CN201785505U - NaCIO generator - Google Patents
NaCIO generator Download PDFInfo
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- CN201785505U CN201785505U CN2010202640758U CN201020264075U CN201785505U CN 201785505 U CN201785505 U CN 201785505U CN 2010202640758 U CN2010202640758 U CN 2010202640758U CN 201020264075 U CN201020264075 U CN 201020264075U CN 201785505 U CN201785505 U CN 201785505U
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- Prior art keywords
- electrolyzer
- naclo
- pipeline
- dissolved salt
- nacio
- Prior art date
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- SUKJFIGYRHOWBL-UHFFFAOYSA-N sodium hypochlorite Chemical compound [Na+].Cl[O-] SUKJFIGYRHOWBL-UHFFFAOYSA-N 0.000 claims abstract description 54
- 150000003839 salts Chemical class 0.000 claims abstract description 39
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 24
- 238000003860 storage Methods 0.000 claims abstract description 17
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims description 22
- 239000002253 acid Substances 0.000 claims description 16
- 238000005868 electrolysis reaction Methods 0.000 claims description 14
- 238000011049 filling Methods 0.000 claims description 14
- 239000011780 sodium chloride Substances 0.000 claims description 11
- 239000001257 hydrogen Substances 0.000 claims description 10
- 229910052739 hydrogen Inorganic materials 0.000 claims description 10
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 9
- 150000001875 compounds Chemical class 0.000 claims description 9
- 239000000463 material Substances 0.000 claims description 8
- 239000007787 solid Substances 0.000 claims description 7
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 6
- 238000011084 recovery Methods 0.000 claims description 6
- 239000010936 titanium Substances 0.000 claims description 6
- 229910052719 titanium Inorganic materials 0.000 claims description 6
- 239000003792 electrolyte Substances 0.000 claims description 5
- 238000003756 stirring Methods 0.000 claims description 4
- 239000003814 drug Substances 0.000 claims description 3
- 229940079593 drug Drugs 0.000 claims description 3
- 238000007667 floating Methods 0.000 claims description 3
- 230000007306 turnover Effects 0.000 claims description 3
- 238000005406 washing Methods 0.000 claims description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 6
- 230000007774 longterm Effects 0.000 abstract description 4
- 238000012423 maintenance Methods 0.000 abstract description 4
- 239000005708 Sodium hypochlorite Substances 0.000 abstract 2
- WQYVRQLZKVEZGA-UHFFFAOYSA-N hypochlorite Chemical compound Cl[O-] WQYVRQLZKVEZGA-UHFFFAOYSA-N 0.000 description 11
- 239000000243 solution Substances 0.000 description 6
- 235000015598 salt intake Nutrition 0.000 description 4
- 239000007788 liquid Substances 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 238000005554 pickling Methods 0.000 description 3
- KZBUYRJDOAKODT-UHFFFAOYSA-N Chlorine Chemical compound ClCl KZBUYRJDOAKODT-UHFFFAOYSA-N 0.000 description 2
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 2
- 230000033228 biological regulation Effects 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 229910052710 silicon Inorganic materials 0.000 description 2
- 239000010703 silicon Substances 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 238000003466 welding Methods 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 241000195493 Cryptophyta Species 0.000 description 1
- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical compound [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 230000003064 anti-oxidating effect Effects 0.000 description 1
- 230000003260 anti-sepsis Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 239000007844 bleaching agent Substances 0.000 description 1
- 239000012267 brine Substances 0.000 description 1
- ZFXVRMSLJDYJCH-UHFFFAOYSA-N calcium magnesium Chemical compound [Mg].[Ca] ZFXVRMSLJDYJCH-UHFFFAOYSA-N 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 239000004020 conductor Substances 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 230000000249 desinfective effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 238000004043 dyeing Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000003487 electrochemical reaction Methods 0.000 description 1
- 230000005518 electrochemistry Effects 0.000 description 1
- 239000008151 electrolyte solution Substances 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 229910052741 iridium Inorganic materials 0.000 description 1
- GKOZUEZYRPOHIO-UHFFFAOYSA-N iridium atom Chemical compound [Ir] GKOZUEZYRPOHIO-UHFFFAOYSA-N 0.000 description 1
- 239000004973 liquid crystal related substance Substances 0.000 description 1
- 229910001425 magnesium ion Inorganic materials 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 230000000873 masking effect Effects 0.000 description 1
- 239000011159 matrix material Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
- 238000007639 printing Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 229910052707 ruthenium Inorganic materials 0.000 description 1
- 238000005480 shot peening Methods 0.000 description 1
- 238000007086 side reaction Methods 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 235000011149 sulphuric acid Nutrition 0.000 description 1
- 239000001117 sulphuric acid Substances 0.000 description 1
- RTKIYNMVFMVABJ-UHFFFAOYSA-L thimerosal Chemical compound [Na+].CC[Hg]SC1=CC=CC=C1C([O-])=O RTKIYNMVFMVABJ-UHFFFAOYSA-L 0.000 description 1
- 229940033663 thimerosal Drugs 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
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- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
A NaCIO generator comprises an electric control cabinet, an electrolyzing device, a salt dissolving device and a NaCIO storage tank. The NaCIO generator is characterized in that the electric control cabinet is electrically connected with the electrolyzing device, an electrolytic bath is arranged inside the electrolyzing device, water is respectively led into the electrolyzing device and the salt dissolving device by pipelines, a lift pump is arranged between the salt dissolving device and the electrolyzing device, an inlet end of the lift pump is connected with the salt dissolving device in a communicated manner by a pipeline, an outlet end of the lift pump is connected with the electrolyzing device in a communicated manner by a pipeline, and an NaCIO lead-out opening arranged on the electrolyzing device is connected with the NaCIO storage tank by a pipeline. The NaCIO generator solves the problems of complicated structure, high manufacturing cost, troublesome maintenance, short running cycle and influence on long-term safe running of equipment of a sodium hypochlorite generator adopting a pipe type electrolyzing pipe in the prior art, is simplified in equipment structure, small in occupied area, low in running cost and convenient in maintenance, and is a sodium hypochlorite generator capable of safely and reliably running in a complicated environment for a long period of time.
Description
Technical field
The utility model relates to technical field of electrochemistry, particularly relates to a kind of hypochlorite generator's electrolyzer.
Background technology
Hypochlorite generator's tubular type titanium-matrix electrode, introduce from the America and Europe eighties, and be applied in drinking water disinfection rapidly, and hospital wastewater is handled, the food disinfecting utensils, decolorizing printing and dyeing waste water, industrial circulating water removes industries such as algae, improves waters, manufacturing district ecology, the protection water surrounding.Generally adopt the electrolytic saltwater method to produce javelle water, its basic structure adopts the tubular type electrolyzer.Application number is a 87202871-hypochlorite generator tubular type electrolyzer, comprises end cap, insulating mat, and the anode seat, gasket, cathode tube, anode tube, anode is stifled, packing ring, insulating mat, gasket.During electrolysis, use the plastic centrifugal pump circulating brine, in electrolyzer, finish electrolytic process, produce the chlorine bleach liquor.When two above tubular type electrolyzers were formed the hypochlorite generator, its electrode on line adopted tandem, to improve electrolysis voltage, reduced Faradaic current, reduced conductor cross-section.Anode adopts the metal titanium pipe, and negative electrode adopts stainless steel tube.The operation of tubular type electrolyzer is because of containing the small amount of calcium magnesium ion in water or the salt, the easy fouling of electrolysis tube makes the electrode punch through damage; And tubular type electrolysis tube complex structure, is safeguarded loaded down with trivial detailsly at the manufacturing cost height, and the cycle of operation is short, influence the equipment long-term safety and moves.Equipment salt consumption, power consumption, water consumption take place in simultaneously present NaClO, and upkeep cost is high, and running cost is risen, and manufacturing expenses are high influences marketing.
The utility model content
In order to solve hypochlorite generator in the prior art, adopt tubular type electrolysis tube complex structure, the manufacturing cost height, safeguard loaded down with trivial details, the cycle of operation is short, influences the problem of equipment long-term safety operation, and the utility model provides a kind of device structure to simplify, floor space is little, running cost is low, and is easy to maintenance, can be the hypochlorite generator of the medium-term and long-term safe and reliable operation of complex environment.
The reaction principle of the utility model NaClO producer is: NaCl and H2O solution fed in the electrolyzer,
H+←H2O→OH-
Na+←NaCl→Cl-
2Cl--2e → Cl2 (anode)
2H++2e → H2 (negative electrode)
Cl2+2NaOH→NaClO+NaCl+H2O+H↑
In order to achieve the above object, technical solution adopted in the utility model is:
A kind of NaClO producer, comprise electrical control cubicles, electrolyzer, dissolved salt device and NaClO storage are irritated, it is characterized in that: described electrical control cubicles and electrolyzer are by being electrically connected, described electrolyzer shell adopts the Reinforced PVC material, be provided with electrolyzer in electrolyzer, described water is introduced electrolyzer and dissolved salt device by pipeline respectively;
Be provided with lift pump between dissolved salt device and electrolyzer, the entrance end of described lift pump connects with the dissolved salt device by pipeline and is connected, and the exit end of described lift pump connects with electrolyzer by pipeline and is connected;
Be provided with the NaClO outlet on electrolyzer, described NaClO outlet is irritated by pipe connection NaClO storage, irritates in the NaClO storage and is provided with the drug valve.
Aforesaid a kind of NaClO producer, it is characterized in that: also comprise the acid filling, between electrolyzer and acid filling, be provided with sour pump, the entrance end of described sour pump is irritated to connect by pipeline and acid and is connected, described sour pump outlet end connects with electrolyzer by pipeline and is connected, offer some discharge tubes in the side of electrolyzer, described discharge tube is connected with recovery channel, and described recovery channel feeds in the acid filling.
Aforesaid a kind of NaClO producer, it is characterized in that: be contained with the NaCl solid in the described dissolved salt device, be provided with the riser tubing that can mix NaCl solid and water at the top of dissolved salt device, the rear end of described riser tubing is connected with the entrance end of dissolved salt pump, described dissolved salt pump outlet end is connected with the dissolved salt device by liquid-inlet pipe, stirs valve and dissolved salt valve other being provided with of riser tubing.
Aforesaid a kind of NaClO producer is characterized in that: the electrolysis cells in the described electrolyzer is made up of the compound electrode of multi-disc, and the material of described compound electrode is TA
1The titanium plate, described electrolyzer electrolyte inside is " S " annularly flow.
Aforesaid a kind of NaClO producer is characterized in that: row's hydrogen blower fan that the hydrogen that produces when being provided with electrolysis at the top of electrolyzer is discharged.
Aforesaid a kind of NaClO producer is characterized in that: be provided with high frequency switch power in the described electrical control cubicles.
Aforesaid a kind of NaClO producer, it is characterized in that: between the NaClO of electrolyzer outlet and NaClO storage filling, be respectively equipped with slow-motion pipeline and F.F. pipeline, described slow-motion pipeline is provided with the slow-motion valve of control slow-motion pipe flow speed, and described F.F. pipeline is provided with the F.F. valve of control F.F. pipe flow speed.
Aforesaid a kind of NaClO producer is characterized in that: be provided with water washing device on the pipeline of water feeding electrolyzer.
Aforesaid a kind of NaClO producer is characterized in that: be provided with magnetic turnover panel liquidometer on the dissolved salt device, irritate in the NaClO storage and be provided with floating ball lever meter.
The beneficial effects of the utility model are
1, electrolyzer shell---crust of the device adopts the Reinforced PVC material, heatproof＞60 ℃, anti-oxidation and antisepsis＞30 year, withstand voltage 0.4Mpa.
2, compound electrode---the device core, electrode adopts TA
1Titanium plate, numerically-controlled machine shape, do not have welding, the surface is coated with multiple dilute metals such as iridium, ruthenium, improves the electrode oxidation-resistance, reduce the folding chloride potential, accurate utmost point water ratio, commutation operation regularly, electrode surface is less scaling, prolongation equipment continuous operating time, reduce pickling number of times (＞90 days), improve device capbility, reduce salt consumption, power consumption, water consumption.
3, cell construction---the compound electrode of electrolysis cells N sheet is formed, and the groove electrolyte inside is " S " annularly flow.Increase solution reaction duration of contact and turbulent property, commutation operation regularly reduces the electrode surface fouling, improves current efficiency, reduces the salt consumption.Suction type row hydrogen, safety is discharged outdoor after the diluted in hydrogen of producing during with electrolysis.
4, electrolysis power---high frequency switch power substitutes silicon-controlled rectifier.Adopt import element, digital control, liquid crystal display apparatus, small product size is little, efficient is high, easy to maintenance, than voltate regulator pressure regulation or transductor pressure regulating energy-saving 30%, than silicon-controlled voltage regulation energy-conservation 18%.
5, the utility model NaClO producer electrolyzer China similar A level product, the technical indicator contrast
| Technical parameter | The utility model product | Like product |
| Current efficiency % | ＞80 | 70 |
| Salt consumption kg/kg | ＜3.5 | 4 |
| Ac consumption KWh/kg | ＜4.2 | 6 |
| Direct current consumption KWh/kg | ＜3.8 | 4.5 |
| Effective concentration g/L | 8.5 | 7.2 |
| Water consumption m3/kg | 0.125 | - |
| Electrode effective run time h | ＞50000 | ?20000 |
6, the utility model NaClO producer prepares the efficient cost accounting of 1kg
=3.4 yuan of 0.85 yuan/degree of the electricity charge 4 degree *
Refined salt 3.2kg*0.8 unit/kg=2.56 unit adds up to: 6.35 yuan/kgCl2
Water consumption 0.13m3*3 unit/m3=0.39 unit
Description of drawings
Fig. 1 is the utility model NaClO generator architecture synoptic diagram;
Fig. 2 is the utility model electrolyzer structural representation.
Embodiment
Below in conjunction with accompanying drawing the utility model is further described.
As depicted in figs. 1 and 2, a kind of NaClO producer comprises electrical control cubicles 1, electrolyzer 2, and dissolved salt device 3, NaClO storage filling 4 and acid irritate 5.
Between dissolved salt device 3 and electrolyzer 2, be provided with lift pump 8, the entrance end of lift pump 8 connects with dissolved salt device 3 by pipeline and is connected, the exit end of lift pump 8 connects with electrolyzer 2 by pipeline and is connected, on dissolved salt device 3, be provided with magnetic turnover panel liquidometer 25, be used for showing liquid level, be convenient to the operator and control.
The utility model NaClO producer is provided with acid and irritates 5, can be used to the electrode in the electrolyzer 2 is carried out pickling, between electrolyzer 2 and acid filling 5, be provided with sour pump 13, the entrance end of acid pump 13 is irritated 5 perforations by pipeline 14 and acid and is connected, the exit end of acid pump 13 connects with electrolyzer 2 by pipeline 15 and is connected, offer some discharge tubes 16 in the side of electrolyzer 2, discharge tube 16 is connected with recovery channel 17, recovery channel 17 feeds acid and irritates in 5, forms the recycle system by above design and carries out pickling.
Row's hydrogen blower fan 23 that the hydrogen that produces when being provided with electrolysis at the top of electrolyzer 2 is discharged, on electrolyzer 2, be provided with the NaClO outlet, NaClO outlet and NaClO storage are respectively equipped with slow-motion pipeline 9 and F.F. pipeline 10 between irritating 4, on slow-motion pipeline 9, be provided with the slow-motion valve 11 of control slow-motion pipeline 9 flow velocitys, on F.F. pipeline 10, be provided with the F.F. valve 12 of control F.F. pipeline 10 flow velocitys, the NaClO solution of producing is conveyed into NaClO storage filling 4 by slow-motion pipeline 9 and F.F. pipeline 10 and stores, in NaClO storage filling 4, be provided with drug valve 27, in NaClO storage filling 4, also be provided with floating ball lever meter 26, be used for showing liquid level, be convenient to the operator and control.
Be contained with the NaCl solid in the dissolved salt device 3 of the present utility model, be provided with the riser tubing 18 that can mix NaCl solid and water at the top of dissolved salt device 3, the rear end of riser tubing 18 is connected with the entrance end of dissolved salt pump 19, the exit end of dissolved salt pump 19 is connected with dissolved salt device 3 by liquid-inlet pipe 20, stir valve 22 and dissolved salt valve 21 riser tubing 18 other being provided with, be used for stirring NaCl solid and water and make it mix generation NaCl solution.
Manufacturing to the utility model electrolyzer and electrode is described in detail below.
1, electrolyte tank (electrolyzer) is made---strengthen white PVC plate welding forming
The water pressure testing is filled with in casing voltage-withstand test---equipment normal pressure operation in the case, casing does not have distortion, leaks.
The test of casing heatproof---water filling is heated to 65 ℃ in the case, and constant temperature 6 hours, casing do not have distortion, leak.
Ageing-resistant test---uviolizing 48 hours, casing and model contrast nondiscoloration.
Corrosion-resistant---soak a week in 90% industrial sulphuric acid, surperficial luminosity is constant, and toughness of material is constant.
2, electrode adopts high-quality titanium plate (TA
1) the line cutting forming, thickness satisfies perveance (1A/mm2).
Pre-treatment: 1. surface finish, shot-peening is removed zone of oxidation.2. mixing acid soaks, boiled 2 hours, and surperficial greyish white inclusion-free, the clean water rinsing is dried stand-by.
Coating: compound masking liquid is by multiple dilute metal peculiar set-up, and pole plate is coated with 30 times, High Temperature Furnaces Heating Apparatus repeatedly the constant temperature sintering coating is closely contacted with pole plate, strong adhesion does not come off.
Install: electrode is vertically mounted in the electrolyzer, the tetrafluoro screw retention supports between the electrode, advance under the electrolytic solution, on go out, dominant discharge is passed through electrode district, logical direct current solution produces electrochemical reaction and produces thimerosal, and side reaction hydrogen is discharged outdoor by the dilution of row's hydrogen blower fan.
The concrete parameter of the every data of the utility model:
Show and described ultimate principle of the present utility model and principal character and advantage of the present utility model.The technician of the industry should understand; the utility model is not restricted to the described embodiments; that describes in the foregoing description and the specification sheets just illustrates principle of the present utility model; under the prerequisite that does not break away from the utility model spirit and scope; the utility model also has various changes and modifications, and these changes and improvements all fall in claimed the utility model scope.The claimed scope of the utility model is defined by appending claims and equivalent thereof.
Claims (9)
1. NaClO producer, comprise electrical control cubicles, electrolyzer, dissolved salt device and NaClO storage are irritated, it is characterized in that: described electrical control cubicles and electrolyzer are by being electrically connected, described electrolyzer shell adopts the Reinforced PVC material, be provided with electrolyzer in electrolyzer, described water is introduced electrolyzer and dissolved salt device by pipeline respectively;
Be provided with lift pump between dissolved salt device and electrolyzer, the entrance end of described lift pump connects with the dissolved salt device by pipeline and is connected, and the exit end of described lift pump connects with electrolyzer by pipeline and is connected;
Be provided with the NaClO outlet on electrolyzer, described NaClO outlet is irritated by pipe connection NaClO storage, irritates in the NaClO storage and is provided with the drug valve.
2. a kind of NaClO producer according to claim 1, it is characterized in that: also comprise the acid filling, between electrolyzer and acid filling, be provided with sour pump, the entrance end of described sour pump is irritated to connect by pipeline and acid and is connected, described sour pump outlet end connects with electrolyzer by pipeline and is connected, offer some discharge tubes in the side of electrolyzer, described discharge tube is connected with recovery channel, and described recovery channel feeds in the acid filling.
3. a kind of NaClO producer according to claim 2, it is characterized in that: be contained with the NaCl solid in the described dissolved salt device, be provided with the riser tubing that can mix NaCl solid and water at the top of dissolved salt device, the rear end of described riser tubing is connected with the entrance end of dissolved salt pump, described dissolved salt pump outlet end is connected with the dissolved salt device by liquid-inlet pipe, stirs valve and dissolved salt valve other being provided with of riser tubing.
4. a kind of NaClO producer according to claim 3 is characterized in that: the electrolysis cells in the described electrolyzer is made up of the compound electrode of multi-disc, and the material of described compound electrode is TA
1The titanium plate, described electrolyzer electrolyte inside is " S " annularly flow.
5. a kind of NaClO producer according to claim 4 is characterized in that: row's hydrogen blower fan that the hydrogen that produces when being provided with electrolysis at the top of electrolyzer is discharged.
6. a kind of NaClO producer according to claim 5 is characterized in that: be provided with high frequency switch power in the described electrical control cubicles.
7. a kind of NaClO producer according to claim 6, it is characterized in that: between the NaClO of electrolyzer outlet and NaClO storage filling, be respectively equipped with slow-motion pipeline and F.F. pipeline, described slow-motion pipeline is provided with the slow-motion valve of control slow-motion pipe flow speed, and described F.F. pipeline is provided with the F.F. valve of control F.F. pipe flow speed.
8. a kind of NaClO producer according to claim 7 is characterized in that: be provided with water washing device on the pipeline of water feeding electrolyzer.
9. a kind of NaClO producer according to claim 8 is characterized in that: be provided with magnetic turnover panel liquidometer on the dissolved salt device, irritate in the NaClO storage and be provided with floating ball lever meter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010202640758U CN201785505U (en) | 2010-07-19 | 2010-07-19 | NaCIO generator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010202640758U CN201785505U (en) | 2010-07-19 | 2010-07-19 | NaCIO generator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201785505U true CN201785505U (en) | 2011-04-06 |
Family
ID=43817479
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010202640758U Expired - Lifetime CN201785505U (en) | 2010-07-19 | 2010-07-19 | NaCIO generator |
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| Country | Link |
|---|---|
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Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102021602A (en) * | 2010-07-19 | 2011-04-20 | 江苏泽宇环境工程有限公司 | Sodium hypochlorite generator |
| CN102671226A (en) * | 2012-06-05 | 2012-09-19 | 张少微 | Multifunctional sterilizer |
| CN104975305A (en) * | 2014-04-03 | 2015-10-14 | 开物科技股份有限公司 | Hypochlorous acid water production system |
| CN105154909A (en) * | 2015-10-16 | 2015-12-16 | 苏州市铂瑞工业材料科技有限公司 | Sodium hypochlorite generator |
| CN106435640A (en) * | 2016-08-30 | 2017-02-22 | 江苏永冠给排水设备有限公司 | Improvement-based full-automatic sodium hypochlorite generator system and achieving method |
| CN106967996A (en) * | 2017-04-18 | 2017-07-21 | 碧海舟（北京）节能环保装备有限公司 | The hydrogen manufacturing of clean energy resource seawater and sodium hypochlorite system |
| CN108996623A (en) * | 2018-08-27 | 2018-12-14 | 江苏创新环境工程有限公司 | A kind of oil field reinjection water electrolytic sterilizing apparatus |
| CN109536987A (en) * | 2018-12-26 | 2019-03-29 | 九阳股份有限公司 | A kind of new structural electrolysis unit |
-
2010
- 2010-07-19 CN CN2010202640758U patent/CN201785505U/en not_active Expired - Lifetime
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102021602A (en) * | 2010-07-19 | 2011-04-20 | 江苏泽宇环境工程有限公司 | Sodium hypochlorite generator |
| CN102671226A (en) * | 2012-06-05 | 2012-09-19 | 张少微 | Multifunctional sterilizer |
| CN104975305A (en) * | 2014-04-03 | 2015-10-14 | 开物科技股份有限公司 | Hypochlorous acid water production system |
| CN105154909A (en) * | 2015-10-16 | 2015-12-16 | 苏州市铂瑞工业材料科技有限公司 | Sodium hypochlorite generator |
| CN106435640A (en) * | 2016-08-30 | 2017-02-22 | 江苏永冠给排水设备有限公司 | Improvement-based full-automatic sodium hypochlorite generator system and achieving method |
| CN106435640B (en) * | 2016-08-30 | 2017-10-13 | 江苏永冠给排水设备有限公司 | One kind is based on follow-on full-automatic hypochlorite generator's system and implementation method |
| CN106967996A (en) * | 2017-04-18 | 2017-07-21 | 碧海舟（北京）节能环保装备有限公司 | The hydrogen manufacturing of clean energy resource seawater and sodium hypochlorite system |
| CN108996623A (en) * | 2018-08-27 | 2018-12-14 | 江苏创新环境工程有限公司 | A kind of oil field reinjection water electrolytic sterilizing apparatus |
| CN109536987A (en) * | 2018-12-26 | 2019-03-29 | 九阳股份有限公司 | A kind of new structural electrolysis unit |
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