CN206219283U - Produce the device of subacidity electrolysis water - Google Patents
Produce the device of subacidity electrolysis water Download PDFInfo
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- CN206219283U CN206219283U CN201621289141.0U CN201621289141U CN206219283U CN 206219283 U CN206219283 U CN 206219283U CN 201621289141 U CN201621289141 U CN 201621289141U CN 206219283 U CN206219283 U CN 206219283U
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- anode
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- electrolysis water
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- subacidity electrolysis
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Abstract
The utility model is related to a kind of device for producing subacidity electrolysis water, belongs to water-treatment technology field.Described device includes being divided into by barrier film the electrolytic cell body of anode chamber and cathode chamber, barrier film is fixed by dividing plate, anode is set in anode chamber, negative electrode is set in cathode chamber, anode and negative electrode are connected with power supply respectively by wire, cathode chamber top sets negative electrode chamber inlet, cathode chamber bottom sets buck outlet, buck outlet is connected with buck branch line, buck regulating valve is set on buck branch line, ratio adjusting valve is set on dividing plate, through separator bottom, upper portion of anode chamber sets anode compartment outlet, anode compartment outlet is connected with subacidity electrolysis water branch line, product water regulating valve is set on subacidity electrolysis water branch line.Using sodium-chloride water solution as electrolyzer, transport preserves easy to use the utility model.
Description
Technical field
The utility model is related to a kind of device for producing subacidity electrolysis water, belongs to water-treatment technology field.
Background technology
Traditional subacidity electrolysis water generating principle is：After the softened treatment of running water, (NaCl is referred to as to add electrolyzer
" salt " and Determining Micro Acid) it is electrolysed in the electrolytic cell without ion diaphragm, subacidity of the generation containing hypochlorous acid molecule (HClO) is electrolysed
Aqueous disinfectant.
Running water and electrolyzer [NaCl and Determining Micro Acid (hydrochloric acid)] enter after uniformly mixing in a mixer by a certain percentage
Diaphragm-free electrolysis room, under weak electric field effect, there is electrochemical reaction in yin, yang the two poles of the earth, and water occurs electrolysis and generated in anode
Chlorine, generation chlorine-containing compound, active oxygen, the aqueous solution of hydrogen peroxide, the sterilization with instantaneous, wide spectrum, efficient, noresidue is special
Property.
But, one of electrolyzer that this method is used hydrochloric acid belongs to control material in China, typically is inconvenient to obtain, should
With scope, especially family expenses have great limitation.Also, hydrochloric acid has corrosivity, there is certain danger during use.
Conventional membrane electrolytic cell can only produce strong acidic electrolyzed water, it is impossible to produce subacidity electrolysis water, and its preparation principle is：
The sodium chloride (concentration is less than 0.1%) of low concentration will be added in running water by sofening treatment, there is ion diaphragm formula electrolytic cell
It is referred to as acid from the acidic aqueous solution with low concentration effective chlorine, high redox potential of anode side generation after middle electrolysis
Electrolyzed oxidizing water (abbreviation acidifying water), in the alkaline aqueous solution referred to as alkaline reduction electric potential water that negative electrode side obtains.The method is only
Strong oxidized water can be prepared.
It produces water index：
pH：2.0-3.0；
ORP：≥1100mV；
Effective chlorine：50-70mg/L.
The diaphragm cell that subacidity electrolysis water can be produced is not reported so far.
Utility model content
According to more than deficiency of the prior art, the purpose of this utility model is to provide a kind of subacidity electrolysis water that produces
Device, can be using saline solution as electrolyzer, and shipping storage application is convenient, using safer.
The device of production subacidity electrolysis water described in the utility model, including electrolytic cell body, electrolytic cell body by every
Film is divided into anode chamber and cathode chamber, and barrier film is fixed on inside electrolytic cell body by dividing plate, and anode, cathode chamber are set in anode chamber
Negative electrode is inside set, anode and negative electrode are connected with power supply respectively by wire, and cathode chamber top sets negative electrode chamber inlet, and cathode chamber bottom sets
Buck is exported, and buck outlet is connected with buck branch line, and buck regulating valve is set on buck branch line, and ratio adjusting valve is set on dividing plate, than
Example regulating valve passes through separator bottom, upper portion of anode chamber to set anode compartment outlet, and anode compartment outlet is connected with subacidity electrolysis water branch line,
Product water regulating valve is set on subacidity electrolysis water branch line.
When in use, electrolyzer is electrolysed described device from negative electrode chamber inlet into cathode chamber, and then, partial electrolyte is produced
Raw buck passing ratio regulating valve enters into anode chamber's electrolysis, obtains subacidity electrolysis water；Adjusted by buck in electrolytic process
The ratio of the buck water outlet that section valve regulation electrolysis is produced, the water outlet of the subacidity electrolysis water for producing is adjusted by producing water regulating valve
Amount.
Described electrolyzer is sodium-chloride water solution.
The mass concentration of described sodium-chloride water solution is 0.05%-0.1%.
Described supply voltage is DC 8-12V, and electric current is 15-25A.
Described anode and cathode electrode is titanium plating ruthenium iridium electrode.
Described barrier film is ionic membrane.
The product water index of described subacidity electrolysis water is：pH：5.0-6.5；ORP：≥850mV；Effective chlorine：40mg/L-
100mg/L。
Described device application method is as follows：
Water regulating valve is produced in regulation, determines the aquifer yield of subacidity electrolysis water, and subacidity electrolysis water index is detected by instrument,
If pH>6.5；ORP：<850mV；Effective chlorine<40mg/L.Regulation buck regulating valve increase buck discharge rate, while the ratio of regulation
Regulating valve, the ratio for making buck enter anode chamber reduces, and by regulation, pH value can reduce, and ORP can increase, and effective chlorine can increase.
, whereas if pH<5.0；ORP：>850mV；Effective chlorine>100mg/L.Regulation buck regulating valve reduces buck discharge rate, while adjusting
Section ratio adjusting valve, the ratio for making buck enter anode chamber increases, and by regulation, pH value can increase, and ORP can be reduced, effective chlorine
Can reduce.
Compared with prior art, the beneficial effects of the utility model are：
1st, using sodium-chloride water solution as electrolyzer, transport preserves easy to use, and than hydrochloric acid safety, it is easier to obtain
.
2nd, it is raw material to use sodium chloride, cheap, convenient buying, energy-conserving and environment-protective.Simplify preparation technology, eliminate hydrochloric acid
With sodium chloride mixing arrangement, it is more suitable for largely producing.
Brief description of the drawings
Fig. 1 is that the utility model produces the apparatus structure schematic diagram that the method for subacidity electrolysis water is used；
In figure：1st, electrolytic cell body；2nd, anode chamber；3rd, cathode chamber；4th, anode；5th, negative electrode；6th, wire；7th, power supply；8th, it is cloudy
Pole room entrance；9th, buck outlet；10th, buck branch line；11st, buck regulating valve；12nd, anode compartment outlet；13rd, subacidity electrolysis water branch
Line；14th, water regulating valve is produced；15th, barrier film；16th, dividing plate；17th, ratio adjusting valve.
Specific embodiment
Embodiment of the present utility model is described further below in conjunction with the accompanying drawings：
As shown in figure 1, the device that the method for described production subacidity electrolysis water is used, including electrolytic cell body 1, electricity
Solution groove cell body 1 is divided into anode chamber 2 and cathode chamber 3 by barrier film 15, and barrier film 15 is fixed in electrolytic cell body 1 by dividing plate 16
Set in portion, anode chamber 2 in anode 4, cathode chamber 3 and set negative electrode 5, anode 4 and negative electrode 5 are connected with power supply 7 respectively by wire 6, it is cloudy
The top of pole room 3 sets negative electrode chamber inlet 8, and the bottom of cathode chamber 3 sets buck outlet 9, and buck outlet 9 is connected with buck branch line 10, buck
Buck regulating valve 11 is set on branch line 10, ratio adjusting valve 17 is set on dividing plate 16, ratio adjusting valve 17 passes through the bottom of barrier film 15, anode
The top of room 2 sets anode compartment outlet 12, and anode compartment outlet 12 is connected with subacidity electrolysis water branch line 13, subacidity electrolysis water branch line 13
On set product water regulating valve 14.
Water index is produced in 3 embodiments is：pH：5.0-6.5；ORP：≥850mV；Effective chlorine：40mg/L-100mg/L.
Embodiment 1
Regulation described device aquifer yield is 1L/min, and it is 10VDC to use decomposition voltage, and concentration of sodium chloride solution is
0.06%.Operating method is as follows：Water regulating valve 14 is produced in regulation makes aquifer yield for 1L/min, and water index is produced in observation, if pH>6.5；
ORP：<850mV；Effective chlorine<40mg/L.Regulation buck regulating valve 11 increases buck discharge rate, while ratio adjusting valve 17 is adjusted,
The ratio for making buck enter anode chamber 2 reduces, and product water index is made in acceptability limit by regulation.If pH<5.0；Effective chlorine>
100mg/L.Regulation buck regulating valve 11 reduces buck discharge rate, while adjusting ratio adjusting valve 17, buck is entered anode chamber 2
Ratio increase, make product water index in acceptability limit by adjusting repeatedly.
Embodiment 2
Regulation described device aquifer yield is 1.5L/min, and it is 10VDC to use decomposition voltage, and concentration of sodium chloride solution is
0.06%.On the basis of embodiment 1, it is 1.5L/min that regulation produce water regulating valve 14 to increase aquifer yield first, now product water pH
Can raise, ORP can be reduced, effective chlorine can be reduced, want to maintain subacidity water index, it is necessary to open big buck regulating valve 11, now
Producing water pH can be reduced, and ORP can be raised, and effective chlorine can be raised, and pH is between 5.0-6.5, ORP>850, adjust proportion adjustment
Valve 17 makes effective chlorine be in acceptability limit.
Embodiment 3
On the basis of embodiment 2, change the micro- 12VDC of decomposition voltage, remaining is constant, and now pH can be reduced, and ORP can rise
Height, effective chlorine can be raised, and want to maintain subacidity water index, it is necessary to turn down buck regulating valve 11, open vast scale regulating valve 17, be closed
Abortion water regulating valve 14, is adjusted repeatedly, can make subacidity electrolysis water index stabilization in the level of embodiment 2.Conversely, decomposition voltage
During using 8VDC, above-mentioned regulating valve can be adjusted to opposite direction.
Claims (5)
1. a kind of device for producing subacidity electrolysis water, it is characterised in that：Including electrolytic cell body (1), electrolytic cell body (1) by
Barrier film (15) is divided into anode chamber (2) and cathode chamber (3), and barrier film (15) is fixed in electrolytic cell body (1) by dividing plate (16)
Set in portion, anode chamber (2) and negative electrode (5) is set in anode (4), cathode chamber (3), anode (4) and negative electrode (5) are by wire (6) difference
It is connected with power supply (7), it is characterised in that：Cathode chamber (3) top sets negative electrode chamber inlet (8), and cathode chamber (3) bottom sets buck outlet
(9), buck outlet (9) is connected with buck branch line (10), and buck regulating valve (11) is set on buck branch line (10), and dividing plate sets on (16)
Ratio adjusting valve (17), ratio adjusting valve (17) sets anode compartment outlet (12) through barrier film (15) bottom, anode chamber (2) top,
Anode compartment outlet (12) is connected with subacidity electrolysis water branch line (13), and subacidity electrolysis water branch line sets product water regulating valve on (13)
(14)。
2. it is according to claim 1 production subacidity electrolysis water device, it is characterised in that：Power supply (7) voltage is DC8-
12V, electric current is 15-25A.
3. it is according to claim 1 production subacidity electrolysis water device, it is characterised in that：Anode (4) and negative electrode (5) electricity
Pole is titanium plating ruthenium iridium electrode.
4. it is according to claim 1 production subacidity electrolysis water device, it is characterised in that：Barrier film (15) is ionic membrane.
5. it is according to claim 1 production subacidity electrolysis water device, it is characterised in that：The index of subacidity electrolysis water
For：pH：5.0-6.5；ORP：≥850mV；Effective chlorine：40mg/L-100mg/L.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621289141.0U CN206219283U (en) | 2016-11-28 | 2016-11-28 | Produce the device of subacidity electrolysis water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621289141.0U CN206219283U (en) | 2016-11-28 | 2016-11-28 | Produce the device of subacidity electrolysis water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206219283U true CN206219283U (en) | 2017-06-06 |
Family
ID=58786657
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621289141.0U Active CN206219283U (en) | 2016-11-28 | 2016-11-28 | Produce the device of subacidity electrolysis water |
Country Status (1)
| Country | Link |
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| CN (1) | CN206219283U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108585308A (en) * | 2018-06-19 | 2018-09-28 | 大连合众金水科技有限公司 | The online preparation system of acidifying water |
| CN113697909A (en) * | 2021-09-27 | 2021-11-26 | 济南飞蓝水处理设备有限公司 | Method and device for preparing acidic electrolyzed water |
-
2016
- 2016-11-28 CN CN201621289141.0U patent/CN206219283U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108585308A (en) * | 2018-06-19 | 2018-09-28 | 大连合众金水科技有限公司 | The online preparation system of acidifying water |
| CN113697909A (en) * | 2021-09-27 | 2021-11-26 | 济南飞蓝水处理设备有限公司 | Method and device for preparing acidic electrolyzed water |
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