Novel compounds as hif-1 alpha inhibitors and manufacturing process thereof
US-2016193215-A1 · Jul 7, 2016 · US
US9550728B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9550728-B2 |
| Application number | US-201214235192-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 27, 2012 |
| Priority date | Jul 27, 2011 |
| Publication date | Jan 24, 2017 |
| Grant date | Jan 24, 2017 |
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The present invention relates to a thermo-responsive draw solute that can be applied to water desalination and purification based on forward osmosis. The thermo-responsive draw solute has a molar mass of 50 to 3000 g/mol and undergoes a phase transition at a temperature of 0° C. to 70° C. The thermo-responsive draw solute creates optimum conditions for the desalination of seawater and the purification of contaminated water based on forward osmosis. The present invention also relates to a method for water desalination and purification using the thermo-responsive draw solute. The method consumes little energy for water desalination or purification, is simple to apply to water desalination or purification, and enables separation of the draw solute in a very easy manner.
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The invention claimed is: 1. A method for water desalination and purification using a thermo-responsive draw solute for forward osmosis, the method comprising: 1) bringing unpurified water into contact with a draw solution comprising the thermo-responsive draw solute at a higher concentration than the unpurified water through a semi-permeable membrane; 2) allowing clean water to flow from the unpurified water into the draw solution through the semi-permeable membrane by forward osmosis; 3) adjusting the temperature of the draw solution to or above the critical solution temperature of the thermo-responsive draw solute to cause a lower critical solution temperature (LCST) phase separation of the thermo-responsive draw solute from the draw solution; and 4) separating the clean water from the thermo-responsive draw solution. 2. The method according to claim 1 , wherein the thermo-responsive draw solute for forward osmosis has a molar mass of 50 to 3000 g/mol and undergoes a LCST phase transition at a temperature of 0° C. to 70° C. 3. The method according to claim 1 , wherein the thermo-responsive draw solute for forward osmosis is selected from the group consisting of: and mixtures thereof. 4. The method according to claim 1 , wherein the semi-permeable membrane is a cellulose acetate or polyether sulfone semi-permeable membrane. 5. The method according to claim 1 , wherein the unpurified water is water comprising ions, colloids, microbes, water soluble molecules, insoluble organic molecules, or mixtures thereof. 6. The method according to claim 1 , wherein the draw solution is formed by dissolving phase-separated thermo-responsive draw solute. 7. A method for water desalination and purification using a thermo-responsive draw solute for forward osmosis, the method comprising: 1) bringing unpurified water into contact with a draw solution comprising the thermo-responsive draw solute at a higher concentration than the unpurified water through a semi-permeable membrane; 2) allowing clean water to flow from the unpurified water into the draw solution through the semi-permeable membrane by forward osmosis; 3) adjusting the temperature of the draw solution to or below the critical solution temperature of the thermo-responsive draw solute to cause an upper critical solution temperature (UCST) phase separation of the thermo-responsive draw solute from the draw solution; and 4) separating the clean water from the thermo-responsive draw solution. 8. The method according to claim 7 , wherein the thermo-responsive draw solute has a molar mass of 50 to 3000 g/mol and undergoes an UCST phase transition at a temperature of 0° C. to 70° C. 9. The method according to claim 7 , wherein the thermo-responsive draw solute is selected from the group consisting of: and mixtures thereof. 10. The method according to claim 7 , wherein the semi-permeable membrane is a cellulose acetate or polyether sulfone semi-permeable membrane. 11. The method according to claim 7 , wherein the unpurified water is water comprising ions, colloids, microbes, water soluble molecules, insoluble organic molecules, or mixtures thereof. 12. The method according to claim 7 , wherein the draw solution is formed by dissolving phase-separated thermo-responsive draw solute. 13. A method for water desalination and purification using a thermo-responsive draw solute for forward osmosis, the method comprising: 1) bringing unpurified water into contact with a draw solution comprising the thermo-responsive draw solute at a higher concentration than the unpurified water through a semi-permeable membrane; 2) allowing clean water to flow from the unpurified water into the draw solution through the semi-permeable membrane by forward osmosis; 3) adjusting the temperature of the draw solution to or below the critical solution temperature of the thermo-responsive draw solute to cause a phase transition of the thermo-responsive draw solute from the draw solution; and 4) separating the clean water from the draw solution, wherein the thermo-responsive draw solute is selected from the group consisting of: and mixtures thereof. 14. The method according to claim 13 , wherein the phase transition in element 3) results in phase separation of the thermo-responsive draw solute.
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