Process For Concentration Of Lithium Containing Solutions

Patent metadata

Field	Value
Publication number	US-2018147532-A1
Application number	US-201515520519-A
Country	US
Kind code	A1
Filing date	Oct 16, 2015
Priority date	Oct 20, 2014
Publication date	May 31, 2018
Grant date	—

Abstract

A forward osmosis process for concentration of lithium-containing salt solutions is described. A difference in osmotic pressure between a lithium-containing salt solution and a second salt solution of higher osmotic pressure is used as a driving force to pass water through a semi-permeable forward osmosis membrane from said lithium-containing salt solution of lower osmotic pressure to the salt solution of higher osmotic pressure. Also, a two-part operation is described wherein reverse osmosis process technology and forward osmosis process technology are used in tandem to concentrate lithium-containing salt solutions and to recover water that can be recycled to the process. The forward osmosis process is conducted without requiring (i) use of superatmospheric pressure or (ii) use of subatmospheric pressure or (iii) use of both such pressures, or (iv) use of one or more additives to assist in causing the flow of water through a forward osmosis membrane.

First claim

1 . A process for increasing the concentration of dissolved lithium salt(s) in a First Solution having a content of at least one dissolved lithium salt(s), which process comprises:
(a) maintaining said First Solution in direct contact with one side of a semi-permeable forward osmosis membrane and (b) maintaining in direct contact with the other side of said membrane, a Second Brine Solution a minimum content of dissolved salt(s) in the range of from about 15 wt % below the saturation point up to the saturation point of the Second Brine Solution, and having an inherent osmotic pressure that is higher than the osmotic pressure of said First Solution during the process, (c) whereby the concentration of dissolved lithium salt(s) in said First Solution is increased by the flux of water from said First Solution through said membrane and into said Second Brine Solution so that the overall concentration of lithium in said First Solution is increased, (d) independently maintain the temperature(s) of said First Solution and said Second Brine Solution in the range of about 5° C. to about 95° C., (e) said process being further characterized in that it is conducted without requiring use of (i) superatmospheric pressure or (ii) subatmospheric pressure or (iii) both of superatmospheric pressure and/or subatmospheric pressure sequentially or consecutively or (iv) one or more additives to assist in causing the flow of water through said membrane from said First Solution and into said Second Brine Solution.

2 . A process as in claim 1 wherein the dissolved lithium salt(s) in said First Solution comprise(s) dissolved lithium chloride.

3 . A process as in claim 1 wherein said First Solution comprises at least dissolved lithium chloride, sodium chloride, and calcium chloride.

4 . A process of claim 1 wherein said forward osmosis membrane has an active membrane side and a backing/support side.

5 . A process as in claim 1 wherein the process is conducted on a batch basis in a unit which supports a forward osmosis membrane and also divides the unit into a first and second internal chamber in which said first chamber is adapted to receive a flow of said First Solution and contact it with one side of said membrane and recirculate said flow back into said first chamber, and wherein said second chamber is adapted to receive a flow of said Second Brine Solution and contact it with the other side of said membrane and recirculate said flow back into said second chamber during a period of operation of the process, whereby water is caused to flux through said membrane from said first chamber and into said second chamber, thereby increasing the lithium concentration of said recirculated First Solution.

6 . A process as in claim 1 wherein the process is conducted on a semi-continuous basis in a unit which supports a forward osmosis membrane and divides the unit into a first and second internal chamber in which said first chamber is adapted to receive a flow of said First Solution and contact it with one side of said membrane and recirculate said flow back into said first chamber, and wherein said second chamber is adapted to receive a continuous or pulsed flow of non-recycled Second Brine Solution into, through, and out of said second chamber while causing said Second Brine Solution to contact the other side of said membrane during a period of operation of the process, whereby water is caused to flux through said membrane from said first chamber into said second chamber, thereby increasing the lithium concentration of said recirculated First Solution.

7 . A process as in claim 1 wherein the process is conducted on a continuous basis in a unit which supports a forward osmosis membrane and divides the unit into a first and second internal chamber in which said first chamber is adapted to receive a continuous or pulsed flow of non-recycled First Solution into, through, and out of said first chamber while causing said First Solution to contact one side of said membrane, and wherein said second chamber is adapted to receive a continuous or pulsed flow of non-recycled Second Brine Solution into, through, and out of said second chamber while causing said Second Brine Solution to contact the other side of said membrane during a period of operation of the process, whereby water is caused to flux through said membrane from said first chamber into said second chamber, thereby increasing the lithium concentration of said non-recycled First Solution.

8 . A process as in claim 7 wherein said unit is adapted to permit both of said flows to pass in and out of said unit in countercurrent directions whereby flow of said first and second solutions can occur at any time through said unit during the operation of the process (i) as recirculated countercurrent flow, or (ii) as continuous countercurrent flow, or (iii) as pulsed countercurrent flow, or (iv) as any combination of any two of said flows of (i), (ii), or (iii).

9 . A process as in claim 7 wherein said unit is adapted to permit both of said flows to pass in and out of the unit in concurrent directions whereby flow of said first and second solutions can occur at any time through said unit during the operation of the process (i) as recirculated concurrent flow, or (ii) as continuous concurrent flow, or (iii) as pulsed concurrent flow, or (iv) as any combination of any two of said flows of (i), (ii), or (iii).

10 . A process as in claim 7 wherein said unit is one of a plurality of units which are disposed either in series or in parallel or both.

11 . A process as in claim 7 wherein said unit is adapted to permit both of said flows to pass in and out of said unit in countercurrent directions whereby flow of said first and second solutions can occur at any time through said unit during the operation of the process (i) as recirculated countercurrent flow, or (ii) as continuous countercurrent flow, or (iii) as pulsed countercurrent flow, or (iv) as any combination of any two of said flows of (i), (ii), or (iii), and wherein said unit is one of a plurality of units which are disposed either in series or in parallel or both.

12 . A process as in claim 7 wherein said unit is adapted to permit both of said flows to pass in and out of the unit in concurrent directions whereby flow of said first and second solutions can occur at any time through said unit during the operation of the process (i) as recirculated concurrent flow, or (ii) as continuous concurrent flow, or (iii) as pulsed concurrent flow, or (iv) as any combination of any two of said flows of (i), (ii), or (iii), and wherein said unit is one of a plurality of units which are disposed either in series or in parallel or both.

13 . A process as in claim 1 wherein said semi-permeable forward osmosis membrane is a (a) thin film composite membrane comprised of an active semi-permeable layer and a backing/support layer of (i) a different film and/or (ii) a porous support member or (b) a cellulose acetate membrane comprised of an active semi-permeable layer and a porous support member, and wherein said osmosis membrane is disposed and supported between said first and second solutions with the active semi-permeable layer facing and in direct contact with said First Solution.

14 . A process as in claim 1 wherein said semi-permeable forward osmosis membrane is a (a) thin film composite membrane comprised of an active semi-permeable layer and a backing/support layer of (i) a different film and/or (ii) a porous support member or (b) a cellulose acetate membrane comprised of an active semi-permeable layer and a porous support member, and wherein said osmosis membrane is disposed and supported

Assignees

• Albemarle Corp

Inventors

• Switzer Jackson Reeves
• Colonius Neal J
• Cheng Chi Hung
• Daudey Pieter Johannes

Classifications

• B01D61/58 Primary

  Multistep processes · CPC title

• Y02W10/37

  using solar energy · CPC title

• B01D61/025

  Reverse osmosis; Hyperfiltration · CPC title

• C02F2209/001

  Upstream control, i.e. monitoring for predictive control · CPC title

• B01D2315/10

  Cross-flow filtration · CPC title