Water with switchable ionic strength

Patent metadata

Field	Value
Publication number	US-11498853-B2
Application number	US-201916279221-A
Country	US
Kind code	B2
Filing date	Feb 19, 2019
Priority date	Feb 10, 2010
Publication date	Nov 15, 2022
Grant date	Nov 15, 2022

Abstract

A method and system for reversibly converting water between an initial ionic strength and an increased ionic strength, using a switchable additive, is described. The disclosed method and system can be used, for example, in distillation-free removal of water from solvents, solutes, or solutions. Following extraction of a solute from a medium by dissolving it in water, the solute can then be isolated from the aqueous solution or “salted-out” by converting the water to a solution having an increased ionic strength. The solute then separates from the increased ionic strength solution as a separate phase. Once the solute is, for example, decanted off, the increased ionic strength aqueous solution can be converted back to water having its original ionic strength and reused. Switching from lower to higher ionic strength is readily achieved using low energy methods such as bubbling with CO2, CS2 or COS. Switching from higher to lower ionic strength is readily achieved using low energy methods such as bubbling with air, heating, agitating, introducing a vacuum or partial vacuum, or any combination or thereof.

First claim

We claim:

1. A system for modulating an osmotic gradient across a membrane, comprising:
a semi-permeable membrane that is selectively permeable for water;
a switchable water, which comprises water and a switchable additive, the switchable water having a switchable ionic strength;
and
a source of an ionizing trigger, wherein the ionizing trigger ionizes the switchable additive into its water-miscible or water soluble protonated salt form and thereby increases the ionic strength of the switchable water;

wherein the switchable water contacts a first side of the semi-permeable membrane, and an aqueous feed stream contacts a second side of the semi-permeable membrane:
wherein the system modulates the osmotic gradient across said semi-permeable membrane via modulating the ionic strength of the switchable water, and
wherein the switchable additive has the general formula (1):

where R 1 , R 2 , and R 3 are independently:
H;
a substituted or unsubstituted C 1 to C 8 aliphatic group that is linear, branched, or cyclic, optionally wherein one or more C of the alkyl group is replaced by {—Si(R 10 ) 2 —O—} up to and including 8 C being replaced by 8 {—Si(R 10 ) 2 —O—};
a substituted or unsubstituted C n Si m group where n and m are independently a number from 0 to 8 and n+m is a number from 1 to 8:
a substituted or unsubstituted C 4 to C 8 aryl group wherein aryl is optionally heteroaryl, optionally wherein one or more C is replaced by {—Si(R 10 ) 2 —O—};
a substituted or unsubstituted aryl group having 4 to 8 ring atoms, optionally including one or more {—Si(R 10 ) 2 —O—}, wherein aryl is optionally heteroaryl;
a —(Si(R 0 ) 2 —O) p — chain in which p is from 1 to 8 which is terminated by H, or is terminated by a substituted or unsubstituted C 1 to C 8 aliphatic and/or aryl group; or a substituted or unsubstituted (C 1 to C 8 aliphatic)-(C 4 to C 8 aryl) group wherein aryl
is optionally heteroaryl, optionally wherein one or more C is replaced by a {—Si(R 10 ) 2 —O—};
wherein any two of R 1 , R 2 , and R 3 , taken together with the nitrogen to which they are attached, are optionally joined to form a heterocyclic ring;
wherein R 10 is a substituted or unsubstituted C 1 to C 8 aliphatic group, a substituted or unsubstituted C 1 to C 8 alkoxy, a substituted or unsubstituted C 4 to C 8 aryl wherein aryl is optionally heteroaryl, a substituted or unsubstituted aliphatic-alkoxy, a substituted or unsubstituted aliphatic-aryl, or a substituted or unsubstituted alkoxy-aryl group; and wherein a substituent is independently; alkyl; alkenyl; alkynyl; aryl; aryl-halide; heteroaryl; cycloalkyl; Si(alkyl) 3 ; Si(alkoxy) 3 ; halo; alkoxyl; amino; alkylamino; alkenylamino; amide; hydroxyl; thioether; alkylcarbonyl; alkylcarbonyloxy; arylcarbonyloxy; alkoxycarbonyloxy; aryloxycarbonyloxy; carbonate; alkoxycarbonyl; aminocarbonyl; alkylthiocarbonyl; phosphate; phosphate ester; phosphonato; phosphinato; cyano; acylamino; imino; sulfhydryl; alkylthio; arylthio; thiocarboxylate; dithiocarboxylate; sulfate; sulfato; sulfonate; sulfamoyl; sulfonamide; nitro; nitrile; azido; heterocyclyl; ether, ester, silicon-containing moieties; thioester; or a combination thereof;
with the proviso that at least one of R 1 , R 2 and R 3 is not H.

2. The system of claim 1 , wherein the feed stream is seawater, brackish water, or wastewater.

3. The system of claim 1 , wherein the ionizing trigger is CO 2 , COS, CS 2 , or a combination thereof.

4. The system of claim 3 , wherein the ionizing trigger is CO 2 .

5. The system of claim 1 , wherein the system additionally comprises a source of a non-ionizing trigger, wherein the non-ionizing trigger deprotonates the switchable additive.

6. The system of claim 5 , wherein the non-ionizing trigger is (i) heat, (ii) a flushing gas, (iii) a vacuum or partial vacuum, (iv) agitation, or (v) any combination thereof.

7. The system of claim 5 , wherein the system additionally comprises an apparatus to separate the deprotonated switchable additive from the water in said switchable water.

8. The system of claim 7 , wherein the apparatus comprises a reverse osmosis system.

9. The system of claim 7 , wherein the deprotonated switchable additive is immiscible in water and wherein the apparatus comprises a decanter to decant the deprotonated switchable additive from the water; or, the deprotonated switchable additive is insoluble in water and wherein the apparatus comprises a filter to remove the insoluble deprotonated switchable additive.

10. The system of claim 1 , wherein the switchable additive is:
MDEA (N-methyl diethanol-amine);
TMDAB (N, N, N′, N′-tetramethyl-1, 4-diaminobutane);
TEDAB (N,N,N′,N′-tetraethyl-1,4-diaminobutane);
EPDAB (N,N′-diethyl-N,N′-dipropyl-1,4-diaminobutane);
THEED (N, N, N′, N′-tetrakis(2-hydroxyethyl) ethylenediamine);
DMAPAP (1-[bis[3-(dimethylamino)]propyl]amino]-2-propanol);
HMTETA (1,1,4,7,10,10-hexamethyl triethylenetetramine);
MeSpe (N 1 ,N 1′ -(butane-1,4-diyl)bis(N 1 ,N 3 ,N 3 -trimethylpropane-1,3-diamine);
Methylated polyethyleneimine; or
CHTDMA (1,1′,1″-(cyclohexane-1,3,5-triyl)tris(N,N,-dimethylmethanamine).

11. A method of desalinating an aqueous salt solution or concentrating a dilute aqueous solution, comprising the steps of:
(a) contacting a switchable water comprising water and a switchable additive with an ionizing trigger to ionize the switchable additive into its water-miscible or water soluble protonated salt form and thereby increase the ionic strength of the switchable water;
(b) providing a semi-permeable membrane that is selectively permeable for water and has on one side a draw solution that comprises said switchable water, wherein the step of contacting the switchable water with the ionizing trigger to switch the switchable additive into its water-miscible or water soluble protonated salt form is performed before or after association of the switchable water with the semi-permeable membrane to increase the osmotic pressure of the draw solution; and
(c) contacting the other side of the semi-permeable membrane with a feed stream of the aqueous salt solution or the dilute aqueous solution to permit water to flow from the feed stream through the semi-permeable membrane into the increased ionic strength draw solution; wherein the switchable additive has the general formula (1):

where R 1 , R 2 , and R 3 are independently:
H;
a substituted or unsubstituted C 1 to C 8 aliphatic group that is linear, branched, or cyclic, optionally wherein one or more C of the alkyl group is replaced by {—Si(R 10 ) 2 —O—} up to and including 8 C being replaced by 8 {—Si(R 10 ) 2 —O—};
a substituted or unsubstituted C n Si m group where n and m are independently a number from 0 to 8 and n+m is a number from 1 to 8;
a substituted or unsubstituted C 4 to C 8 aryl group wherein aryl is optionally heteroaryl, optionally wherein one or more C is replaced by {—Si(R 10 ) 2 —O—};
a substituted or unsubstituted aryl group having 4 to 8 ring atoms, optionally including one or more {—Si(R 10 ) 2 —O—}, wherein aryl is optionally heteroaryl;
a —(Si(R 10 ) 2 —O) p — chain in which p is from 1 to 8 which is terminated by H, or is terminated by a substituted or unsubstituted C 1 to C 8 aliphatic and/or aryl group; or a substituted or unsubstituted (C 1 to C 8 aliphatic)-(C 4 to C 8 aryl) group wherein ar

Assignees

• Univ Kingston

Inventors

• Jessop Philip G
• Mercer Sean M
• Brown R Stephen
• Robert Tobias

Classifications

• C02F1/008

  Control or steering systems not provided for elsewhere in subclass C02F · CPC title

• C02F1/445

  by forward osmosis · CPC title

• C02F1/02

  by heating (methods of steam generation F22B; preheating boiler feed-water or accumulating preheated boiler feed-water F22D) · CPC title

• B01D61/025

  Reverse osmosis; Hyperfiltration · CPC title

• C02F1/44 Primary

  by dialysis, osmosis or reverse osmosis {(general membrane separation processes B01D61/00, membrane modules B01D63/00, electrodialysis C02F1/4693, combination of membrane modules and bioreactors C02F3/1268)} · CPC title