CN2839256Y - Oxidation potential water generator - Google Patents
Oxidation potential water generator Download PDFInfo
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- CN2839256Y CN2839256Y CN 200520121929 CN200520121929U CN2839256Y CN 2839256 Y CN2839256 Y CN 2839256Y CN 200520121929 CN200520121929 CN 200520121929 CN 200520121929 U CN200520121929 U CN 200520121929U CN 2839256 Y CN2839256 Y CN 2839256Y
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- water
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- electrolyte quota
- outlet
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Abstract
The utility model relates to an oxidation potential water generator, which comprises an electrolytic chamber, wherein the electrolytic chamber is provided with an inlet for electrolytic solution, an outlet for acidic water and an outlet for alkaline water; the inlet for the electrolytic solution of the electrolytic chamber is connected with an outlet of a mixer; an inlet of the mixer is connected with a preparing supply device for the electrolytic solution. The utility model has the advantages that the structure for tap water changed into oxidation potential water and output is simple, the reliability is high, the type of the oxidation potential water generator is designed to be small, and the manufacturing cost is largely reduced; due to the use of the mixer, the electrolytic solution is uniformly mixed, and thus, the quality of the oxidation potential water is effectively ensured.
Description
Technical field
The utility model relates to a kind of oxidizing potential water generator, relates in particular to a kind of automatic oxidizing potential water generator of even mixed salt in proportion.The utility model is also referred to as oxidizing potential Water generator or strong acidic electrolyzed water producer.
Background technology
The electrolyte quota feedway of existing oxidizing potential water generator is very complicated, and volume is big, can not regulate the saltiness of electrolytic solution automatically; Do not have the electrolytic solution mixing tank in addition, can not fully electrolytic solution be mixed, thereby influence amount of electrolyte.
Summary of the invention
The purpose of this utility model provides a kind of oxidizing potential water generator, and to solve the complex structure that prior art exists, volume is big, can not regulate the saltiness of electrolytic solution automatically, can not fully electrolytic solution be mixed and influences the problem of amount of electrolyte.
The technical solution of the utility model is: comprise tank room, be provided with electrolyte entrance, sour water outlet and alkaline water outlet at this tank room, the electrolyte entrance of described tank room is connected with the outlet of a mixing tank, and the inlet of this mixing tank is connected with the electrolyte quota feedway.
Described mixing tank comprises jet-pump, mixes water drum and last lower baffle plate, and the upper end of mixing water drum is provided with water outlet, and last lower baffle plate is horizontally installed on the top and the bottom of mixing in the water drum respectively, is respectively equipped with the mouth of a river and water hole on this on the lower baffle plate; The water jet of jet-pump is connected the bottom of described mixed water drum, and the water inlet of jet-pump is connected with the electrolyte outlet of described tap water joint and electrolyte quota feedway respectively with suction port.
Described electrolyte quota feedway comprises saturated salt solution preparation case and electrolyte quota case, saturated salt solution preparation case is provided with the parallel-series of tap water joint valve, in saturated salt solution preparation case, be provided with agitator, be connected with throttling valve by placed in-line water pump between saturated salt solution preparation case and the electrolyte quota case; The inlet of electrolyte quota case is connected with described tap water joint with placed in-line valve by pipeline, and the outlet of electrolyte quota case is connected with the suction port of described mixing tank by pipeline; Between the water-in of described tap water joint and mixing tank, be connected with placed in-line reducing valve, valve by pipeline.
Valve between described tap water joint and saturated salt solution preparation case, electrolyte quota case and the mixing tank is magnetic valve; Sour water outlet at described tank room is connected with sensing chamber, the signal output part of this sensing chamber is connected with the input terminus of a controller, the different output terminals of this controller respectively with described each magnetic valve, and be connected described saturated salt solution preparation case and be connected with water pump between the electrolyte quota case.
Top in described electrolyte quota case is provided with electrolytic bath, and the bottom in the electrolyte quota case is equipped with water pump and the electrolytic solution in the case is extracted in the electrolytic bath on top; This electrolytic bath is connected with the jet pump intake of described mixing tank by pipeline.
Compared with the prior art, the utility model has the advantages that: it is simple to enter into the electrolyzed oxidizing water export structure by tap water, and the reliability height can be the miniaturization of type design, and manufacturing cost also reduces significantly; Owing to used mixing tank electrolytic solution to be mixed uniformly, thereby effectively guaranteed the quality of electrolyzed oxidizing water.
Description of drawings
Fig. 1 is an overall formation synoptic diagram of the present utility model;
Fig. 2 is the structural representation (being the B-B sectional view of Fig. 3) of mixing tank of the present utility model;
Fig. 3 is the A-A sectional view of Fig. 2.
Embodiment
Referring to Fig. 1～Fig. 3, structure of the present utility model and working process are as follows: tap water enters this machine by tap water joint 1, prepare case 12 water fillings by magnetic valve 3 to saturated salt, artificial simultaneously toward the saturated salt preparation case 12 interior salt (NaCl) that add q.s, make it to become the saturated solution of salt, water pump 11 as agitator with the solution that quickens salt and saturated.By shut off valve 14 quantitative dispensing in the electrolyte quota case 9 under the control of automatic control system, tap water makes it to become by magnetic valve 13 conveying in the electrolyte quota case 9 and contains a certain proportion of salt solution electrolytic solution water pump 10 with the saturated solution of salt.Opens solenoid valve 4 in the time will carrying out electrolysis, tap water i.e. the water-in 50 of the injecting mixer 5 by reducing valve 2 constant currents, the suction port 57 of the jet-pump 58 of mixing tank 5 (promptly inhaling salt chews) draw automatically in the electrolyte quota case 9 electrolytic solution and with the tap water uniform mixing after be sent to diaphragm electrolysis chamber 6 and carried out electrolysis.Electrolytic solution becomes acidic oxidized electric potential water and alkaline oxygenated current potential water after the electrolysis in tank room 6, and obtain from sour water outlet 15 and alkaline water outlet 16 respectively.For the quality that guarantees acidic oxidized electric potential water is provided with sensing chamber 7 on the pipeline of sour water water outlet, necessary ion electrode (ORP electrode, PH electrode, chlorine ion electrode all can) is installed in the sensing chamber, this ion electrode is connected with controller C, the latter carries out closed-loop control according to detected data to water pump 10, and shows the corresponding data that detects.Top in described electrolyte quota case 9 is provided with electrolytic bath 91, and the bottom in the electrolyte quota case is equipped with water pump 8 electrolytic solution in the case is extracted in the electrolytic bath 91 on top.This electrolytic bath 91 is connected with the jet pump intake 57 of described mixing tank 5 by pipeline 17.
Described Controlling System comprises that controller C (can adopt micro-chip or PLC) and input and output unit thereof form, and wherein input block has: the water level sensor up and down in switch key (not shown), saturated solution preparation case 12 and the electrolyte quota case 9 and the redox potential detector of the sour water in the sensing chamber 7; Output unit has: described in the equipment each magnetic valve, water pump and electrolysis power.Its control process is: by the work of switch key Controlling System with stop, be input among the controller C by the detected redox potential of the redox potential detector of sour water, by it electrolysis power is carried out closed-loop control, simultaneously the detected redox potential of detector is carried out numeral and show.The signal that is input among the controller C by the water level sensor up and down in saturated solution preparation case 12 and the electrolyte quota case 9 takes water level situation and electromagnetic valve of instruction make up water and salt in analysis and judgement control saturated solution preparation case and the electrolyte quota case by it.Realize the whole control process automatizations of this machine thus.
Referring to Fig. 2 and Fig. 3, the structure of mixing tank 5 of the present utility model comprises jet-pump 58, mixes water drum 52, overhead gage 53 and lower baffle plate 54, the upper end of mixing water drum 52 is provided with water outlet 51, last lower baffle plate is horizontally installed on the top and the bottom of mixing in the water drum respectively, be provided with the mouth of a river 55 at overhead gage 53, be provided with water hole 56 at lower baffle plate 54; The water jet 59 of jet-pump 58 is connected the bottom of described mixed water drum 52.When work, tap water is at first chewed 57 suction electrolytic solution through jet-pump 58 by inhaling salt by water-in 50, tap water and electrolytic solution are together by water jet 59 ejections, the mixed electrolytic solution of ejection is along the inwall rotation that mixes water drum 52, center water hole 56 ejections by lower baffle plate 54 enter epicoele along the mouth of a river 55 of crossing of overhead gage again, at this moment, tap water and electrolytic solution have mixed by water outlet 51 outflows and have had a certain proportion of electrolytic solution, electrolysis chamber electrolytic oxidation current potential water uniformly.
Function of the present utility model and purposes are: the oxidizing potential water generator is to do raw material with ordinary tap water to carry out electrolysis by the tank room that has ionic membrane, and the water decomposition after the electrolysis is that acidic oxidized electric potential water is that sour water and alkaline oxygenated current potential water are alkaline water.When the pH value of sour water less than 2.7, available chlorine content is greater than 20mg/kg
2The time this glassware for drinking water very strong germicidal action is arranged, can be used for doing medicine equipment and medical space, medical worker's sterilization and the sterilization of catering industry, gourd, fruit and vegetable etc.The washing that can be used for various article greater than 11 time when the pH value of alkaline water has the effect of very strong degreasing.
Claims (5)
1. oxidizing potential water generator, comprise tank room, be provided with electrolyte entrance, sour water outlet and alkaline water outlet at this tank room, it is characterized in that: the electrolyte entrance of described tank room is connected with the outlet of a mixing tank, and the inlet of this mixing tank is connected with the electrolyte quota feedway.
2. oxidizing potential water generator according to claim 1, it is characterized in that: described mixing tank comprises jet-pump, mixes water drum and last lower baffle plate, the upper end of mixing water drum is provided with water outlet, last lower baffle plate is horizontally installed on the top and the bottom of mixing in the water drum respectively, is respectively equipped with the mouth of a river and water hole on this on the lower baffle plate; The water jet of jet-pump is connected the bottom of described mixed water drum, and the water inlet of jet-pump is connected with the electrolyte outlet of described tap water joint and electrolyte quota feedway respectively with suction port.
3. oxidizing potential water generator according to claim 1, it is characterized in that: described electrolyte quota feedway comprises saturated salt solution preparation case and electrolyte quota case, saturated salt solution preparation case is provided with the parallel-series of tap water joint valve, in saturated salt solution preparation case, be provided with agitator, be connected with throttling valve by placed in-line water pump between saturated salt solution preparation case and the electrolyte quota case; The inlet of electrolyte quota case is connected with described tap water joint with placed in-line valve by pipeline, and the outlet of electrolyte quota case is connected with the suction port of described mixing tank by pipeline; Between the water-in of described tap water joint and mixing tank, be connected with placed in-line reducing valve, valve by pipeline.
4. oxidizing potential water generator according to claim 3 is characterized in that: the valve between described tap water joint and saturated salt solution preparation case, electrolyte quota case and the mixing tank is magnetic valve; Sour water outlet at described tank room is connected with sensing chamber, the signal output part of this sensing chamber is connected with the input terminus of a controller, the different output terminals of this controller respectively with described each magnetic valve, and be connected described saturated salt solution preparation case and be connected with water pump between the electrolyte quota case.
5. according to claim 2 or 3 described oxidizing potential water generators, it is characterized in that: the top in described electrolyte quota case is provided with electrolytic bath, and the bottom in the electrolyte quota case is equipped with water pump and the electrolytic solution in the case is extracted in the electrolytic bath on top; This electrolytic bath is connected with the jet pump intake of described mixing tank by pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200520121929 CN2839256Y (en) | 2005-09-22 | 2005-09-22 | Oxidation potential water generator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200520121929 CN2839256Y (en) | 2005-09-22 | 2005-09-22 | Oxidation potential water generator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2839256Y true CN2839256Y (en) | 2006-11-22 |
Family
ID=37427241
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200520121929 Expired - Fee Related CN2839256Y (en) | 2005-09-22 | 2005-09-22 | Oxidation potential water generator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2839256Y (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103241808A (en) * | 2013-05-28 | 2013-08-14 | 顾宗义 | Complete plant for producing high oxidation potential disinfectant |
| CN104591346A (en) * | 2015-01-07 | 2015-05-06 | 成都邦研科技有限公司 | Intelligent control acidic oxidation potential water generator |
| CN105129922A (en) * | 2015-09-07 | 2015-12-09 | 太仓文广汇清洁设备有限公司 | Well water electrolysis device |
-
2005
- 2005-09-22 CN CN 200520121929 patent/CN2839256Y/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103241808A (en) * | 2013-05-28 | 2013-08-14 | 顾宗义 | Complete plant for producing high oxidation potential disinfectant |
| CN104591346A (en) * | 2015-01-07 | 2015-05-06 | 成都邦研科技有限公司 | Intelligent control acidic oxidation potential water generator |
| CN105129922A (en) * | 2015-09-07 | 2015-12-09 | 太仓文广汇清洁设备有限公司 | Well water electrolysis device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20061122 Termination date: 20110922 |