CN2581430Y - Subacid electrolytic sterilizing water producing device - Google Patents
Subacid electrolytic sterilizing water producing device Download PDFInfo
- Publication number
- CN2581430Y CN2581430Y CN 02244949 CN02244949U CN2581430Y CN 2581430 Y CN2581430 Y CN 2581430Y CN 02244949 CN02244949 CN 02244949 CN 02244949 U CN02244949 U CN 02244949U CN 2581430 Y CN2581430 Y CN 2581430Y
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- water
- hydrochloric acid
- transfer lime
- subacidity
- making device
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Abstract
The utility model provides a subacid electrolytic sterilizing water producing device which comprises a hydrochloric acid water storage tank, an electrolytic tank with a hydrochloric acid water inlet and an electrolyte outlet, a jet flow mixing pump which is respectively communicated with a raw water conveying pipe and the electrolyte outlet, and a sterilizing water diluent storage tank communicated with the outlet of the jet flow mixing pump, wherein the hydrochloric acid water inlet of the electrolytic tank is communicated with a hydrochloric acid water storage tank through a hydrochloric acid water conveying pipe. The utility model has the advantages of simple structure, low cost, long service life and convenient maintenance and can produce hypochlorous acid subacid pure water sterilizing liquid with a high efficient sterilizing function.
Description
Technical field:
The utility model relates to a kind of electrolytic sterilizing wetting system, particularly be a kind of subacidity electrolytic sterilizing water making device.
Background technology:
Along with the development in an all-round way of science and technology, the raising that people require quality of life, more and more higher to the requirement of sterilization and disinfection technology.People's chemosterilization sterilizing agent commonly used carries out sterilization and disinfection at present.Adopt the loss of this antibacterial disinfectant effective constituent big, unpleasant irritating smell is arranged, and residue is arranged, must carry out secondary cleaning after the sterilization on sterilization thing surface.
The utility model content:
The purpose of this utility model is in order to overcome above deficiency, to provide a kind of simple in structure, and expense is low, long service life, easy to maintenance, can produce the subacidity electrolytic sterilizing water making device of the little sour pure water disinfecting liquid of the hypochlorous acid with efficient sterilizing effect.
The purpose of this utility model is achieved like this:
The utility model device comprises subacidity electrolytic sterilizing water making device, it is characterized in that comprising the hydrochloric acid water storage tank, the electrolyzer of hydrochloric water inlet and electrolyte outlet, the jet mixing pump that is communicated with former water transfer lime and electrolyte outlet respectively, with the sterilization water diluent storage tank that the outlet of jet mixing pump is communicated with, electrolyzer hydrochloric acid water inlet is communicated with the hydrochloric acid water storage tank by salt sour water transfer lime.
In the above-mentioned electrolyzer cell body is arranged, be positioned at the multi-disc battery lead plate that a plurality of tetrafluoroethylene spacer rings of the intravital usefulness of electrolyzer separate and are parallel to each other, the fluid channel that is communicated with hydrochloric acid water inlet and electrolyte outlet respectively, outermost two plate electrode plates have the connection terminal that links to each other with the direct supply positive and negative electrode respectively relatively.
Between above-mentioned former water transfer lime and salt sour water transfer lime former moisture flow transfer lime is arranged.
On the above-mentioned former moisture flow transfer lime water pump, vacuum breaker are housed.
PH automatic tester with electronic gate valve is housed between above-mentioned mixing pump and sterilization water diluent storage tank.
Strainer is housed, stopping valve, constant flow rate valve on the above-mentioned former water transfer lime.
On the above-mentioned former water transfer lime vacuum breaker is housed.
The hydrochloric acid volume pump is housed, vacuum breaker on the above-mentioned salt sour water transfer lime.
Above-mentioned sterilization water storage tank upper and lower part is equipped with gas blower, vent valve, water level upper and lower detector switch, stopping valve respectively.
Referring to Fig. 1～Fig. 6, during the utility model work, the hydrochloric acid that the hydrochloric acid volume pump will have finite concentration (as 3% or 21%) pumps into hydrochloric acid to electrolyzer continuously with certain flow rate (as 0.15L/h) flow from the hydrochloric acid water storage tank, pass to electric current (as 1.25A or 3A) to electrolyzer simultaneously, the direct current of voltage (as 8.4V or 16V) carries out electrolysis to hydrochloric acid, electrolytic solution enters dilution jet mixing pump by delivery pipe and dilutes, open former water stopping valve then, allow former water pass through constant flow rate valve, flow (as 240L/h or 1200L/h) enters the jet mixing pump in accordance with regulations, the electrolytic solution that electrolyzer is given off dilutes, can obtain the sterilization water of pH=4.5～7 continuously, throughput can reach 240L/h or 1200L/h, and the cl concn that contains of sterilization water can be 10～20ppm.Can produce the various sterilization water that contain cl concn as required.Should regularly detect sterilization water pH value in the production process, regularly detect sterilization water effective concentration.Maybe can be equipped with pH detection paper pH value with automatic pH meter.Cl concn detects by iodimetry.
The not too big working space of sterilization such as family, restaurant water consumption preferably modulates concentration of hydrochloric acid in advance.Because the salt sour water does not need redilution and directly injects electrolyzer and carry out electrolysis, therefore, be mixed with volumetric molar concentration in advance is the salt sour water of 0.05～0.2mol/L.Electrolysis energy consumption is few in this scope, and sterilization effects is also better after the electrolysis.
As big places of sterilization water consumption such as food processing plant, Soft Drinks Plant, hospital, waterworks, swimming pools, when adopting this device production sterilization water, raw material hydrochloric acid is prefabricated to be 6.0mol/L concentration salt sour water or directly use market hydrochloric acid (food additive hydrochloric acid 34.46%), become the salt sour water of 0.001～1mol/L to enter electrolyzer by the automatically adding device thin up and carry out electrolysis, then electrolytic solution is added the sterilization water that the jet mixing pump is mixed with required various concentration, output is big, sterilization effect good.
The utility model is simple in structure, expense is low, long service life, easy to maintenance.The utility model is owing to adopt food additive hydrochloric acid and ortho-water as raw material, the sterilization water of producing does not have niff, dry back does not have surplus thing, therefore is specially adapted to food, and the disinfection of the pipeline of industries such as pharmacy, packaging facilities and various containers etc. is handled.
Description of drawings:
Fig. 1 is the utility model structural representation.
Fig. 2 is a cell construction synoptic diagram among Fig. 1.
Fig. 3 is the left view of Fig. 2.
Fig. 4 is another structural representation of the utility model.
Fig. 5 is a cell construction synoptic diagram among Fig. 4.
Fig. 6 is the left view of Fig. 5.
Embodiment:
Embodiment 1:
Fig. 1～Fig. 3 has provided the utility model embodiment 1 figure.The capacity of polyethylene hydrochloric acid water storage tank 1 is 2L, and the concentration that stores preparation in advance is 2.8% dilute hydrochloric acid.Discharge capacity 0.150L/h is arranged, the ZJ1-0.2/20 hydrochloric acid volume pump 3 of power 90W, vacuum breaker 51 on the hydrochloric acid transfer lime 2.Cell body in the electrolyzer 4 adopts tetrafluoroethylene (or polyethylene) to make, the hydrochloric acid water inlet 5 that is communicated with hydrochloric acid transfer lime 2 is arranged on it, electrolyte outlet 6, the fluid channel 7 that is communicated with hydrochloric acid water inlet and electrolyte outlet, the five titanium net platinized electrode plates 8 that are parallel to each other that separate with a plurality of tetrafluoroethylene spacer rings 52.Battery lead plate monolithic effective surface area 0.25dm
2, battery lead plate spacing 3mm, bath voltage 8.4V, cell current 1.25A, battery lead plate spacing voltage is equivalent to 2.1V, and natural rubber sealing-ring 9 is arranged in the electrolyzer.Relative outermost two plate electrode plates 10,11 are respectively the electrode of band connection terminal, and 12V is adjustable with output voltage, and the direct supply 12 of electric current 1.25A is communicated with.Be the minimizing cathode deposition, but this power supply timing reversing. be connected with raw water filtration device 14 successively on the former water transfer lime 13 of stainless steel, stopping valve 53, dilution constant flow rate valve 15, vacuum breaker 16.φ 8 fluid orifices are arranged, φ 4 electrolytic solution imports, outlet on the electrolytic solution jet mixing pump 17.Electrolyte outlet on the electrolyzer is communicated with the jet mixing pump by pipeline.Sterilization water diluent storage tank 18 is communicated with the jet mixing pump.This sterilization water diluent tankage 500L makes with stainless steel or vinyon.Which is provided with vent valve 19, gas blower 20, water level upper and lower limit detector switch 21,22, water intaking stopping valve 23.
Embodiment 2:
Fig. 4～Fig. 6 has provided the utility model embodiment 1 figure.The capacity of polyethylene hydrochloric acid tank 24 is 2L, and the concentration that stores preparation in advance is 21% dilute hydrochloric acid.Discharge capacity 0.2L/h is arranged, the ZJ1-0.2/20 hydrochloric acid volume pump 26 of power 90W, vacuum breaker 54 on the hydrochloric acid transfer lime 25.Cell body in the electrolyzer 27 adopts tetrafluoroethylene (or polyethylene) to make, and the hydrochloric acid water inlet 55 that is communicated with hydrochloric acid transfer lime 25 is arranged, electrolyte outlet 56, the fluid passage 28 that is communicated with hydrochloric acid water inlet and electrolyte outlet on it.The eight titanium net platinized electrode plates 30 that are parallel to each other that separate with a plurality of tetrafluoroethylene spacer rings 29.Battery lead plate monolithic effective surface area 0.75dm
2, battery lead plate spacing 3mm, bath voltage 16V, cell current 3A, voltage is equivalent to 2.28V between battery lead plate, and electrolyzer seals with natural rubber sealing-ring 31.Relative outermost two plate electrode plates 32,33 are the electrode of band connection terminal.16V is adjustable with output voltage, and the direct supply 34 of electric current 3A is communicated with.Be the minimizing cathode deposition, but this power supply timing reversing.Be connected with raw water filtration device 35 successively on the former water transfer lime 50 of stainless steel, electric gate valve 36, dilution water constant flow rate valve 37.φ 10 fluid orifices are arranged, φ 6 electrolytic solution imports, outlet on the electrolytic solution jet mixing pump 38.Electrolyte outlet on the electrolyzer is communicated with the jet mixing pump by pipeline.Sterilization water diluent storage tank 39 is communicated with the jet mixing pump.This sterilization water diluent tankage 1000L makes with stainless steel or vinyon.Which is provided with vent valve 40, gas blower 41, water level upper and lower limit detector switch 42,43, water intaking stopping valve 44.The automatic pH value detector 46 of band self-locking magnetic valve 45 is housed on the pipeline between mixing pump and sterilization water diluent storage tank.Between former water transfer lime and salt sour water transfer lime, former moisture flow transfer lime 47 is arranged.Water pump 48, vacuum breaker 49 are housed on the former moisture flow transfer lime.
Claims (9)
1, subacidity electrolytic sterilizing water making device, it is characterized in that comprising the hydrochloric acid water storage tank, the electrolyzer of hydrochloric water inlet and electrolyte outlet, the jet mixing pump that is communicated with former water transfer lime and electrolyte outlet respectively, with the sterilization water diluent storage tank that the outlet of jet mixing pump is communicated with, electrolyzer hydrochloric acid water inlet is communicated with the hydrochloric acid water storage tank by salt sour water transfer lime.
2, subacidity electrolytic sterilizing water making device according to claim 1, it is characterized in that cell body is arranged in the electrolyzer, be positioned at the multi-disc battery lead plate that a plurality of tetrafluoroethylene spacer rings of the intravital usefulness of electrolyzer separate and are parallel to each other, the fluid channel that is communicated with hydrochloric acid water inlet and electrolyte outlet respectively, outermost two plate electrode plates have the connection terminal that links to each other with the direct supply positive and negative electrode respectively relatively.
3, subacidity electrolytic sterilizing water making device according to claim 1 and 2 is characterized in that between former water transfer lime and salt sour water transfer lime former moisture flow transfer lime being arranged.
4, subacidity electrolytic sterilizing water making device according to claim 3 is characterized in that on the former moisture flow transfer lime water pump, vacuum breaker being housed.
5, subacidity electrolytic sterilizing water making device according to claim 3 is characterized in that being equipped with the pH automatic tester with electronic gate valve between mixing pump and sterilization water diluent storage tank.
6, subacidity electrolytic sterilizing water making device according to claim 1 and 2 is characterized in that on the former water transfer lime strainer being housed, stopping valve, constant flow rate valve.
7, subacidity electrolytic sterilizing water making device according to claim 6 is characterized in that on the former water transfer lime vacuum breaker being housed.
8, subacidity electrolytic sterilizing water making device according to claim 1 and 2 is characterized in that the hydrochloric acid volume pump being housed, vacuum breaker on the salt sour water transfer lime.
9, subacidity electrolytic sterilizing water making device according to claim 1 and 2 is characterized in that sterilization water storage tank upper and lower part is equipped with gas blower, vent valve, water level upper and lower detector switch, stopping valve respectively.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 02244949 CN2581430Y (en) | 2002-11-29 | 2002-11-29 | Subacid electrolytic sterilizing water producing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 02244949 CN2581430Y (en) | 2002-11-29 | 2002-11-29 | Subacid electrolytic sterilizing water producing device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2581430Y true CN2581430Y (en) | 2003-10-22 |
Family
ID=33716704
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 02244949 Expired - Fee Related CN2581430Y (en) | 2002-11-29 | 2002-11-29 | Subacid electrolytic sterilizing water producing device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2581430Y (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101223885B (en) * | 2008-02-01 | 2011-08-24 | 中国农业大学 | Micro electrolysis disinfecting preparation and preparing method thereof |
| CN101899672B (en) * | 2009-05-25 | 2012-02-15 | 官有文 | Electrolytic system for preparing hypochlorous acid water |
| CN102732907A (en) * | 2011-04-08 | 2012-10-17 | 黄肇铭 | Method for producing electrolyzed water |
| CN104856867A (en) * | 2015-05-05 | 2015-08-26 | 韩永俊 | Subacidity oxidation electric potential water treatment apparatus |
| CN107099813A (en) * | 2017-05-18 | 2017-08-29 | 蔡合旺事业股份有限公司 | Hypochloric acid water prepares supply equipment |
| CN109423661A (en) * | 2017-09-04 | 2019-03-05 | 株式会社北越 | High concentration subacidity electrolysis water generation method and device |
-
2002
- 2002-11-29 CN CN 02244949 patent/CN2581430Y/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101223885B (en) * | 2008-02-01 | 2011-08-24 | 中国农业大学 | Micro electrolysis disinfecting preparation and preparing method thereof |
| CN101899672B (en) * | 2009-05-25 | 2012-02-15 | 官有文 | Electrolytic system for preparing hypochlorous acid water |
| CN102732907A (en) * | 2011-04-08 | 2012-10-17 | 黄肇铭 | Method for producing electrolyzed water |
| CN102732907B (en) * | 2011-04-08 | 2015-01-14 | 黄肇铭 | Method for producing electrolyzed water |
| CN104856867A (en) * | 2015-05-05 | 2015-08-26 | 韩永俊 | Subacidity oxidation electric potential water treatment apparatus |
| CN107099813A (en) * | 2017-05-18 | 2017-08-29 | 蔡合旺事业股份有限公司 | Hypochloric acid water prepares supply equipment |
| CN109423661A (en) * | 2017-09-04 | 2019-03-05 | 株式会社北越 | High concentration subacidity electrolysis water generation method and device |
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Legal Events
| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |