Method of treatment of radioactive wastewater
US-2015336815-A1 · Nov 26, 2015 · US
US9637400B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9637400-B2 |
| Application number | US-201514632003-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 26, 2015 |
| Priority date | Nov 30, 2007 |
| Publication date | May 2, 2017 |
| Grant date | May 2, 2017 |
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Electrochemical devices and methods for water treatment are disclosed. An electrodeionization device ( 100 ) may include one or more compartments ( 110 ) containing an ionselective media, such as boron-selective resin ( 170 ). Cyclic adsorption of target ions and regeneration of the media in-situ is used to treat process water, and may be driven by the promotion of various pH conditions within the electrochemical device.
Opening claim text (preview).
What is claimed is: 1. An electrically driven separation device, comprising: a first compartment at least partially defined by a first cation selective membrane and a first anion selective membrane; a second compartment at least partially defined by the first anion selective membrane and a second cation selective membrane, and at least one of the first compartment and the second compartment comprising a mixture of an anion exchange resin and a boron selective resin, the boron-selective resin located in at least one of the first compartment and the second compartment; and a third compartment at least partially defined by the second cation selective membrane and a bipolar membrane. 2. The device of claim 1 , wherein the mixture is 50/50 by volume of the anion exchange resin and the boron selective resin. 3. The device of claim 2 , wherein an outlet of the first compartment is fluidly connected to an inlet of the third compartment. 4. The device of claim 2 , wherein an outlet of the electrically driven separation device is fluidly connected to a potable point of use. 5. The device of claim 2 , wherein the resin comprises cis-diol functional groups. 6. The device of claim 1 , wherein the third compartment is substantially free of boron selective resin. 7. The device of claim 2 , wherein no reverse osmosis membrane is fluidly connected downstream of the electrically driven separation device. 8. The device of claim 2 , wherein no resin bed is fluidly connected downstream of the electrically driven separation device. 9. The device of claim 2 , further comprising a sensor positioned in fluid communication downstream of a resin bed in at least one of the first and second compartments, the sensor configured to provide a measurement signal representative of a concentration of boron in the treated water from the electrically driven separation device. 10. The device of claim 9 , wherein the measurement signal comprises a detected pH level. 11. The device of claim 9 , further comprising a controller in communication with the sensor and configured to produce a control signal to a power supply associated with the electrically driven separation device based at least partially on the measurement signal. 12. The device of claim 5 , wherein the boron selective media comprises N-methylglucamine functional groups.
Control or steering systems not provided for elsewhere in subclass C02F · CPC title
Boron compounds · CPC title
Regeneration of sorbents, filters · CPC title
Electrolytic cell with membranes or diaphragms · CPC title
pH · CPC title
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