CN107720900A - A kind of method for treating water of washing machine water processing unit - Google Patents
A kind of method for treating water of washing machine water processing unit Download PDFInfo
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- CN107720900A CN107720900A CN201711037605.8A CN201711037605A CN107720900A CN 107720900 A CN107720900 A CN 107720900A CN 201711037605 A CN201711037605 A CN 201711037605A CN 107720900 A CN107720900 A CN 107720900A
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- Prior art keywords
- water
- silver ion
- ozone
- concentration
- electrolytic silver
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 107
- 238000005406 washing Methods 0.000 title claims abstract description 35
- 238000012545 processing Methods 0.000 title claims abstract description 30
- 238000000034 method Methods 0.000 title claims abstract description 26
- FOIXSVOLVBLSDH-UHFFFAOYSA-N Silver ion Chemical compound [Ag+] FOIXSVOLVBLSDH-UHFFFAOYSA-N 0.000 claims abstract description 84
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 83
- 239000007788 liquid Substances 0.000 claims abstract description 29
- 229910052709 silver Inorganic materials 0.000 claims abstract description 11
- 239000004332 silver Substances 0.000 claims abstract description 11
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 6
- 239000001301 oxygen Substances 0.000 claims abstract description 6
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 6
- 238000005259 measurement Methods 0.000 claims abstract description 4
- 238000005868 electrolysis reaction Methods 0.000 claims description 46
- 230000001105 regulatory effect Effects 0.000 claims description 10
- 229910017435 S2 In Inorganic materials 0.000 claims 6
- 150000002500 ions Chemical class 0.000 claims 1
- -1 silver ions Chemical class 0.000 abstract description 6
- 241000894007 species Species 0.000 abstract description 6
- 239000007789 gas Substances 0.000 abstract description 4
- 230000036541 health Effects 0.000 abstract description 4
- 230000008569 process Effects 0.000 abstract description 4
- 244000052616 bacterial pathogen Species 0.000 abstract description 3
- 230000003749 cleanliness Effects 0.000 abstract description 3
- 230000002779 inactivation Effects 0.000 abstract description 3
- 230000032258 transport Effects 0.000 abstract description 3
- 230000009286 beneficial effect Effects 0.000 abstract description 2
- 230000007613 environmental effect Effects 0.000 abstract description 2
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 4
- 239000003599 detergent Substances 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 238000004140 cleaning Methods 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 238000004891 communication Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000000249 desinfective effect Effects 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 239000000686 essence Substances 0.000 description 1
- 231100001261 hazardous Toxicity 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- RECVMTHOQWMYFX-UHFFFAOYSA-N oxygen(1+) dihydride Chemical compound [OH2+] RECVMTHOQWMYFX-UHFFFAOYSA-N 0.000 description 1
- 239000011941 photocatalyst Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/50—Treatment of water, waste water, or sewage by addition or application of a germicide or by oligodynamic treatment
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/68—Treatment of water, waste water, or sewage by addition of specified substances, e.g. trace elements, for ameliorating potable water
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/68—Treatment of water, waste water, or sewage by addition of specified substances, e.g. trace elements, for ameliorating potable water
- C02F1/685—Devices for dosing the additives
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2307/00—Location of water treatment or water treatment device
- C02F2307/12—Location of water treatment or water treatment device as part of household appliances such as dishwashers, laundry washing machines or vacuum cleaners
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Medicinal Chemistry (AREA)
- Detail Structures Of Washing Machines And Dryers (AREA)
- Control Of Washing Machine And Dryer (AREA)
Abstract
The invention discloses a kind of method for treating water of washing machine water processing unit, comprise the following steps：Ozone concentration in the water-carrying capacity and gas-liquid mixed plasma generator of collection water inlet unit interval；Ozone concentration value and the relation of electrolytic silver ion concentration and the water-carrying capacity of unit interval based on measurement, adjust ozone concentration and electrolytic silver ion concentration in washing machine water processing unit；Beneficial effect of the present invention：Active oxygen solubility ratio in the inactivation ratio of pathogenic bacteria, water is effectively increased in water, enhances clothes washing cleanliness factor；It is monitored and controlled by the implementation of sensor and controller, realizes and the dynamic and intelligent of ozone and concentration of silver ions is controlled, it is ensured that in optimal standard application, meets efficient, clean, health, the laundry demand of environmental protection；In addition, causing active specy caused by gas phase to dissolve in real time in water using gas-liquid mixed plasma, the loss during active specy transports is reduced, improves the efficiency of water process.
Description
Technical field
The present invention relates to cleaning equipment technology field, more particularly to a kind of method for treating water of washing machine water processing unit.
Background technology
Chemical detergent has turned into people's articles for use essential in laundry processes, but in use, these
Detergent can enter human body by modes such as skin contact or residuals, be caused to human health potentially hazardous, while also feed water
Environment brings serious pollution.As the improvement of people's living standards, and the awareness of environment protection and health enhancing, in the mistake of laundry
The usage amount of detergent is reduced in journey, does not even turn into people's tight demand using detergent.It is currently used to improve water
Cleaning ability, while there is the wash water processor of disinfecting and sterilizing functions, major technique has：Ozone, photocatalyst, uviol lamp,
Silver ion, or combinations thereof mode；But the dirt-removing power of water is limited after such hydrotreater processing, the generation of ozone needs
Connected by pipeline soluble in water, certain loss be present, reduce service efficiency, cause to be typically not capable of expected washing effect
Fruit, additionally, there may be Measuring Ozone Concentration in Water and silver ion burst size can not accurately control, cause Measuring Ozone Concentration in Water and silver from
Sub- content fluctuation range is big, ozone concentration and the exceeded and insufficient hidden danger of concentration of silver ions be present.
Therefore, it is necessary to which a kind of dynamic and intelligent controls ozone and concentration of silver ions, handles washing machine water efficient, easy to use
Processing unit and control method, to meet the high demand of the green laundry of people.
The problem of in correlation technique, effective solution is not yet proposed at present.
The content of the invention
This is to overcome existing technological deficiency using new technical problems to be solved, there is provided a kind of washing machine water processing dress
The method for treating water put, effectively can solve the problems, such as in background technology.
In order to solve the above technical problems, one aspect of the present invention is；
Provide a kind of method for treating water of washing machine water processing unit, it is characterised in that comprise the following steps：
S1：Ozone concentration in the water-carrying capacity and gas-liquid mixed plasma generator of collection water inlet unit interval；
S2：Ozone concentration value and the relation of electrolytic silver ion concentration and the water-carrying capacity of unit interval based on measurement, regulation are washed
Ozone concentration and electrolytic silver ion concentration in clothing machine water treatment facilities.
Further, in step S2, when the ozone concentration value is less than the lower limit of ozone concentration threshold range, regulation
The concentration of ozone is improved, when the ozone concentration value is more than the higher limit of ozone concentration threshold range, regulation reduces ozone
Concentration.
Further, in step S2, the relation of the water-carrying capacity of electrolytic silver ion concentration and unit interval is：
Wherein：CAg+ it is electrolytic silver ion concentration, F is the water-carrying capacity of unit time, and I is electrolysis power output current.
Further, in step S2, when the electrolytic silver ion concentration value is less than electrolytic silver ion concentration threshold scope
During lower limit, regulation improves the concentration of electrolytic silver ion, when the electrolytic silver ion concentration value is more than electrolytic silver ion concentration threshold
When being worth the higher limit of scope, regulation reduces the concentration of electrolytic silver ion.
Further, in step S2, ozone concentration in the gas-liquid mixed plasma generator is determined using controller
When value is less than the lower limit of ozone concentration threshold range or the higher limit more than ozone concentration threshold range, the controller control
High voltage power supply processed（Output voltage make ozone concentration value in gas-liquid mixed plasma generator to close to the ozone concentration
The direction of threshold range is adjusted, until the ozone concentration value is located at control when in the ozone concentration threshold range
Device keeps the output voltage of high voltage power supply.
Further, in step S2, electrolytic silver ion in the washing machine water processing unit is determined using the controller
Concentration is less than the lower limit of electrolytic silver ion concentration threshold scope or the higher limit more than electrolytic silver ion concentration threshold scope
When, the output current of the controller control electrolysis power makes electrolytic silver ion concentration to close to the electrolytic silver ion concentration threshold
The direction of value scope is adjusted, until the electrolytic silver ion concentration value is located in the range of the electrolytic silver ion concentration threshold
When controller keep electrolysis power output current.
Further, in step S2, the controller is sent out to the high voltage power supply control terminal and/or electrolysis power control terminal
Send regulating command；Based on the regulating command, high voltage power supply control terminal and/or electrolysis power the control terminal control is respective defeated
Go out end output, the high voltage power supply output end driving high-field electrode produces ozone, and the electrolysis power output end drives silver ion
Generator produces silver ion.
Further, including water inlet, electrolysis power and high voltage power supply, the water inlet is provided with water intaking valve, it is described enter
Water valve has gas-liquid mixed plasma generator by pipeline communication, and the pipeline is sequentially provided with water-carrying capacity biography at water intaking valve
Sensor and the silver ion generator electrically connected with electrolysis power output end, be provided with the gas-liquid mixed plasma generator with
The high-field electrode of high voltage power supply output end electrical connection, the gas-liquid mixed plasma generator bottom sense provided with dissolved ozone
Device, the gas-liquid mixed plasma generator bottom are provided with delivery port, the electrolysis power（Control terminal and high voltage power supply
Control terminal is connected with controller, and the controller also communicates to connect water intaking valve, water flow sensor and dissolved ozone sensing respectively
Device.
Further, based on the ozone concentration and the electrolytic silver ion concentration and the relation of respective threshold range, lead to
Cross the controller and control the output end of the electrolysis power and/or the output end of high voltage power supply, adjust at the washing machine water
Manage ozone concentration and electrolytic silver ion concentration in device.
Further, the controller sends regulation life to the high voltage power supply control terminal and/or electrolysis power control terminal
Order；Based on the regulating command, the high voltage power supply control terminal and/or electrolysis power control terminal control respective output end defeated
Go out, the high voltage power supply output end driving high-field electrode produces ozone, and the electrolysis power output end drives silver ion generator
Produce silver ion.
Beneficial effects of the present invention：A kind of method for treating water of washing machine water processing unit of the present invention, by install silver from
Electronic generator, gas-liquid mixed plasma generator, effectively increase active oxygen dissolving in the inactivation ratio of pathogenic bacteria, water in water
Rate, it greatly strengthen clothes washing cleanliness factor；It is monitored and controlled simultaneously by the implementation of sensor and controller, effectively dynamic is adjusted
Silver ion and ozone concentration in whole water, it is ensured that in optimal standard application, meet laundry efficiently, clean, hygienic, environmentally friendly
Demand；In addition, enabling to active specy caused by gas phase to dissolve in real time in water using gas-liquid mixed plasma, work is reduced
Property species transport in loss, improve the efficiency of water process；Realize and the dynamic and intelligent of ozone and concentration of silver ions is controlled.
Brief description of the drawings
In order to illustrate more clearly about the embodiment of the present invention or technical scheme of the prior art, below will be to institute in embodiment
The accompanying drawing needed to use is briefly described, it should be apparent that, drawings in the following description are only some implementations of the present invention
Example, for those of ordinary skill in the art, on the premise of not paying creative work, can also be obtained according to these accompanying drawings
Obtain other accompanying drawings.
Fig. 1 is a kind of schematic flow sheet of the method for treating water of washing machine water processing unit of the present invention；
Fig. 2 is a kind of structural representation of the preferred embodiment of device one of washing machine water processing of the present invention.
Embodiment
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is carried out clear, complete
Site preparation describes, it is clear that described embodiment is only part of the embodiment of the present invention, rather than whole embodiments.It is based on
Embodiment in the present invention, the every other embodiment that those of ordinary skill in the art are obtained, belong to what the present invention protected
Scope.
As shown in figure 1, according to a kind of method for treating water of washing machine water processing unit of the present invention, its feature exists
In comprising the following steps：
S1：Gather water inlet 1 at the unit interval water-carrying capacity and gas-liquid mixed plasma generator 8 in ozone concentration；
S2：Ozone concentration value and the relation of electrolytic silver ion concentration and the water-carrying capacity of unit interval based on measurement, regulation are washed
Ozone concentration and electrolytic silver ion concentration in clothing machine water treatment facilities.
In the present embodiment, in step S2, when the ozone concentration value is less than the lower limit of ozone concentration threshold range, adjust
Section improves the concentration of ozone, and when the ozone concentration value is more than the higher limit of ozone concentration threshold range, regulation reduces ozone
Concentration.
In the present embodiment, in step S2, the relation of the water-carrying capacity of electrolytic silver ion concentration and unit interval is：
Wherein：CAg+ it is electrolytic silver ion concentration, F is the water-carrying capacity of unit time, and I is electrolysis power output current.
In the present embodiment, in step S2, when the electrolytic silver ion concentration value is less than electrolytic silver ion concentration threshold scope
Lower limit when, regulation improve electrolytic silver ion concentration, when the electrolytic silver ion concentration value is more than electrolytic silver ion concentration
During the higher limit of threshold range, regulation reduces the concentration of electrolytic silver ion.
In the present embodiment, in step S2, ozone in the gas-liquid mixed plasma generator 8 is determined using controller 9
When concentration value is less than the lower limit of ozone concentration threshold range or the higher limit more than ozone concentration threshold range, the control
Device 9 controls the output voltage of high voltage power supply 7 to make the ozone concentration value in gas-liquid mixed plasma generator 8 to close to described smelly
The direction of oxygen concentration threshold range is adjusted, until the ozone concentration value is located at when institute in the ozone concentration threshold range
State the output voltage that controller 9 keeps high voltage power supply 7.
In the present embodiment, in step S2, using the controller 9 determine in the washing machine water processing unit electrolytic silver from
Sub- concentration is less than the lower limit of electrolytic silver ion concentration threshold scope or the upper limit more than electrolytic silver ion concentration threshold scope
During value, the controller 9 controls the output current of electrolysis power 4 to make electrolytic silver ion concentration dense to the close electrolytic silver ion
The direction of degree threshold range is adjusted, until the electrolytic silver ion concentration value is located at the electrolytic silver ion concentration threshold model
Controller 9 keeps the output current of electrolysis power 4 when enclosing interior.
In the present embodiment, in step S2, the controller 9 is controlled to the control terminal of high voltage power supply 7 and/or electrolysis power 4
End processed sends regulating command；Based on the regulating command, the control terminal of high voltage power supply 7 and/or the control of the control terminal of electrolysis power 4
Respective output end output, the output end of the high voltage power supply 7 driving high-field electrode 11 produce ozone, and the electrolysis power 4 exports
End driving silver ion generator 5 produces silver ion.
As shown in Fig. 2 a kind of washing machine water processing unit, including water inlet 1, electrolysis power 4 and high voltage power supply 7, it is described
Water intaking valve 2 is provided with water inlet 1, the water intaking valve 2 is communicated with gas-liquid mixed plasma generator 8, the pipe by pipeline 6
Road 6 is sequentially provided with water flow sensor 3 and the silver ion generator electrically connected with the output end of electrolysis power 4 at water intaking valve 2
5, the gas-liquid mixed plasma generator 8 is interior to be provided with the high-field electrode 11 electrically connected with the output end of high voltage power supply 7, the gas
The bottom of liquid hybrid plasma generator 8 is provided with dissolved ozone sensor 13, the bottom of gas-liquid mixed plasma generator 8
Provided with delivery port 12, the control terminal of the electrolysis power 4 and the control terminal of high voltage power supply 7 are connected with controller 9, the controller
9 also communicate to connect water intaking valve 2, water flow sensor 3 and dissolved ozone sensor 13 respectively.
In the present embodiment, the relation based on the ozone concentration and the electrolytic silver ion concentration and respective threshold range,
The output end of the electrolysis power 4 and/or the output end of high voltage power supply 7 are controlled by the controller 9, adjusts the washing machine
Ozone concentration and electrolytic silver ion concentration in water treatment facilities.
In the present embodiment, the controller 9 sends to the control terminal of high voltage power supply 7 and/or the control terminal of electrolysis power 4 and adjusted
Section order；Based on the regulating command, the control terminal of high voltage power supply 7 and/or the control terminal of electrolysis power 4 control respective output
End output, the output end of high voltage power supply 7 driving high-field electrode 11 produce ozone, the output end of the electrolysis power 4 driving silver from
Electronic generator 5 produces silver ion.
When specifically used, first on device after electricity, water intaking valve 2 is opened in controller control, and current are passed through by water inlet 1
After water flow sensor 3, flow through silver ion generator 5 and gas-liquid hybrid plasma generator 8 carries out purified treatment, most pass through afterwards
Delivery port is discharged, and for the washing of clothing, controller 9 passes through water flow sensor 3 and the real-time delivery of dissolved ozone sensor 13
Data, control electrolysis power 4 output current and high voltage power supply 7 power output, when in water concentration of silver ions be less than setting
During value, the output current of electrolysis power 4 is improved；Conversely, reduce the output current of electrolysis power 4；When Measuring Ozone Concentration in Water is less than
During setting value, the power output of high voltage power supply 7 is improved, conversely, the increase power output of high voltage power supply 7, so that it is guaranteed that the water of processing
Matter meets standard requirement.
In the present embodiment, the water-carrying capacity F of unit interval at water inlet 1 is collected in step S1 by water flow sensor 3,
Ozone concentration n in gas-liquid mixed plasma generator 8 is detected by dissolved ozone sensor 13oz。
In the present embodiment, in step S2, ozone concentration threshold range is set as ns0-△n0~ns0, the controller 9 is to smelly
Oxygen concentration value nozThe method for being judged and being adjusted includes：
Work as ns0 - △n0 < noz < ns0 When, controller 9 keeps the output end of high voltage power supply 7 to the output voltage of high-field electrode 11；
Work as noz < ns0 - △n0When, controller 9 increases the output end of high voltage power supply 7 to the output voltage of high-field electrode 11；
Work as noz > ns0When, controller 9 reduces the output end of high voltage power supply 7 to the output voltage of high-field electrode 11.
In the present embodiment, in step S2, electrolytic silver ion concentration threshold scope n is sets1-△n1~ns1, the controller 9
Device Inner electrolysis concentration of silver ions n is obtained by the relation of electrolytic silver ion concentration and the water-carrying capacity of unit intervalAg, the control
Device 9 is to electrolytic silver ion concentration nAgThe method for being judged and being adjusted includes：
Work as ns1 - △n1 < nAg < ns1 When, controller 9 keeps the output end of electrolysis power 4 to export electricity to silver ion generator 5
Stream；
Work as nAg < ns1 - △n1When, controller 9 increases the output end of electrolysis power 4 to the output current of silver ion generator 5；
Work as nAg > ns1When, controller 9 reduces the output end of electrolysis power 4 to the output current of silver ion generator 5.
In summary, by means of the above-mentioned technical proposal of the present invention, at a kind of water of washing machine water processing unit of the present invention
Reason method, by installing silver ion generator, gas-liquid mixed plasma generator, effectively increase the inactivation of pathogenic bacteria in water
Active oxygen solubility ratio in rate, water, greatly strengthen clothes washing cleanliness factor；Monitored simultaneously by the implementation of sensor and controller
And control, silver ion and ozone concentration effectively in dynamic adjustment water, it is ensured that in optimal standard application, meet efficient, clean
Only, health, the laundry demand of environmental protection；In addition, enable to active specy caused by gas phase real using gas-liquid mixed plasma
When dissolve in water, reduce the loss during active specy transports, improve the efficiency of water process；Realize to ozone and silver ion
The dynamic and intelligent control of concentration.
The foregoing is merely illustrative of the preferred embodiments of the present invention, is not intended to limit the invention, all essences in the present invention
God any modification, equivalent substitution and improvements made etc., should be included in the scope of the protection with principle.
Claims (10)
1. a kind of method for treating water of washing machine water processing unit, it is characterised in that comprise the following steps：
S1：Gather water inlet（1）Locate the water-carrying capacity and gas-liquid mixed plasma generator of unit interval（8）Middle ozone is dense
Degree；
S2：Ozone concentration value and the relation of electrolytic silver ion concentration and the water-carrying capacity of unit interval based on measurement, regulation are washed
Ozone concentration and electrolytic silver ion concentration in clothing machine water treatment facilities.
A kind of 2. method for treating water of washing machine water processing unit according to claim 1, it is characterised in that step S2
In, when the ozone concentration value is less than the lower limit of ozone concentration threshold range, regulation improves the concentration of ozone, when described smelly
When oxygen concentration value is more than the higher limit of ozone concentration threshold range, regulation reduces the concentration of ozone.
A kind of 3. method for treating water of washing machine water processing unit according to claim 2, it is characterised in that step S2
In, the relation of the water-carrying capacity of electrolytic silver ion concentration and unit interval is：
Wherein：CAg+ it is electrolytic silver ion concentration, F is the water-carrying capacity of unit time, and I is electrolysis power output current.
A kind of 4. method for treating water of washing machine water processing unit according to claim 3, it is characterised in that step S2
In, when the electrolytic silver ion concentration value is less than the lower limit of electrolytic silver ion concentration threshold scope, regulation improves electrolytic silver
The concentration of ion, when the electrolytic silver ion concentration value is more than the higher limit of electrolytic silver ion concentration threshold scope, regulation subtracts
The concentration of few electrolytic silver ion.
A kind of 5. method for treating water of washing machine water processing unit according to claim 4, it is characterised in that step S2
In, utilize controller（9）Determine the gas-liquid mixed plasma generator（8）Middle ozone concentration value is less than ozone concentration threshold value
When the lower limit of scope or the higher limit more than ozone concentration threshold range, the controller（9）Control high voltage power supply（7）'s
Output voltage makes gas-liquid mixed plasma generator（8）Interior ozone concentration value is to close to the ozone concentration threshold range
Direction is adjusted, until the ozone concentration value is located at controller when in the ozone concentration threshold range（9）Keep
High voltage power supply（7）Output voltage.
A kind of 6. method for treating water of washing machine water processing unit according to claim 5, it is characterised in that step S2
In, utilize the controller（9）Determine that it is dense to be less than electrolytic silver ion for electrolytic silver ion concentration in the washing machine water processing unit
When spending the lower limit of threshold range or the higher limit more than electrolytic silver ion concentration threshold scope, the controller（9）Control
Electrolysis power（4）Output current electrolytic silver ion concentration is entered to close to the direction of the electrolytic silver ion concentration threshold scope
Row regulation, until the electrolytic silver ion concentration value is located at controller when in the range of the electrolytic silver ion concentration threshold（9）Protect
Hold electrolysis power（4）Output current.
A kind of 7. method for treating water of washing machine water processing unit according to claim 6, it is characterised in that step S2
In, the controller（9）To the high voltage power supply（7）Control terminal and/or electrolysis power（4）Control terminal sends regulating command；Base
In the regulating command, the high voltage power supply（7）Control terminal and/or electrolysis power（4）Control terminal controls respective output end defeated
Go out, the high voltage power supply（7）Output end drives high-field electrode（11）Produce ozone, the electrolysis power（4）Output end driving silver
Ion generator（5）Produce silver ion.
8. a kind of washing machine water processing unit, it is characterised in that including water inlet（1）, electrolysis power（4）And high voltage power supply（7）,
The water inlet（1）Place is provided with water intaking valve（2）, the water intaking valve（2）Pass through pipeline（6）It is communicated with gas-liquid mixed plasma hair
Raw device（8）, the pipeline（6）Close to water intaking valve（2）Place is sequentially provided with water flow sensor（3）With with electrolysis power（4）Output
Hold the silver ion generator of electrical connection（5）, the gas-liquid mixed plasma generator（8）Inside it is provided with and high voltage power supply（7）It is defeated
Go out the high-field electrode of end electrical connection（11）, the gas-liquid mixed plasma generator（8）Bottom is provided with dissolved ozone sensor
（13）, the gas-liquid mixed plasma generator（8）Bottom is provided with delivery port（12）, the electrolysis power（4）Control terminal
And high voltage power supply（7）Control terminal be connected with controller（9）, the controller（9）Water intaking valve is also communicated to connect respectively（2）, water
Flow sensor（3）With dissolved ozone sensor（13）.
9. a kind of washing machine water processing unit according to claim 8, it is characterised in that based on the ozone concentration and institute
The relation of electrolytic silver ion concentration and respective threshold range is stated, passes through the controller（9）Control the electrolysis power（4）It is defeated
Go out end and/or high voltage power supply（7）Output end, it is dense to adjust ozone concentration and electrolytic silver ion in the washing machine water processing unit
Degree.
A kind of 10. washing machine water processing unit according to claim 9, it is characterised in that the controller（9）To described
High voltage power supply（7）Control terminal and/or electrolysis power（4）Control terminal sends regulating command；Based on the regulating command, the high pressure
Power supply（7）Control terminal and/or electrolysis power（4）Control terminal controls respective output end output, the high voltage power supply（7）Output end
Drive high-field electrode（11）Produce ozone, the electrolysis power（4）Output end drives silver ion generator（5）Produce silver ion.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711037605.8A CN107720900A (en) | 2017-10-30 | 2017-10-30 | A kind of method for treating water of washing machine water processing unit |
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| CN201711037605.8A CN107720900A (en) | 2017-10-30 | 2017-10-30 | A kind of method for treating water of washing machine water processing unit |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| ES2760006A1 (en) * | 2018-11-12 | 2020-05-12 | Imp Ecologicas S L | OZONE BASED DETERGENT CLEANING SYSTEM (Machine-translation by Google Translate, not legally binding) |
| CN112263196A (en) * | 2020-10-23 | 2021-01-26 | 珠海格力电器股份有限公司 | Electrolysis control method and device, electrolysis equipment and readable storage medium |
Citations (15)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN112263196A (en) * | 2020-10-23 | 2021-01-26 | 珠海格力电器股份有限公司 | Electrolysis control method and device, electrolysis equipment and readable storage medium |
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Effective date of registration: 20181008 Address after: 519000 No. 2402, block B, Fuhua Li, 2021 Jiuzhou Road West, Xiangzhou District, Zhuhai, Guangdong. Applicant after: Wen Shijie Address before: 519000 No. 2402, block B, Fuhua Li, 2021 Jiuzhou Road West, Xiangzhou District, Zhuhai, Guangdong. Applicant before: Wen Shijie Applicant before: Lin Guoping |