CN203530440U - Electrolysis device - Google Patents
Electrolysis device Download PDFInfo
- Publication number
- CN203530440U CN203530440U CN201320572821.3U CN201320572821U CN203530440U CN 203530440 U CN203530440 U CN 203530440U CN 201320572821 U CN201320572821 U CN 201320572821U CN 203530440 U CN203530440 U CN 203530440U
- Authority
- CN
- China
- Prior art keywords
- electrolyzer
- tank
- retaining plate
- pedestal
- electrolytic solution
- 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.)
- Expired - Fee Related
Links
- 238000005868 electrolysis reaction Methods 0.000 title claims abstract description 32
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 41
- 229910001868 water Inorganic materials 0.000 claims abstract description 41
- 239000007788 liquid Substances 0.000 claims abstract description 36
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims abstract description 17
- 229910052719 titanium Inorganic materials 0.000 claims abstract description 17
- 239000010936 titanium Substances 0.000 claims abstract description 17
- 230000008901 benefit Effects 0.000 claims abstract description 13
- 239000008151 electrolyte solution Substances 0.000 claims description 29
- NJPPVKZQTLUDBO-UHFFFAOYSA-N novaluron Chemical compound C1=C(Cl)C(OC(F)(F)C(OC(F)(F)F)F)=CC=C1NC(=O)NC(=O)C1=C(F)C=CC=C1F NJPPVKZQTLUDBO-UHFFFAOYSA-N 0.000 claims description 25
- 230000004888 barrier function Effects 0.000 claims description 18
- 238000001816 cooling Methods 0.000 claims description 15
- 239000002699 waste material Substances 0.000 claims description 14
- 239000004020 conductor Substances 0.000 claims description 11
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims description 6
- 235000011941 Tilia x europaea Nutrition 0.000 claims description 6
- 239000002826 coolant Substances 0.000 claims description 6
- 239000004571 lime Substances 0.000 claims description 6
- 230000005574 cross-species transmission Effects 0.000 claims description 5
- 239000012528 membrane Substances 0.000 claims description 4
- 229910001069 Ti alloy Inorganic materials 0.000 claims description 3
- 239000000956 alloy Substances 0.000 claims description 3
- 238000005452 bending Methods 0.000 claims description 3
- 230000008595 infiltration Effects 0.000 claims description 3
- 238000001764 infiltration Methods 0.000 claims description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 2
- 125000000129 anionic group Chemical group 0.000 claims description 2
- 229910052799 carbon Inorganic materials 0.000 claims description 2
- 125000002091 cationic group Chemical group 0.000 claims description 2
- 239000011159 matrix material Substances 0.000 claims description 2
- 239000003792 electrolyte Substances 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 13
- 239000000498 cooling water Substances 0.000 description 4
- 239000001257 hydrogen Substances 0.000 description 4
- 229910052739 hydrogen Inorganic materials 0.000 description 4
- 150000002431 hydrogen Chemical class 0.000 description 3
- 239000012266 salt solution Substances 0.000 description 3
- 239000002912 waste gas Substances 0.000 description 3
- OSVXSBDYLRYLIG-UHFFFAOYSA-N dioxidochlorine(.) Chemical compound O=Cl=O OSVXSBDYLRYLIG-UHFFFAOYSA-N 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 150000002978 peroxides Chemical class 0.000 description 2
- 230000021715 photosynthesis, light harvesting Effects 0.000 description 2
- 239000004155 Chlorine dioxide Substances 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 235000019398 chlorine dioxide Nutrition 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
Images
Abstract
The utility model relates to an electrolysis device, which comprises a water tank and an electrolysis bath; wherein, the water tank is used for holding water liquid and the electrolytic bath, a water inlet is arranged at the lower side of the water tank, and an overflow port is arranged above the other end of the water tank; the electrolytic tank is placed in the water tank and comprises a base, a titanium net is arranged in the base in an inner ring mode to serve as an anode, the top of the base is provided with a gas collecting port and a conductive piece connected with the titanium net, the lower side of the base is provided with an electrolyte inlet, two sides of the base are respectively provided with a diaphragm unit through combination elements, the outer sides of the two diaphragm units are respectively provided with a fixing plate used as a cathode, the top of the fixing plate is provided with the conductive piece, an anode chamber is formed between the titanium net and the diaphragm, and a cathode chamber is formed between the fixing plate and the diaphragm; by means of the structure, the water liquid in the water tank can directly cool the fixing plate used as the cathode so as to cool and reduce the temperature of the cathode, and further the electrolysis benefit can be improved and the cathode damage can be reduced.
Description
Technical field
The utility model is a kind of electrolyzer, particularly a kind ofly can effectively reduce cathode temperature, to improve the electrolyzer of electrolysis benefit.
Background technology
Current electrolytic industry, mainly to utilize negative plate and positive plate are set in an electrolyzer, then anticathode plate and positive plate are switched on so as to electrolytic solution (as: water, salt solution etc.) is carried out to electrolysis, to obtain the product (as: hydrogen, oxygen or dioxide peroxide etc.) after electrolysis, and the product isolation of barrier film so that negative electrode and positive electrode is given birth to can be set in electric groove, so as to improving the purity of electrolysate.
And look into, because electrolysis operation anticathode plate and positive plate switch on to carry out electrolysis operation, and when energising electrolysis, it can produce heat energy in negative plate, temperature in electrolyzer in electrolyzer is increased, and it makes the Quality Down of product except easily causing the temperature of electrolysate to raise, and it is also easy to cause the excess Temperature of electrolytic solution, and then reduce electrolysis benefit and electrolysate is reduced, and be easy to so cause the damage of negative plate and positive plate; Vertical have dealer fan to be set to reduce the temperature in electrolyzer in electrolyzer both sides, but because it is failed direct cooling negative plate and makes it reduce temperature, and effective clear and have the facts that needs external source drive fan and have energy dissipation to occur; The temperature of electrolytic solution in electrolyzer while therefore how effectively to reduce energising electrolysis, in fact for current electrolysis industry has problem to be solved.
Utility model content
Technical problem underlying to be solved in the utility model is, overcomes the above-mentioned defect that prior art exists, and a kind of electrolyzer is provided, and the temperature can cooling reduction negative electrode producing because of energising, improves electrolysis benefit.
The utility model solves the technical scheme that its technical problem adopts:
An electrolyzer, includes a tank and an electrolyzer; Wherein:
Tank, in order to bearing water liquid and electrolyzer, this tank downside is provided with a water-in, and this water-in can pivot joint cooling-water machine, frozen water machine etc., and tank the other end top is provided with an overflow port, makes the water coolant liquid of too much spill-over can discharge tank;
Electrolyzer, be placed in tank, include a pedestal, this pedestal is generally a frame-like, in pedestal, being equipped with titanium net makes as anode, pedestal top is also provided with a gas collection mouth and an electric-conductor being connected with titanium net, and this gas collection mouth provides discharge and the collection of gas after electrolysis, and this electric-conductor provides the energising of titanium net; Pedestal downside is also provided with an electrolytic solution input aperture, and this electrolytic solution input aperture can be connected with electrolytic solution storage tanks by transfer lime, and pedestal upside is provided with an electrolytic solution overflow port, and this electrolytic solution overflow port can be connected with electrolytic solution accumulator tank by transfer lime; Again, these pedestal both sides each by binding member in conjunction with being provided with a diaphragm cell, this diaphragm cell includes a film frame, holds in framed and is provided with barrier film, framed both sides are held from inside to outside and are provided with a gasket, strongback and a gasket, and this strongback obtains can locate fixedly barrier film its unlikely bending is come off; The outside of two diaphragm cells is respectively provided with a retaining plate, and this retaining plate is usingd as negative electrode use so that titanium alloy material is made, and the top of retaining plate is provided with electric-conductor, to provide the energising of retaining plate to use; Make between titanium net and barrier film and form anolyte compartment, between retaining plate and barrier film, form cathode compartment; Again, on this retaining plate and be provided with a waste liquid relief outlet and a gas discharge outlet; Meanwhile, by gasket only every, make to form in electrolyzer in the unlikely infiltration electrolyzer of water liquid of confined air chien shih cooling trough;
By above-mentioned structure, provide a kind of water liquid of tank can be directly to making retaining plate that negative electrode uses, to carry out coolingly, with the temperature of cooling reduction negative electrode, and then can improve electrolysis benefit and reduce the electrolyzer that negative electrode damages.
The beneficial effects of the utility model are, the temperature can cooling reduction negative electrode producing because of energising, improves electrolysis benefit.
Accompanying drawing explanation
Below in conjunction with drawings and Examples, the utility model is further illustrated.
Fig. 1 is three-dimensional exploded view of the present utility model.
Fig. 2 is the three-dimensional exploded view of the utility model diaphragm cell.
Fig. 3 is frontview of the present utility model.
Fig. 4 is sectional view of the present utility model.
Fig. 5 is assembled sectional view of the present utility model, and the schematic diagram of the direct cooling retaining plate of water liquid of tank.
Number in the figure explanation:
10 tank 11 water-ins
12 overflow port 20 electrolyzers
21 pedestal 211 titanium nets
212 gas collection mouth 213 electric-conductors
214 electrolytic solution input aperture 215 electrolytic solution overflow ports
22 diaphragm cells 221 are framed
222 barrier film 223 gaskets
224 strongback 225 windows
23 retaining plate 231 electric-conductors
232 waste liquid relief outlet 233 gas discharge outlets
30A, 30B binding member A anolyte compartment
B cathode compartment
Embodiment
As shown in Figure 1, the electrolyzer in embodiment, includes a tank 10 and an electrolyzer 20; Wherein:
Tank 10 (shown in Fig. 3, Fig. 4), in order to bearing water liquid and electrolyzer 20, these tank 10 downsides are provided with a water-in 11, this water-in 11 can pivot joint cooling-water machine, frozen water machine etc., tank 10 the other end tops are provided with an overflow port 12, make the water coolant liquid of too much spill-over can discharge tank 10.
Electrolyzer 20 (shown in Fig. 2, Fig. 3, Fig. 4), be placed in tank 10, include a pedestal 21, this pedestal 21 is generally a frame-like, in pedestal 21, being equipped with titanium net 211 makes as anode, pedestal 21 tops are also provided with a gas collection mouth 212 and an electric-conductor 213 being connected with titanium net 211, and this gas collection mouth 212 provides discharge and the collection of gas after electrolysis, and this electric-conductor 213 provides the energising of titanium net 211; Pedestal 21 downsides are also provided with an electrolytic solution input aperture 214, this electrolytic solution input aperture 214 can be connected with electrolytic solution storage tanks (not disclosing in figure) by transfer lime (not disclosing in figure), pedestal 21 upsides are provided with an electrolytic solution overflow port 215, and this electrolytic solution overflow port 215 can be connected with electrolytic solution accumulator tank (not disclosing in figure) by transfer lime (not disclosing in figure); Again, each is provided with a diaphragm cell 22 by binding member 30A, 30B combination these pedestal 21 both sides, this diaphragm cell 22 includes a film frame 221, in framed 221, hold and be provided with barrier film 222, make 222, titanium net 211 and barrier film form the A of anolyte compartment, framed 221 both sides are held from inside to outside and are provided with a gasket 223, strongback 224 and a gasket 223, and this strongback 224 is provided with several windows 225, make strongback 224 can locate fixedly barrier film 222 its unlikely bending is come off; The outside of two diaphragm cells 22 is respectively provided with a retaining plate 23, this retaining plate 23 with titanium alloy material made using as negative electrode, use, the top of retaining plate 23 is provided with electric-conductor 231, to provide the energising of retaining plate 23 to use, and makes retaining plate 23 and 222, barrier film form cathode compartment B; Again, on this retaining plate 23 and be provided with a waste liquid relief outlet 232 and a gas discharge outlet 233, this waste liquid relief outlet 232 can connecting conveying pipe (not disclosing in figure) be discharged waste liquid; Meanwhile, by gasket 223 only every, make in the unlikely infiltration electrolyzer 20 of water liquid of the interior formation confined air of electrolyzer 20 chien shih cooling trough 10.
Hold above-mentionedly, this barrier film 222 can be the film that an anionic membrane, cationic membrane, carbon element film or other matrix material etc. are made.
By above-mentioned structure, as shown in Figure 5, this electrolyzer 20 is placed in the tank 10 of water filling, and make electrolytic solution (as: salt solution) in the 214 input A of anolyte compartment of the electrolytic solution input aperture of electrolyzer, during electrolytic solution spill-over in the A of anolyte compartment, can be discharged by the set electrolytic solution overflow port 215 of pedestal 21 the other ends; Titanium net 211 and retaining plate 23 are switched on to electrolytic solution (as: salt solution) is carried out to electrolysis, with electrolysis, produce the gas that wish is collected, and by the obstruct of barrier film 222, gas (as: the dioxide peroxide ClO that makes wish collect
2) be able to discharge and collect from the gas collection mouth 213 at electrolyzer 20 tops, and the waste liquid producing after electrolysis (as: water H
2o) and waste gas (as: hydrogen H
2) can drain in cathode compartment B through ion-exchange, make waste liquid (as: water H
2o) obtain and can discharge from waste liquid relief outlet 232, waste gas (as: hydrogen H
2) can be discharged by outlet port 233, waste liquid and waste gas are not stranded in electrolyzer 20 and affect electrolysis operation.
Now, by this electrolyzer 20, be directly placed in tank 10, when being used as retaining plate 23 that negative electrode uses and producing heat energy because of energising, water liquid in tank 10 can directly be done heat exchange to retaining plate 23, and so as to reducing the temperature of retaining plate 23, the temperature of non-reason retaining plate 23 rises and causes electrolysis benefit unclear; And because tank 10 continues by water-in 11 input water liquid, this overflow port 12 can make the water liquid of spill-over discharge, therefore make the water liquid heating up after heat exchange flow out from overflow port 12, and can be connected to continue to input with cooling-water machine or frozen water machine cold water by water-in 11, make can maintain low-temperature condition in cooling trough 10, and 23 energisings of reason retaining plate do not heat up and make the temperature in cooling trough 20 increase.
By above-mentioned structure and illustrate knownly, the utility model really has advantages of as follows:
(1) because the utility model is combined pedestal 21, diaphragm cell 22 by binding member 30A, 30B with retaining plate 23 pivot joints, it tears prescription open just, when pedestal 21, diaphragm cell 22 or retaining plate 23 have damage, detachable maintaining is changed in real time, and the carrying out of the follow-up electrolysis operation of unlikely impact.
(2) by the utility model, utilize barrier film 222 to separate out the A of anolyte compartment and cathode compartment B, make the unlikely mutual circulation of waste liquid after electrolytic solution and electrolysis, and then can separate electrolysate (as: chlorine dioxide, hydrogen and water etc.), and the waste liquid producing after electrolysis can be discharged and unlikely residuing in cathode compartment B, and then can effectively improve electrolysis benefit.
(3) because the utility model is directly used the retaining plate 23 in electrolyzer 20 outsides as negative electrode, and this electrolyzer 20 is placed in tank 10, make the water liquid in tank 10 directly to retaining plate 23, do heat exchange, make retaining plate 23 reason electrolysis when energising the heat energy that produces and cause temperature to rise, and then can effectively to retaining plate 23, cool, to improve electrolysis benefit.
(4) because the utility model utilizes water coolant stored in tank 10, retaining plate 23 is cooled, therefore the utility model can be by water-in 11 pivot joint cooling-water machines, frozen water machine, aqua storage tank etc., water coolant by input lower temperature cools to retaining plate 23, it can improve the cooling rate of retaining plate 23, and the water liquid after heat exchange is discharged to recovery cooling to be used with recirculation, and the facts that can reduce energy dissipation occurs, and because this cooling trough 10 is open shape, therefore it can improve the radiating rate of retaining plate 23 and water coolant liquid again, to improve the rate of heat exchange of water liquid.
By being, from above described, the utility model really can provide a kind of can cooling by anticathode, make negative electrode not reason energising produce heat energy and heat up, and then can improve electrolysis benefit and reduce negative electrode and damage electrolyzer.
The above, it is only preferred embodiment of the present utility model, not the utility model is done to any pro forma restriction, any simple modification, equivalent variations and modification that every foundation technical spirit of the present utility model is done above embodiment, all still belong in the scope of technical solutions of the utility model.
In sum, the utility model is in structure design, use practicality and cost benefit, meet industry development completely required, and the structure disclosing is also to have unprecedented innovative structure, there is novelty, creativeness, practicality, the regulation that meets relevant new patent important document, therefore mention application in accordance with the law.
Claims (2)
1. an electrolyzer, is characterized in that, includes a tank and an electrolyzer; Wherein:
Tank, in order to bearing water liquid and electrolyzer, this tank downside is provided with a water-in, and tank the other end top is provided with an overflow port, makes the water coolant liquid of too much spill-over can discharge tank;
Electrolyzer, be placed in tank, include a pedestal, this pedestal is generally a frame-like, in pedestal, being equipped with titanium net makes as anode, pedestal top is also provided with a gas collection mouth and an electric-conductor being connected with titanium net, and this gas collection mouth provides discharge and the collection of gas after electrolysis, and this electric-conductor provides the energising of titanium net; Pedestal downside is also provided with an electrolytic solution input aperture, and this electrolytic solution input aperture can be connected with electrolytic solution storage tanks by transfer lime, and pedestal upside is provided with an electrolytic solution overflow port, and this electrolytic solution overflow port can be connected with electrolytic solution accumulator tank by transfer lime; Again, each is provided with a diaphragm cell by binding member combination these pedestal both sides, this diaphragm cell includes a film frame, in framed, hold and be provided with barrier film, make between titanium net and barrier film and form anolyte compartment, framed both sides are held from inside to outside and are provided with a gasket, strongback and a gasket, and this strongback is provided with several windows, make strongback can locate fixedly barrier film its unlikely bending is come off; The outside of two diaphragm cells is respectively provided with a retaining plate, this retaining plate with titanium alloy material made using as negative electrode, use, the top of retaining plate is provided with electric-conductor, to provide the energising of retaining plate to use, and makes and between retaining plate and barrier film, forms cathode compartment; Again, on this retaining plate and be provided with a waste liquid relief outlet and a gas discharge outlet, this waste liquid relief outlet can connecting conveying pipe so that waste liquid is discharged; Meanwhile, by gasket only every, make to form in electrolyzer in the unlikely infiltration electrolyzer of water liquid of confined air chien shih cooling trough;
By above-mentioned structure, provide a kind of water liquid of tank can be directly to making retaining plate that negative electrode uses, to carry out coolingly, with the temperature of cooling reduction negative electrode, and then can improve electrolysis benefit and reduce the electrolyzer that negative electrode damages.
2. electrolyzer according to claim 1, is characterized in that, described barrier film can be anionic membrane, cationic membrane, carbon element film or the made film of other matrix material.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| TW101218182U TWM445585U (en) | 2012-09-20 | 2012-09-20 | Electrolysis apparatus |
| TW101218182 | 2012-09-20 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203530440U true CN203530440U (en) | 2014-04-09 |
Family
ID=48091258
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320572821.3U Expired - Fee Related CN203530440U (en) | 2012-09-20 | 2013-09-14 | Electrolysis device |
Country Status (2)
| Country | Link |
|---|---|
| CN (1) | CN203530440U (en) |
| TW (1) | TWM445585U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107513722A (en) * | 2016-06-15 | 2017-12-26 | 庄政霖 | Electrolysis installation |
| CN114807992A (en) * | 2021-01-18 | 2022-07-29 | 庄政霖 | Two-tank electrolytic tank |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| TWI648431B (en) * | 2018-01-03 | 2019-01-21 | 莊政霖 | Electrolysis device |
-
2012
- 2012-09-20 TW TW101218182U patent/TWM445585U/en not_active IP Right Cessation
-
2013
- 2013-09-14 CN CN201320572821.3U patent/CN203530440U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107513722A (en) * | 2016-06-15 | 2017-12-26 | 庄政霖 | Electrolysis installation |
| CN107513722B (en) * | 2016-06-15 | 2019-04-09 | 庄政霖 | Electrolysis installation |
| CN114807992A (en) * | 2021-01-18 | 2022-07-29 | 庄政霖 | Two-tank electrolytic tank |
Also Published As
| Publication number | Publication date |
|---|---|
| TWM445585U (en) | 2013-01-21 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140409 Termination date: 20150914 |
|
| EXPY | Termination of patent right or utility model |