CN105110431A - Filtering plant and technique by using flow-through capacitor deionization - Google Patents
Filtering plant and technique by using flow-through capacitor deionization Download PDFInfo
- Publication number
- CN105110431A CN105110431A CN201510550081.7A CN201510550081A CN105110431A CN 105110431 A CN105110431 A CN 105110431A CN 201510550081 A CN201510550081 A CN 201510550081A CN 105110431 A CN105110431 A CN 105110431A
- Authority
- CN
- China
- Prior art keywords
- dividing plate
- fluid
- type
- insoluble electrode
- tabula
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Abstract
The invention relates to a filtering plant and technique by using flow-through capacitor deionization. The filtering plant is composed of an A-type partition, a B-type partition, an electrolysis-insoluble electrode and a fluid storage tank, wherein the A-type partition, B-type partition and electrolysis-insoluble electrode are sequentially superposed to constitute a capacitor group; and when a filtered fluid sinuously flows through plate capacitors in the capacitor group to form an electric field, ions in the filtered fluid are adsorbed to the electrolysis-insoluble electrode, thereby filtering and purifying the filtered fluid.
Description
Technical field
The present invention relates to field of Environment Protection, particularly filter plant and the technique of formula capacitive deionization method is flow through in a kind of utilization.
Background technology
Flow through formula capacitive deionization method FTC(FlowThroughCapacitor, also known as CDI:CapacitiveDeionization), also electrostatic adhesion method is claimed, CDI is under the effect of electrical forces, directly the ionic adsorption that relative quantity in fluid is very little is separated, instead of a large amount of fluids is separated from former fluid, thus without the need to high temperature, high pressure, so energy consumption is relatively low, and dense less fluid, output capacity are high.CDI technology obtains practical application in the sewage disposal such as ferrous metallurgy, petrochemical refining, and embodies advantage;
Above-mentioned fluid choice liquid, a kind of in gas, special choice water;
The ＂ mono-kind of the present inventor is that just oneself discloses a kind of winding capacitance formula and utilizes the filter plant and technique that flow through formula capacitive deionization method for the electro-adsorption water treating equipment of electrode and technique ＂ (201210315573.4) patent of invention with active carbon fiber fabrics, because the filter effect that flows through formula capacitive deionization method and capacity area and fluid electric field distance of passing by is directly proportional function, and electrode has resistance, filter effect and electrode resistance are inversely proportional to function, so the folded folder wire netting way of electrode reduces electrode resistance in No. 201210315573.4 patent of invention equipment, there is wire netting and active carbon fiber fabrics loose contact risk in this, and add production cost, Samsung Electronics Co., Ltd also has capacity plate antenna type " deionizer and manufacture method thereof " (200810178157.8) to have employed metal currect collecting net to reduce electrode resistance in China's application, be necessary reform for this reason.
Summary of the invention
The object of the invention is to provide a kind of has comparatively bulky capacitor area in a constant volume, make fluid electric field distance of passing by longer, and electrode has the utilization of less resistive to flow through filter plant and the technique of formula capacitive deionization method;
The present invention seeks to realize like this: the filter plant of formula capacitive deionization method is flow through in a kind of utilization, by A type dividing plate, Type B dividing plate, electrolysis insoluble electrode, store fluid chamber to form, it is characterized in that described A type dividing plate has the breach a1 of an extended electrolysis insoluble electrode wicking termination on the right of upper end, water flowing breach a2 is had on the right of A type dividing plate, rectangle emptying aperture in the middle of A type dividing plate, 2-5 bar is had to give prominence to tabula a3, outstanding tabula a3 ensures two inter-electrode space isolation, forms capacity plate antenna, also forms fluid and flows through electric capacity passage;
Electrically insulating material selected by A type dividing plate, selects plastics especially;
Type B dividing plate has the breach b1 of an extended electrolysis insoluble electrode wicking termination on the left side, upper end, there is water flowing breach b2 on the Type B dividing plate left side, rectangle emptying aperture in the middle of Type B dividing plate, 2-5 bar is had to give prominence to tabula b3, outstanding tabula b3 ensures two inter-electrode space isolation, form capacity plate antenna, also form fluid and flow through electric capacity passage;
Electrically insulating material selected by Type B dividing plate, selects plastics especially;
Electrolysis insoluble electrode is tabular rectangle, has an outstanding rectangular electrode wicking termination on electrolysis insoluble electrode upper left side;
Electrolysis insoluble electrode Material selec-tion titanium, graphite, a kind of in activated carbon fiber, select activated carbon fiber especially;
Store the square chest that fluid chamber cross section is rectangle, its geometrical dimension meets loading closed assembly capacity plate antenna group,
Be filtered fluid inlet joint storing the left case basifacial of fluid chamber, be filtered fluid outlet connection storing top, fluid chamber right case face, there is backwash fluid inlet union storing the right case basifacial of fluid chamber, have backwash fluid outlet connection storing top, fluid chamber left case face;
Store fluid chamber and select electrically insulating material, select plastics especially;
The filter plant installation order that formula capacitive deionization method is flow through in above-mentioned utilization is as follows:
1.) sequentially install from left to right: first piece is A type dividing plate, second piece is electrolysis insoluble electrode, electrolysis insoluble electrode wicking termination is stretched out from the breach a1 of first piece of A type dividing plate, 3rd piece is Type B dividing plate, 4th piece is electrolysis insoluble electrode, electrolysis insoluble electrode wicking termination is stretched out from the breach b1 of the 3rd piece of Type B dividing plate, 5th piece is A type dividing plate, 6th piece is electrolysis insoluble electrode, and electrolysis insoluble electrode wicking termination is stretched out from the breach a1 of the 5th piece of A type dividing plate;
Forwards like this below, form closed assembly capacity plate antenna group, closed assembly capacity plate antenna group contains 41-121 electrolysis insoluble electrode, form 40-120 capacity plate antenna electric field, owing to having 2-5 bar to give prominence to tabula a3 and outstanding tabula b3 in the middle of A type dividing plate and Type B dividing plate, outstanding tabula a3 and outstanding tabula b3 has ensured that two inter-electrode space are isolated, and forms capacity plate antenna, also forms fluid and flows through electric capacity passage;
2.) closed assembly capacity plate antenna group put into and store fluid chamber, it is in parallel all breach a1 from A type dividing plate to be stretched out electrolysis insoluble electrode wicking termination, connects power cathode; All breach b1 from Type B dividing plate are stretched out electrolysis insoluble electrode wicking termination in parallel, connect positive source;
3.) to dispute painting leak-proof coating storing fluid chamber upper surface, anti-fluid spills from the gap closed assembly capacity plate antenna group;
The above-mentioned filter plant flowing through formula capacitive deionization method is utilized to carry out filtration process as follows:
(a). be filtered fluid and be filtered fluid inlet enter from storing the left case basifacial of fluid chamber, at A type dividing plate water flowing breach a2, outstanding tabula a3 and Type B dividing plate water flowing breach b2, under outstanding tabula b3 guides, complications form electric field by capacity plate antenna, are finally filtered fluid outlet outflow from storing top, fluid chamber right case face;
Be filtered fluid when complications form electric field by capacity plate antenna, be filtered fluid intermediate ion and be attracted to filtration, purification electrolysis insoluble electrode realizing being filtered fluid;
(b) adopt known technology to confirm in technique on electrolysis insoluble electrode absorption be filtered ion in fluid oneself saturated time, cut off the electricity supply, change valve, stop being filtered fluid and flow into; Change from storing fluid chamber right case basifacial backwash fluid import input backwash fluid; backwash fluid is at A type dividing plate water flowing breach a2; outstanding tabula a3 and Type B dividing plate water flowing breach b2; under outstanding tabula b3 guides; tortuous by capacity plate antenna Special composition, flow out from storing the backwash fluid outlet of top, fluid chamber left case face;
Owing to cutting off the electricity supply, capacitive field rut disappears, and ion, from desorption electrolysis insoluble electrode, is carried by backwash fluid, flowing out, realizing electrolysis insoluble electrode regeneration purification from storing the backwash fluid outlet of top, fluid chamber left case face;
C () gets back to program (a).
Accompanying drawing explanation
Fig. 1 is A type diaphragm structure schematic diagram.
Fig. 2 is Type B diaphragm structure schematic diagram.
Fig. 3 is electrolysis insoluble electrode structural representation.
Fig. 4 is closed assembly capacity plate antenna group structure schematic diagram.
Fig. 5 is filtered fluid at A type dividing plate water flowing breach a2, outstanding tabula a3 and Type B dividing plate water flowing breach b2, under outstanding tabula b3 guides, and the tortuous schematic diagram being formed electric field by capacity plate antenna.
Fig. 6 is electrolysis insoluble electrode electricity wiring schematic diagram in closed assembly capacity plate antenna group.
Fig. 7 stores fluid chamber structural representation.
Embodiment
Below in conjunction with accompanying drawing, the present invention is specifically described (but not limiting the scope of the present invention), the filter plant of formula capacitive deionization method is flow through in a kind of utilization, by A type dividing plate (1), Type B dividing plate (2), electrolysis insoluble electrode (3), store fluid chamber (4) to form, it is characterized in that seeing that A type dividing plate (1) described in accompanying drawing 1 has the breach a1(1-1 of an extended electrolysis insoluble electrode (3) wicking termination (3-2) on the right of upper end), there is water flowing breach a2(1-2 on A type dividing plate (1) the right), rectangle emptying aperture in the middle of A type dividing plate (1), 2-5 bar is had to give prominence to tabula a3(1-3), outstanding tabula a3(1-3) ensure that two inter-electrode space isolation have 1-4mm, form capacity plate antenna, also form fluid and flow through electric capacity passage,
Electrically insulating material selected by A type dividing plate (1), selects plastics especially; A type dividing plate (1) supports vertical bar (1-4) thickness 2-4mm;
See that Type B dividing plate (2) described in accompanying drawing 2 has the breach b1 (2-1) of an extended electrolysis insoluble electrode (3) wicking termination (3-2) on the left side, upper end, there is water flowing breach b2 (2-2) on Type B dividing plate (2) left side, rectangle emptying aperture in the middle of Type B dividing plate (2), 2-5 bar is had to give prominence to tabula b3 (2-3), outstanding tabula b3 (2-3) ensures that two inter-electrode space isolation have 1-4mm, form capacity plate antenna, also form fluid and flow through electric capacity passage;
Electrically insulating material selected by Type B dividing plate (2), selects plastics especially; Type B dividing plate (2) supports vertical bar (2-4) thickness 2-4mm;
See that electrolysis insoluble electrode (3) described in accompanying drawing 3 is tabular 160 × 240-320 × 480mm
2rectangle, has an outstanding 10 × 20-20 × 40mm on electrolysis insoluble electrode (3) upper left side
2rectangular electrode wicking termination (3-2), tabular electrolysis insoluble electrode (3) thickness 2-6mm;
Electrolysis insoluble electrode (3) Material selec-tion titanium, graphite, a kind of in activated carbon fiber, select activated carbon fiber especially;
See that storing fluid chamber (4) cross section described in accompanying drawing 7 is the square chest of rectangle, its geometrical dimension meets loading closed assembly capacity plate antenna group (5),
Be filtered fluid inlet joint (4-3) storing the left case basifacial of fluid chamber (4), be filtered fluid outlet connection (4-4) storing top, fluid chamber right case face, there is backwash fluid import (4-1) joint storing the right case basifacial of fluid chamber, have backwash fluid outlet connection (4-2) storing top, fluid chamber left case face;
Store fluid chamber (4) and select electrically insulating material, select plastics especially;
The filter plant installation order that formula capacitive deionization method is flow through in above-mentioned utilization is as follows:
4. sequentially install from left to right: first piece is A type dividing plate (1), second piece is electrolysis insoluble electrode (3), electrolysis insoluble electrode wicking termination (3-2) is stretched out from the breach a1 (1-1) of first piece of A type dividing plate (1), 3rd piece is Type B dividing plate (2), 4th piece is electrolysis insoluble electrode (3), electrolysis insoluble electrode wicking termination (3-2) is stretched out from the breach b1 (2-1) of the 3rd piece of Type B dividing plate, 5th piece is A type dividing plate (1), 6th piece is electrolysis insoluble electrode (3), electrolysis insoluble electrode wicking termination (3-2) is stretched out from the breach a1 (1-1) of the mat woven of fine bamboo strips five pieces of A type dividing plates,
Forwards like this below, see and form closed assembly capacity plate antenna group (5) described in accompanying drawing 4, closed assembly capacity plate antenna group (5) is containing 41-121 electrolysis insoluble electrode, form 40-120 capacity plate antenna electric field, owing to having 2-5 bar to give prominence to tabula a3 (1-3) and outstanding tabula b3 (2-3) in the middle of A type dividing plate (1) and Type B dividing plate (2), outstanding tabula a3 (1-3) and outstanding tabula b3 (2-3) have ensured that two inter-electrode space are isolated and had 1-4mm, form capacity plate antenna, also form fluid and flow through electric capacity passage;
5. closed assembly capacity plate antenna group (5) is put into and store fluid chamber (4), see and all breach a1 (1-1) from A type dividing plate (1) are stretched out electrolysis insoluble electrode wicking termination (3-2) parallel connection described in accompanying drawing 6, connect power cathode; All breach b1 (2-1) from Type B dividing plate (2) are stretched out electrolysis insoluble electrode wicking termination (3-2) in parallel, connect positive source;
6. to dispute painting leak-proof coating storing fluid chamber (4) upper surface, anti-fluid spills from the gap closed assembly capacity plate antenna group (5);
The above-mentioned filter plant flowing through formula capacitive deionization method is utilized to carry out filtration process as follows:
(a). be filtered fluid and be filtered fluid inlet (4-3) enter from storing the left case basifacial of fluid chamber (4), at A type dividing plate (1) water flowing breach a2 (1-2), outstanding tabula a3 (1-3) and Type B dividing plate (2) water flowing breach b2 (2-2), under outstanding tabula b3 (2-3) guides, complications form electric field by capacity plate antenna, are finally filtered fluid outlet (4-4) outflow from storing top, fluid chamber right case face;
Be filtered fluid when complications form electric field by capacity plate antenna, be filtered fluid intermediate ion and be attracted to the upper filtration, purification realizing being filtered fluid of electrolysis insoluble electrode (3);
Capacity plate antenna applies volts DS 2-6V; Be filtered fluid by capacity plate antenna flow velocity 0.5-0.6m/min:
(b) adopt known technology to confirm in technique on electrolysis insoluble electrode absorption be filtered ion in fluid oneself saturated time, cut off the electricity supply, change valve, stop being filtered fluid and flow into; Change and input backwash fluid from storing fluid chamber (4) right case basifacial backwash fluid import (4-1); backwash fluid is at A type dividing plate (1) water flowing breach a2 (1-2); outstanding tabula a3 (1-3) and Type B dividing plate (2) water flowing breach b2 (2-2); under outstanding tabula b3 (2-3) guides; tortuous by capacity plate antenna Special composition, flow out from storing top, fluid chamber left case face backwash fluid outlet (4-2);
Owing to cutting off the electricity supply; capacitive field rut disappears, and ion, from desorption electrolysis insoluble electrode (3), is carried by backwash fluid; flowing out from storing top, fluid chamber left case face backwash fluid outlet (4-2), realizing electrolysis insoluble electrode regeneration purification;
Backwash fluid is be filtered fluid by the 1-20 of capacity plate antenna flow velocity doubly by capacity plate antenna flow velocity;
C () gets back to program (a);
See the tortuous schematic diagram being formed electric field by capacity plate antenna of fluid shown in accompanying drawing 5.
Embodiment
Embodiment 1. selects seawater to be filtered fluid, utilizes the above-mentioned filter plant flowing through formula capacitive deionization method to realize fresh water with technique and is separated with saliferous concentrated seawater, then adopts known technology from saliferous concentrated seawater, to be separated results sodium salt, sylvite, lithium salts; Backwash fluid selects fresh water;
Embodiment 2. selects alkali paper-making black liquor to be filtered fluid, utilizes the above-mentioned filter plant flowing through formula capacitive deionization method to realize alkali with technique and is separated with containing xylogen water, then adopt known technology to gather in the crops xylogen from containing being separated xylogen water; Backwash fluid selects water purification; Alkali reuse papermaking;
Embodiment 3. selects electroplating wastewater to be filtered fluid; utilize the above-mentioned filter plant flowing through formula capacitive deionization method to realize water purification with technique to be separated with the dense water containing poisonous electroplating composition, then adopt known technology from the dense water of poisonous electroplating composition, be separated the solid-state poisonous electroplating composition of results; Backwash fluid selects water purification; Solid-state poisonous electroplating composition contains nickel, chromium, copper recoverable.
Claims (2)
1. the filter plant of formula capacitive deionization method is flow through in a utilization, by A type dividing plate (1), Type B dividing plate (2), electrolysis insoluble electrode (3), store fluid chamber (4) to form, it is characterized in that seeing that A type dividing plate (1) described in accompanying drawing 1 has the breach a1(1-1 of an extended electrolysis insoluble electrode (3) wicking termination (3-2) on the right of upper end), there is water flowing breach a2(1-2 on A type dividing plate (1) the right), rectangle emptying aperture in the middle of A type dividing plate (1), 2-5 bar is had to give prominence to tabula a3(1-3), outstanding tabula a3(1-3) ensure that two inter-electrode space isolation have 1-4mm, form capacity plate antenna, also form fluid and flow through electric capacity passage, electrically insulating material selected by A type dividing plate (1), selects plastics especially, A type dividing plate (1) supports vertical bar (1-4) thickness 2-4mm,
See that Type B dividing plate (2) described in accompanying drawing 2 has the breach b1 (2-1) of an extended electrolysis insoluble electrode (3) wicking termination (3-2) on the left side, upper end, there is water flowing breach b2 (2-2) on Type B dividing plate (2) left side, rectangle emptying aperture in the middle of Type B dividing plate (2), 2-5 bar is had to give prominence to tabula b3 (2-3), outstanding tabula b3 (2-3) ensures that two inter-electrode space isolation have 1-4mm, form capacity plate antenna, also form fluid and flow through electric capacity passage; Electrically insulating material selected by Type B dividing plate (2), selects plastics especially; Type B dividing plate (2) supports vertical bar (2-4) thickness 2-4mm;
See that electrolysis insoluble electrode (3) described in accompanying drawing 3 is tabular 160 × 240-320 × 480mm
2rectangle, has an outstanding 10 × 20-20 × 40mm on electrolysis insoluble electrode (3) upper left side
2rectangular electrode wicking termination (3-2), tabular electrolysis insoluble electrode (3) thickness 2-6mm; Electrolysis insoluble electrode (3) Material selec-tion titanium, graphite, a kind of in activated carbon fiber, select activated carbon fiber especially; See that storing fluid chamber (4) cross section described in accompanying drawing 7 is the square chest of rectangle, its geometrical dimension meets loading closed assembly capacity plate antenna group (5), be filtered fluid inlet joint (4-3) storing the left case basifacial of fluid chamber (4), be filtered fluid outlet connection (4-4) storing top, fluid chamber right case face, there is backwash fluid import (4-1) joint storing the right case basifacial of fluid chamber, have backwash fluid outlet connection (4-2) storing top, fluid chamber left case face; Store fluid chamber (4) and select electrically insulating material, select plastics especially;
The filter plant installation order that formula capacitive deionization method is flow through in above-mentioned utilization is as follows:
(1) sequentially install from left to right: first piece is A type dividing plate (1), second piece is electrolysis insoluble electrode (3), electrolysis insoluble electrode wicking termination (3-2) is stretched out from the breach a1 (1-1) of first piece of A type dividing plate (1), 3rd piece is Type B dividing plate (2), 4th piece is electrolysis insoluble electrode (3), electrolysis insoluble electrode wicking termination (3-2) is stretched out from the breach b1 (2-1) of the 3rd piece of Type B dividing plate, 5th piece is A type dividing plate (1), 6th piece is electrolysis insoluble electrode (3), electrolysis insoluble electrode wicking termination (3-2) is stretched out from the breach a1 (1-1) of the 5th piece of A type dividing plate,
Forwards like this below, see and form closed assembly capacity plate antenna group (5) described in accompanying drawing 4, closed assembly capacity plate antenna group (5) is containing 41-121 electrolysis insoluble electrode, form 40-120 capacity plate antenna electric field, owing to having 2-5 bar to give prominence to tabula a3 (1-3) and outstanding tabula b3 (2-3) in the middle of A type dividing plate (1) and Type B dividing plate (2), outstanding tabula a3 (1-3) and outstanding tabula b3 (2-3) have ensured that two inter-electrode space are isolated and had 1-4mm, form capacity plate antenna, also form fluid and flow through electric capacity passage;
(2) closed assembly capacity plate antenna group (5) is put into store fluid chamber (4), see and all breach a1 (1-1) from A type dividing plate (1) are stretched out electrolysis insoluble electrode wicking termination (3-2) parallel connection described in accompanying drawing 6, connect power cathode; All breach b1 (2-1) from Type B dividing plate (2) are stretched out electrolysis insoluble electrode wicking termination (3-2) in parallel, connect positive source;
(3) to dispute painting leak-proof coating storing fluid chamber (4) upper surface, anti-fluid spills from the gap closed assembly capacity plate antenna group (5).
2., according to right 1, utilize the above-mentioned filter plant flowing through formula capacitive deionization method to carry out filtration process as follows:
A () is filtered fluid and is filtered fluid inlet (4-3) enters from storing the left case basifacial of fluid chamber (4), at A type dividing plate (1) water flowing breach a2 (1-2), outstanding tabula a3 (1-3) and Type B dividing plate (2) water flowing breach b2 (2-2), under outstanding tabula b3 (2-3) guides, complications form electric field by capacity plate antenna, are finally filtered fluid outlet (4-4) outflow from storing top, fluid chamber right case face; Be filtered fluid when complications form electric field by capacity plate antenna, be filtered fluid intermediate ion and be attracted to the upper filtration, purification realizing being filtered fluid of electrolysis insoluble electrode (3); Capacity plate antenna applies volts DS 2-6V; Be filtered fluid by capacity plate antenna flow velocity 0.5-0.6m/min:
(b) adopt known technology to confirm in technique on electrolysis insoluble electrode absorption be filtered ion in fluid oneself saturated time, cut off the electricity supply, change valve, stop being filtered fluid and flow into; Change and input backwash fluid from storing fluid chamber (4) right case basifacial backwash fluid import (4-1); backwash fluid is at A type dividing plate (1) water flowing breach a2 (1-2); outstanding tabula a3 (1-3) and Type B dividing plate (2) water flowing breach b2 (2-2); under outstanding tabula b3 (2-3) guides; tortuous by capacity plate antenna Special composition, flow out from storing top, fluid chamber left case face backwash fluid outlet (4-2); Owing to cutting off the electricity supply; capacitive field rut disappears, and ion, from desorption electrolysis insoluble electrode (3), is carried by backwash fluid; flowing out from storing top, fluid chamber left case face backwash fluid outlet (4-2), realizing electrolysis insoluble electrode regeneration purification;
Backwash fluid is be filtered fluid by the 1-20 of capacity plate antenna flow velocity doubly by capacity plate antenna flow velocity;
C () gets back to program (a).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510550081.7A CN105110431B (en) | 2015-09-01 | 2015-09-01 | It is a kind of to utilize the filter plant and technique for flowing through formula capacitive deionization method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510550081.7A CN105110431B (en) | 2015-09-01 | 2015-09-01 | It is a kind of to utilize the filter plant and technique for flowing through formula capacitive deionization method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105110431A true CN105110431A (en) | 2015-12-02 |
| CN105110431B CN105110431B (en) | 2017-07-07 |
Family
ID=54658603
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510550081.7A Active CN105110431B (en) | 2015-09-01 | 2015-09-01 | It is a kind of to utilize the filter plant and technique for flowing through formula capacitive deionization method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105110431B (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106977024A (en) * | 2017-05-12 | 2017-07-25 | 长沙理工大学 | A kind of suspension purifier suitable for South Sea dredging work |
| CN112794415A (en) * | 2021-01-28 | 2021-05-14 | 重庆大学 | Capacitive deionization device and method for submerged flow electrode |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1417816A (en) * | 2001-10-31 | 2003-05-14 | 友昕科技股份有限公司 | Independent flow-thru capacitor |
| CN101518748A (en) * | 2008-02-29 | 2009-09-02 | 三星电子株式会社 | Deionization apparatus and method of manufacturing the same |
| US20100025247A1 (en) * | 2008-07-31 | 2010-02-04 | Daily Iii William D | Capacitive de-ionization electrode |
| CN101973608A (en) * | 2010-11-12 | 2011-02-16 | 北京化工大学 | Electro adsorption water treatment module |
| WO2012066413A1 (en) * | 2010-11-18 | 2012-05-24 | Idropan Dell'orto Depuratori S.R.L. | Flow-through condenser cell for purifying a fluid |
| KR101150841B1 (en) * | 2009-10-26 | 2012-06-13 | 한국전력공사 | Suction electrode and water treatment system by electrosorption |
-
2015
- 2015-09-01 CN CN201510550081.7A patent/CN105110431B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1417816A (en) * | 2001-10-31 | 2003-05-14 | 友昕科技股份有限公司 | Independent flow-thru capacitor |
| CN101518748A (en) * | 2008-02-29 | 2009-09-02 | 三星电子株式会社 | Deionization apparatus and method of manufacturing the same |
| US20100025247A1 (en) * | 2008-07-31 | 2010-02-04 | Daily Iii William D | Capacitive de-ionization electrode |
| KR101150841B1 (en) * | 2009-10-26 | 2012-06-13 | 한국전력공사 | Suction electrode and water treatment system by electrosorption |
| CN101973608A (en) * | 2010-11-12 | 2011-02-16 | 北京化工大学 | Electro adsorption water treatment module |
| WO2012066413A1 (en) * | 2010-11-18 | 2012-05-24 | Idropan Dell'orto Depuratori S.R.L. | Flow-through condenser cell for purifying a fluid |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106977024A (en) * | 2017-05-12 | 2017-07-25 | 长沙理工大学 | A kind of suspension purifier suitable for South Sea dredging work |
| CN112794415A (en) * | 2021-01-28 | 2021-05-14 | 重庆大学 | Capacitive deionization device and method for submerged flow electrode |
Also Published As
| Publication number | Publication date |
|---|---|
| CN105110431B (en) | 2017-07-07 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103723868B (en) | Water purifier | |
| US20020167782A1 (en) | Charge barrier flow-through capacitor | |
| CN205151856U (en) | Electric capacity deionization purifier | |
| CN102807266B (en) | Supercapacitor desalting unit, device and method | |
| US20030106845A1 (en) | Automatic device for purifying drinking water | |
| CN104817143A (en) | Ion exchange membrane composite multi-electrode capacitance adsorption desalting apparatus | |
| KR20150084956A (en) | Impregnated electrode for capacitive deionisation, process for preparing it and apparatus employing the electrodes | |
| RU169004U1 (en) | SORPTION FILTER | |
| KR20140098241A (en) | Flow-through capacitor, deionized liquid manufacturing device, and deionized liquid manufacturing method | |
| CN105110431A (en) | Filtering plant and technique by using flow-through capacitor deionization | |
| CN108046385A (en) | A kind of total closed type capacitor deionizing instrument | |
| ITPD20120363A1 (en) | EQUIPMENT FOR THE PURIFICATION OF A FLUID AND A PURIFICATION METHOD OF A FLUID, IN PARTICULAR THROUGH THE ABOVE EQUIPMENT | |
| KR20150061323A (en) | Regeneration methods of capacitive deionization electrodes | |
| CN107244720A (en) | The device of electro-adsorption demineralization and salinity | |
| CN110809564B (en) | Desalination apparatus and method of manufacturing the same | |
| CN203820507U (en) | Laboratory wastewater treatment device | |
| CN204039187U (en) | A kind of household water purification system of electric flocculation treatment reverse osmosis concentrated water | |
| CN217051729U (en) | Water body deionization filter | |
| CN208218473U (en) | A kind of total closed type capacitive deionization desalter | |
| CN103880118A (en) | Wastewater treatment device for laboratory | |
| CN114906971A (en) | Composite multi-effect descaling integrated device and descaling system for geothermal fluid | |
| CN213202684U (en) | High salt waste water desalination processing system | |
| UA113995C2 (en) | METHOD OF WATER Purification Using Capacitive Deionization | |
| CN204324964U (en) | A kind of filter plant based on electromagnetic water treatment | |
| CN106474786A (en) | A kind of sea water desalinating unit |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |