Rotary Enthalpy Exchange Wheel Having Sulfonated Block Copolymer
US-2015375199-A1 · Dec 31, 2015 · US
US9550168B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9550168-B2 |
| Application number | US-201514864637-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 24, 2015 |
| Priority date | Apr 25, 2012 |
| Publication date | Jan 24, 2017 |
| Grant date | Jan 24, 2017 |
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A programmable pH buffer comprises a copolymer that changes pK a at a lower critical solution temperature (LCST) in water. The copolymer comprises a thermally programmable polymer that undergoes a hydrophobic-to-hydrophilic phase change at the LCST and an electrolytic polymer that exhibits acid-base properties that are responsive to the phase change. The programmable pH buffer can be used to sequester CO 2 into water.
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We claim: 1. A method for CO 2 sequestration into water, comprising: dissolving a programmable pH buffer in water thereby providing an aqueous solution, wherein the programmable pH buffer comprises a copolymer that changes pK a at a lower critical solution temperature in water, and wherein the copolymer comprises a thermally programmable polymer that undergoes a hydrophobic-to-hydrophilic phase change at the lower critical temperature and an electrolytic polymer that exhibits acid-base properties that are responsive to the phase change, and heating the aqueous solution above the lower critical solution temperature, wherein the copolymer changes from a high pK a in water below the lower critical solution temperature to a low pK a in water above the lower critical solution temperature, thereby releasing CO 2 into water upon heating the aqueous solution above the lower critical solution temperature. 2. A method for changing solution pH, comprising: dissolving a programmable pH buffer in water thereby providing an aqueous solution, wherein the programmable pH buffer comprises a copolymer that changes pK a at a lower critical solution temperature in water, and wherein the copolymer comprises a thermally programmable polymer that undergoes a hydrophobic-to-hydrophilic phase change at the lower critical temperature and an electrolytic polymer that exhibits acid-base properties that are responsive to the phase change, and wherein the copolymer has a buffer capacity of greater than 1 mM in aqueous solution, and heating the aqueous solution above or cooling the aqueous solution below the lower critical solution temperature, thereby changing the pH of the aqueous solution. 3. The method of claim 2 , wherein the electrolytic polymer comprises an acid. 4. The method of claim 3 , wherein the acid comprises acrylic acid. 5. The method of claim 2 , wherein the electrolytic polymer comprises an amine. 6. The method of claim 5 , wherein the amine comprises a primary amine. 7. The method of claim 6 , wherein the primary amine comprises N-(3-aminopropyl)methacrylamide hydrochloride. 8. The method of claim 2 , wherein the copolymer further comprises a hydrophobic monomer. 9. The method of claim 8 , wherein the hydrophobic monomer comprises methylmethacrylate, styrene, or n-butyl acrylate. 10. A method for CO 2 sequestration into water, comprising: dissolving a programmable pH buffer in water thereby providing an aqueous solution, wherein the programmable pH buffer comprises a copolymer that changes pK a at a lower critical solution temperature in water, and wherein the copolymer comprises a thermally programmable polymer that undergoes a hydrophobic-to-hydrophilic phase change at the lower critical temperature and an electrolytic polymer that exhibits acid-base properties that are responsive to the phase change, and heating the aqueous solution above the lower critical solution temperature, wherein the electrolytic polymer comprises a carboxylic acid group that captures CO 2 (g) from water above the lower critical solution temperature by converting carbonic acid (H 2 CO 3 ) to bicarbonate anion (HCO 3− ). 11. The method of claim 10 , further comprising cooling the aqueous solution below the lower critical solution temperature, whereby the copolymer releases CO 2 into water. 12. The method of claim 1 , 2 , or 10 , wherein the lower critical solution temperature is greater than 20° C. and less than 50° C. 13. The method of claim 1 , 2 , or 10 , wherein the thermally programmable polymer comprises poly(N-isopropylacrylamide), poly(N-ethylacrylamide) or poly(N,N-dimethylacrylamide).
derived from different types of monomers, e.g. linear or branched copolymers, block copolymers, graft copolymers · CPC title
Cross-Sectional Technologies · mapped topic
of CO2 · CPC title
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