Electrochemical system with real time modification of composition and use of complex wave form in same
US-2015241091-A1 · Aug 27, 2015 · US
US11339996B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11339996-B2 |
| Application number | US-201715800259-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 1, 2017 |
| Priority date | Mar 3, 2016 |
| Publication date | May 24, 2022 |
| Grant date | May 24, 2022 |
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An electrochemical compressor utilizes an anion conducting layer disposed between an anode and a cathode for transporting a working fluid. The working fluid may include carbon dioxide that is dissolved in water and is partially converted to carbonic acid that is equilibrium with bicarbonate anion. An electrical potential across the anode and cathode creates a pH gradient that drives the bicarbonate anion across the anion conducting layer to the cathode, wherein it is reformed into carbon dioxide. Therefore, carbon dioxide is pumped across the anion conducting layer. The compressor may be part of a refrigeration system that pumps the working fluid in a closed loop through a condenser and an evaporator.
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What is claimed is: 1. An electrochemical compressor system comprising: a) an electrochemical compressor comprising: i) an anode; ii) a cathode, iii) an anisotropic anion conducting layer between and in contact with the anode and cathode and comprising an anion conducting polymer; wherein the anion conducting polymer comprises a backbone selected from the group consisting of: poly(arylene), poly(phenylene) and poly(styrene); wherein the anion conducting layer is a composite anion conducting layer comprising a support material attached to the anion conducting polymer; wherein the anisotropic anion conducting layer has a concentration gradient of the functional groups from the anode to the cathode of at least 1.5:1; b) a working fluid; c) a power supply coupled electrically with the anode and cathode to produce a voltage potential across the anode and cathode; wherein the voltage potential at the anode produces hydroxyl ions and wherein the voltage potential at the cathode consumes hydroxyl ions to create a pH gradient to transfer the working fluid from the anode to the cathode; wherein the working fluid comprises carbon dioxide; wherein the carbon dioxide is in equilibrium with bicarbonate ions and wherein the bicarbonate ions are transported through the anion conducting layer from the anode to the cathode and reformed into carbon dioxide at the cathode. 2. The electrochemical compressor system of claim 1 , wherein the anisotropic anion conducting layer comprise a first anion conducting layer having a first concentration of functional groups and a second anion conducting layer having a second concentration of functional groups and wherein the first anion conducting layer is in contact with the anode and wherein the second anion conducting layer is in contact with the cathode. 3. The electrochemical compressor system of claim 2 , wherein the first concentration of functional groups is at least 1.5 greater than the second concentration of functional groups. 4. The electrochemical compressor system of claim 1 , wherein the anion conducting polymer comprises quaternary ammonium functional groups. 5. The electrochemical compressor system of claim 1 , wherein the anion conducting polymer comprises phosphonium groups functional groups. 6. The electrochemical compressor system of claim 1 , wherein the anion conducting polymer comprises alkyl or a piperidine side chain configured between a functional group and a backbone of the anion conducting polymer. 7. The electrochemical compressor system of claim 1 , wherein the anion conducting polymer comprises a backbone selected from the group consisting of: poly(arylene), poly(phenylene) and poly(styrene). 8. The electrochemical compressor system of claim 1 , wherein the anion conducting polymer comprises: quaternary ammonium functional groups, a backbone selected from the group consisting of: poly(arylene), poly(phenylene) and poly(styrene); and an alkyl or piperidine side chain configured between a functional group and a backbone of the anion conducting polymer. 9. The electrochemical compressor system of claim 1 , wherein the anion conducting layer is a composite anion conducting layer comprising a support material attached to the anion conducting polymer. 10. The electrochemical compressor system of claim 9 wherein the support material has a porosity of 55% to 90%. 11. The electrochemical compressor system of claim, 1 wherein the anion conducting layer has a thickness between 5 and 50 microns. 12. The electrochemical compressor system of claim 1 , wherein the working fluid comprises ammonia. 13. A refrigeration system defining a closed loop that contains a working fluid, wherein at least part of the working fluid is circulated through the closed loop, the refrigeration system comprising: a) an electrochemical compressor system of claim 1 ; b) a condenser; and c) an evaporator. 14. The refrigeration system of claim 13 , wherein the working fluid comprises carbon dioxide; wherein the carbon dioxide is in equilibrium with bicarbonate ions and wherein the bicarbonate ions are transported through the anion conducting layer from the anode to the cathode and reformed into carbon dioxide at the cathode. 15. The refrigeration system of claim 14 , wherein the anion conducting polymer comprises: quaternary ammonium functional groups, a backbone selected from the group consisting of: poly(arylene), poly(phenylene) and poly(styrene); and an alkyl or piperidine side chain configured between a functional group and a backbone of the anion conducting polymer. 16. The refrigeration system of claim 15 , wherein the anisotropic anion conducting layer comprise a first anion conducting layer having a first concentration of functional groups and a second anion conducting layer having a second concentration of functional groups and wherein the first anion conducting layer is in contact with the anode and wherein the second anion conducting layer is in contact with the cathode; and wherein the first concentration of functional groups is at least 1.5 greater than the second concentration of functional groups. 17. The refrigeration system of claim 13 , wherein the working fluid comprises ammonia.
Organic support material · CPC title
Specific temperatures applied · CPC title
Polystyrene · CPC title
by introduction of specific groups after membrane formation, e.g. by grafting · CPC title
In situ manufacturing by polymerisation, polycondensation, cross-linking or chemical reaction · CPC title
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