CN101077800A - Modified fully automatic high oxidation electric potential sterilized water generator - Google Patents
Modified fully automatic high oxidation electric potential sterilized water generator Download PDFInfo
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- CN101077800A CN101077800A CN 200610029595 CN200610029595A CN101077800A CN 101077800 A CN101077800 A CN 101077800A CN 200610029595 CN200610029595 CN 200610029595 CN 200610029595 A CN200610029595 A CN 200610029595A CN 101077800 A CN101077800 A CN 101077800A
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- sterilized water
- electrolysis
- high oxidation
- water
- electric potential
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Abstract
The automatic high oxidation potential sterilized water producing machine has two identical intermittent electrolytic cells to produce sterilized water alternately, and the water inlet time and the water outlet time are superposed with the electrolysis time to increase the yield of sterilized water greatly. The electrolysis time is regulated with the fixed salt adding concentration so as to obtain required ORP value, and this simplifies the control.
Description
Affiliated field: the present invention is with the equipment of electrolytic process generation high oxidation electric potential sterilized water, belongs to the sterilizing agent production unit.
Background technology: the fully automatic high oxidation electric potential sterilized water generator of ZL01210497.3 patent, with ORP feedback control sterilized water quality.Its control techniques is complicated and be out of order easily, also has single electrolyzer output not high.
The purpose of invention: the machine of fully automatic high oxidation electric potential sterilized water generator of the present invention and ZL01210497.3 is similar, equally by water inlet, outlet system, electrolytic system, Controlling System and power supply are formed, but adopt two identical intermittent electrolyzers, electrolysis in turn, and only use a power supply and Controlling System, increased the output of sterilized water, change the ORP value with fixedly adding salt concn change electrolysis time, control is simplified and the easier assurance of quality.
Technical scheme: foregoing invention can realize with the system of Fig. 1.
Symbol 1, volume pump 2, brine tank 3, V1 4, electrolyzer 5, V26, v3 7, V4 8, tap water water inlet pipe 9, V5 10, sterilization tank 11, ORP transmitter 12, wastewater discharge pipe 13, L1 14, L2 15, L316, power supply among the figure
V1, V3, V4, V5 are normally closed solenoid valve
L1, L2, L3 are liquid level switch
Do not mark among the valve of second electrolyzer and the liquid level switch figure, Wen Zhongru quotes and adds ", ", and as V4 ', L3 ' etc., both are chain mutually, can not open simultaneously.
Intermittent type electrolyzer 4, it is middle that the left side is an anode by the separation of micropore ceramics barrier film, the right is a negative electrode.Water intaking valve V4 and add brine valve V1 all in anode side, tap water and salt solution are mixed and go into cathode side through the barrier film overflow, and liquid level switch L3 control liquid level, touches when leading to V4, V1 are closed.The anode rising pipe of electrolyzer flows into sterilization tank 10 through V3.Two liquid level switch L2 and L1 are housed up and down, to guarantee that liquid level remains between L1 and the L2 in the groove on the groove.The ORP transmitter is used for showing sterilized water on panel ORP value also is housed in the groove.The negative electrode water outlet is a strong lye, through the V5 discharging, but also can collect utilization.
Power supply 16 will have two dc output ends behind the AC rectification, be connected to two electrolyzers respectively, and power supply is equipped with shifter, disconnected/exchange device and device of falling the utmost point.
The negative plate surface can be polluted in the electrolytic process, needs after work for some time to clean with the method for falling the utmost point.Waste discharge is all wanted in the two poles of the earth water outlet during cleaning, so cathode side also is provided with wash water valve V2.Controlling System can adopt programmable controller, realizes full automatic control.The program that adopts is as follows:
First electrolyzer 1, V4, V1 open, volume pump 1 is opened, and close after importing quantitative salt solution.L3 touches logical V4, V1 and closes water inlet end.(required time t1).
2, direct current is logical, switches after electrolysis t2 minute, and electrolysis finishes.
3, V3, V5 open after t3 minute and close, and water outlet finishes.
4, reciprocation cycle 1-3.
Second electrolyzer is when first electrolytic tank electrolysis, elder generation's water outlet, water inlet again, because t1+t3＜t2, water outlet and water inlet process can be finished in electrolysis time, water, electrolysis and water outlet are advanced in two continuous one after the others of electrolyzer of event and first electrolyzer one after the other circulation is carried out.
Follow also the electrolysis production sterilized water and touch logically up to the last liquid level switch L2 of sterilization tank, direct supply disconnects, the termination cyclic electrolysis.Take sterilized water and touch logically when liquid level is reduced to play liquid level switch L1, direct supply is connected again, recovers cyclic electrolysis, and supreme liquid level switch L2 touches once again when leading to and stops.
The cleaning electrode program is as follows: (this program starts when next)
1, the direct supply utmost point
2, V4 opens L3 and touches V4 pass, logical back
3, switch behind the logical first electrolytic tank electrolysis t4 of power supply.V2 ' V5 ' closes after opening t3 when electrolysis begins, and V4 ' opens L3 ' and touches pass, logical back then
4, second electrolyzer begins behind the electrolysis t4 the utmost point, switching, pass.Electrolytic while V2, V5 close after opening t3 in beginning
5, V2 ' V5 ' closes after opening t3
6, general supply is closed
Illustrate: do not add salt solution during cleaning electrode
Embodiment:
By equipment shown in Figure 1.The volume of electrolyzer is 20 liters, and the volts DS of power supply is 190V.Flooding time is 1 minute and 20 seconds in the equipment debugging process.The water outlet time is 2 minutes and 30 seconds, and electrolysis time is 4 minutes, and adding salt concn is 0.1%.The sterilized water ORP that obtains is+1170mv.Aquifer yield is per hour 150 liters.Liquid level is 100 liters on the sterilization tank.Following liquid level is 60 liters.By high oxidation electric potential sterilized water when ORP＞+1000mv just can 100% kills all microorganisms, so the sterilized water quality that the control techniques that the present invention need not complexity obtains is guaranteed equally.
Claims (4)
1, a kind of high oxidation electric potential sterilized water of being made up of water inlet, outlet system, electrolytic system, Controlling System and power supply generates machine, it is characterized in that electrolytic system is made up of two identical intermittent electrolyzers.
2,, it is characterized in that two electrolyzers are with the electrolysis that continues in turn of same power supply and Controlling System by the described sterilization hydrogenesis machine of claim 1.
3, by the described sterilization hydrogenesis machine of claim 1, it is characterized in that an electrolyzer when electrolysis another electrolyzer then in water outlet and water inlet.
4,, it is characterized in that adding that salt concn is constant changes the ORP value with the change electrolysis time by the described sterilization hydrogenesis machine of claim 1.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006100295959A CN100540747C (en) | 2006-08-01 | 2006-08-01 | The modified version fully automatic high oxidation electric potential sterilized water generator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006100295959A CN100540747C (en) | 2006-08-01 | 2006-08-01 | The modified version fully automatic high oxidation electric potential sterilized water generator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101077800A true CN101077800A (en) | 2007-11-28 |
| CN100540747C CN100540747C (en) | 2009-09-16 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2006100295959A Expired - Fee Related CN100540747C (en) | 2006-08-01 | 2006-08-01 | The modified version fully automatic high oxidation electric potential sterilized water generator |
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| CN (1) | CN100540747C (en) |
Cited By (4)
| 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 |
| CN104118923A (en) * | 2013-04-26 | 2014-10-29 | 上海高创医疗科技有限公司 | Device for preparation of redox potential water by use of ceramic body as ion exchange interval |
| CN105165890A (en) * | 2015-09-20 | 2015-12-23 | 连云港龙卷风环保技术有限公司 | Disinfectant fluid and preparation method and device thereof |
| CN107119284A (en) * | 2017-06-27 | 2017-09-01 | 中国灌溉排水发展中心 | A kind of batch (-type) electrolyzes table salt hypochlorite generator |
-
2006
- 2006-08-01 CN CNB2006100295959A patent/CN100540747C/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104118923A (en) * | 2013-04-26 | 2014-10-29 | 上海高创医疗科技有限公司 | Device for preparation of redox potential water by use of ceramic body as ion exchange interval |
| CN103241808A (en) * | 2013-05-28 | 2013-08-14 | 顾宗义 | Complete plant for producing high oxidation potential disinfectant |
| CN105165890A (en) * | 2015-09-20 | 2015-12-23 | 连云港龙卷风环保技术有限公司 | Disinfectant fluid and preparation method and device thereof |
| CN107119284A (en) * | 2017-06-27 | 2017-09-01 | 中国灌溉排水发展中心 | A kind of batch (-type) electrolyzes table salt hypochlorite generator |
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| Publication number | Publication date |
|---|---|
| CN100540747C (en) | 2009-09-16 |
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Effective date of registration: 20080111 Address after: Three hundred and ten thousand and twenty-seven Environmental Engineering Research Institute, Yuquan campus, Zhejiang University, 38 Zhejiang Road, Zhejiang, Hangzhou, Postal Code: 310027 Applicant after: Zhejiang University Address before: Room 3, No. 105, Lane 401, Jiangsu North Road, Shanghai, China Applicant before: Gu Zongyi |
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Granted publication date: 20090916 Termination date: 20120801 |