by physical processes, e.g. by filtration, by magnetic means {, or by thermal decomposition} (treatment or purification of solutions by liquid-liquid extraction C22B3/26) · CPC title

• C22B9/02

  Refining by liquating, filtering, centrifuging, distilling, or supersonic wave action {including acoustic waves; (C22B9/003, C22B9/006, C22B9/05, C22B9/22 take precedence)} · CPC title

• B01D61/58

  Multistep processes · CPC title

• B01D2313/246

  Energy recovery means · CPC title

• B01D2311/08

  Specific process operations in the concentrate stream · CPC title