Mesoporous carbon composite material, production methods thereof, and electronic device including the same
US-2015340172-A1 · Nov 26, 2015 · US
US2016289097A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016289097-A1 |
| Application number | US-201415038111-A |
| Country | US |
| Kind code | A1 |
| Filing date | Nov 26, 2014 |
| Priority date | Nov 27, 2013 |
| Publication date | Oct 6, 2016 |
| Grant date | — |
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Treating a fluid may include using a flow-through capacitor that includes first and second electrodes and a flow path between the first and second electrodes, wherein an acidic aqueous solution is supplied to the capacitor to flow through the flow path while a reverse potential difference is formed across the first and second electrodes, and thereby deposits formed in the flow-through capacitor may be removed.
Opening claim text (preview).
1 . A method of treating a fluid containing dissolved solids, comprising: obtaining a flow-through capacitor, the flow-through capacitor including, at least one pair of porous electrodes, the at least one pair of porous electrodes including a first electrode and a second electrode, each electrode of the first and second electrodes including an electrode material, the electrode material having a surface area, each electrode being configured to electrostatically adsorb dissolved solids; and a flow path between the first electrode and the second electrode; flowing a fluid through the flow path of the flow-through capacitor, the fluid including dissolved solids; applying an electric potential difference across the first and second electrodes such that the first electrode becomes a positive electrode and the second electrode becomes a negative electrode, and the dissolved solids included in the fluid in the flow path are adsorbed to at least one porous electrode of the porous electrodes; causing the first electrode to become a negative electrode and the second electrode to become a positive electrode, such that the dissolved solids adsorbed to the at least one porous electrode are desorbed therefrom, based on performing one of removing the electric potential difference or applying a first reverse electric potential difference across the first and second electrodes and flowing an acidic aqueous solution through the flow path of the flow-through capacitor, concurrently with applying a second reverse electric potential difference across the first and second electrodes to remove deposits formed in the flow through capacitor. 2 . The method of claim 1 , wherein the flow path includes a spacer, the spacer defining a fluid flow channel, the spacer configured to permit the fluid to contact the first electrode and the second electrode. 3 . The method of claim 1 , wherein the flow-through capacitor further includes a charge barrier against cations, the charge barrier against cations being between the first electrode and a spacer, and a charge barrier against anions, the charge barrier against anions being between the second electrode and the spacer. 4 . The method of claim 1 , further comprising: iteratively performing, for a particular quantity of iterations, the applying the electric potential difference across the first and second electrodes, and the causing the first electrode to become a negative electrode and the second electrode to become a positive electrode. 5 . The method of claim 4 , further comprising: iteratively performing, until the flow-through capacitor has a deionization efficiency that is less than or equal to 70% of an initial deionization efficiency of the flow-through capacitor, the applying the electric potential difference across the first and second electrodes, and the causing the first electrode to become a negative electrode and the second electrode to become a positive electrode. 6 . The method of claim 1 , wherein, the electric potential difference applied across the first and second electrodes is greater than or equal to about 0.5 volts and less than or equal to about 3 volts, and the first reverse electric potential difference applied across the first and second electrodes is from about −3 volts to about 0 volts. 7 . The method of claim 1 , wherein the acidic aqueous solution includes at least one of an organic acid and an inorganic acid. 8 . The method of claim 1 , wherein the acidic aqueous solution has a pH of less than or equal to about 3. 9 . The method of claim 1 , wherein the acidic aqueous solution has apH of greater than or equal to about 1. 10 . The method of claim 1 , where the second reverse electric potential difference applied across the first and second electrodes is from about −3 volts to about −1.2 volts. 11 . The method of claim 1 , where an absolute value of the second reverse electric potential difference is less than or equal to an absolute value of the electric potential difference. 12 . The method of claim 1 , further comprising: flowing water through the flow path of the flow-through capacitor to remove the acidic aqueous solution remaining therein after the removal of the deposits. 13 . A capacitive deionization apparatus, comprising: a housing including an inlet and an outlet, the inlet configured to introduce at least one of a fluid to be treated or an acidic aqueous solution into the housing, the outlet configured to withdraw the at least one of the treated fluid or the acidic aqueous solution from the housing; a flow-through capacitor in the housing, the flow-through capacitor including at least one pair of porous electrodes, the at least one pair of porous electrodes including a first electrode and a second electrode, each electrode of the at least one pair of porous electrodes including an electrode material, the electrode material having a surface area, each electrode being configured to electrostatically adsorb dissolved solids; and a flow path between the first electrode and the second electrode; a supply unit configured to supply the fluid to be treated to the inlet; and a supply unit configured to supply an acidic aqueous solution to the inlet, the acidic aqueous solution having pH of about 1 to about 3. 14 . The capacitive deionization apparatus of claim 13 , wherein the flow path includes a spacer, the spacer defining a fluid flow channel, the spacer configured to permit the fluid to contact the first electrode and the second electrode. 15 . The capacitive deionization apparatus of claim 13 , wherein the flow-through capacitor further includes at least one of, a charge barrier against cations, the charge barrier against cations being between the first electrode and the spacer, and a charge barrier against anions, the charge barrier against anions being between the second electrode and the spacer. 16 . The capacitive deionization apparatus of claim 13 , wherein, the charge barrier against cations includes an anion exchange membrane, and the charge barrier against anions includes a cation exchange membrane. 17 . The capacitive deionization apparatus of claim 13 , wherein each electrode of the first electrode and the second electrode further includes a current collector at an opposite side of the electrode, relative to a side exposed to the flow path. 18 . The capacitive deionization apparatus of claim 13 , wherein each electrode of the first electrode and the second electrode includes a polarity-variable electrode.
Cleaning the electrodes · CPC title
Capacitive deionisation · CPC title
Regeneration of sorbents, filters · CPC title
by electrochemical separation, e.g. by electro-osmosis, electrodialysis, electrophoresis · CPC title
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