A kind of acid oxidation potential disinfectant production system
Technical field
This utility model belongs to water-treatment technology field, relates to a kind of electrolysis and produces the water generator of acid oxidation potential disinfectant industry.
Background technology
Acidic oxidized electric potential water maker process for producing water out has low ph value, and owing to the hydrion enrichment in anode region makes the pH value of anode chamber can reach less than 2.7, low pH value and high ORP value are the significant features of micro-electrolytic water anodic product;Additionally, its available chlorine content is low, under the preparation condition generally used (in raw material, sodium chloride content is less than 0.1%), in acidic potential aquatic products, available chlorine content is typically 30~50ppm, and the acidity that acidic oxidized electric potential water is possessed (pH (ORP) 1100mV), even if making in the case of the lowest " trace " chlorine residue, acidic oxidized electric potential water still has wide spectrum, quick disinfection effect;And noresidue after its use, after the electrolyzed-oxidizing water effect body surface with antibacterial, virus or other dissolved organic matter, the organisms such as wherein effective ingredient (such as effective chlorine and active oxidation intermediate species etc.) can be had an effect by rapid antibacterial, virus or dissolved organic matter with body surface, antibacterial are decomposed by rapid oxidation;And electrolyzed-oxidizing water itself is reduced to light water the most therewith, even if the body surface of acidic potential water loading is not with and without the Organic substance such as antibacterial of q.s, effective ingredient in electrolyzed-oxidizing water is as react with the impurity micronic dust of Reduction in Air and be reduced inefficacy, so, acidic oxidized electric potential water reality apply after without any residual.
This utility model is that a kind of acidic oxidized electric potential water generates equipment, be a kind of with saline solution for raw material electrolysis production for sterilizing, sterilizing, fresh-keeping strong oxidized water and for decontamination, remove the residual strong alkaline water of agriculture.
Utility model content
The problem that the purpose of this utility model is to overcome prior art to exist, it is provided that acid oxidation potential disinfectant production system.
For realizing above-mentioned technical purpose, reaching above-mentioned technique effect, this utility model is achieved through the following technical solutions:
A kind of acid oxidation potential disinfectant production system, this system includes into water path, described water inlet communication multistage filtering path, the water side of described multistage filtering path is respectively communicated with electrolysis bath water inlet branch road and brine tank water inlet branch road, one end of described electrolysis bath water inlet branch road connects the water inlet of an electrolysis bath, one end of described brine tank water inlet branch road connects a brine tank, described brine tank enters the salt mouth of a river by a pump water branch road connection electrolysis bath, and described electrolysis bath is additionally provided with strong acid water out and highly basic water out.
Further; described water inlet path is provided with water intaking valve; PP cotton filter core bucket, granular active carbon filter element bucket and extruded activated carbon filter element bucket sequentially it is provided with on described multistage filtering path; described electrolysis bath water inlet branch road is provided with entering water electromagnetic valve; described brine tank water inlet branch road is provided with NC electromagnetic valve; described brine tank top is provided with salt and adds mouth, and described pump water branch road is sequentially provided with brine pump and cleaner.
Further, described brine tank upside is provided with overflow valve, and brine tank bottom is provided with drain valve, and described brine pump is arranged at the bottom of brine tank.
Further, described brine tank water inlet branch road connection salt adds mouth.
Further, this system also includes controller, and the upper liquid level sensor of electrical connection controller, lower liquid level sensor and low tension switch, described upper liquid level sensor is arranged at the internal box top of brine tank, for detecting whether saline solution face exceedes setting height and send detection signal to controller, described lower liquid level sensor is arranged at the internal box bottom of brine tank, for whether detecting saline solution face less than setting height and to controller transmission detection signal, described low tension switch is arranged on electrolysis bath water inlet branch road, for detecting the hydraulic pressure in electrolysis bath water inlet branch road and sending detection signal to controller.
Further, on the electrolysis bath water inlet branch road that described low tension switch is arranged between entering water electromagnetic valve and water inlet.
Further, described controller is also electrically connected entering water electromagnetic valve and NC electromagnetic valve, controls water inlet for the detection signal transmitted according to described upper liquid level sensor, lower liquid level sensor and low tension switch or cuts off the water supply.
The beneficial effects of the utility model are:
Technical solutions of the utility model, simple and reliable for structure, the multistage filtering of water inlet can significantly extend the life-span of electrolysis bath, and has brine tank water level automatic control structure, electrolysis bath water cut-off protection structure, improves system reliability further, improves system work efficiency.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Label declaration in figure: 1, water inlet path, 11, water intaking valve, 2, multistage filtering path, 21, PP cotton filter core bucket, 22, granular active carbon filter element bucket, 23, extruded activated carbon filter element bucket, 3, electrolysis bath water inlet branch road, 31, entering water electromagnetic valve, 32, low tension switch, 4, brine tank water inlet branch road, 41, NC electromagnetic valve, 5, electrolysis bath, 51, water inlet, 52, enter the salt mouth of a river, 53, strong acid water out, 54, highly basic water out, 6, brine tank, 61, salt adds mouth, 62, overflow valve, 63, drain valve, 7, pump water branch road, 71, brine pump, 72, cleaner, 8, upper liquid level sensor, 9, lower liquid level sensor.
Detailed description of the invention
Below with reference to the accompanying drawings and in conjunction with the embodiments, this utility model is described in detail.
nullWith reference to shown in Fig. 1,A kind of acidic oxidation point position disinfectant production system,This system includes into water path 1,Described water inlet path 1 connects multistage filtering path 2,The water side of described multistage filtering path 2 is respectively communicated with electrolysis bath water inlet branch road 3 and brine tank water inlet branch road 4,In the present embodiment,A three-way valve is used to connect,One end of described electrolysis bath water inlet branch road 3 connects the water inlet 51 of an electrolysis bath 5,One end of described brine tank water inlet branch road 4 connects a brine tank 6,Described brine tank 6 enters the salt mouth of a river 52 by what a pump water branch road 7 connected electrolysis bath 5,In the present embodiment,Electrolysis bath 5 is acid electrolysis bath,Electrolysis bath 5 is by salt water mixed solution electrolysis production strong oxidized water (pH value is less than 2.7) and strong alkaline water (pH value is more than 11),Strong acid water out 53 and highly basic water out 54 it is additionally provided with on described electrolysis bath 5.
Described water inlet path 1 is provided with water intaking valve 11; PP cotton filter core bucket 21, granular active carbon filter element bucket 22 and extruded activated carbon filter element bucket 23 sequentially it is provided with on described multistage filtering path 2; described electrolysis bath water inlet branch road 3 is provided with entering water electromagnetic valve 31; described brine tank water inlet branch road 4 is provided with NC electromagnetic valve 41; add water for configuring electrolyte (saline solution); described brine tank 6 top is provided with salt and adds mouth 61, and described pump water branch road 7 is sequentially provided with brine pump 71 and cleaner 72.PP cotton filter core bucket 21 is for removing the solid impurity that rust, sandstone etc. in water are thicker; granular active carbon filter element bucket 22 adsorbs the chlorine in water, odor, the material such as heterochromatic, and extruded activated carbon filter element bucket 23 decolours further, removes Organic substance in water, heavy metal, chlorine residue etc..
Described brine tank 6 upside is provided with overflow valve 62, and brine tank 6 bottom is provided with drain valve 63, and described brine pump 71 is arranged at the bottom of brine tank 6.
Described brine tank water inlet branch road 4 connects salt and adds mouth 61.
This system also includes controller, and the upper liquid level sensor 8 of electrical connection controller, lower liquid level sensor 9 and low tension switch 32, described upper liquid level sensor 8 is arranged at the internal box top of brine tank 6, for detecting whether saline solution face exceedes setting height and send detection signal to controller, described lower liquid level sensor 9 is arranged at the internal box bottom of brine tank 6, for whether detecting saline solution face less than setting height and to controller transmission detection signal, described low tension switch 32 is arranged on electrolysis bath water inlet branch road 3, for detecting the hydraulic pressure in electrolysis bath water inlet branch road 3 and sending detection signal to controller.
On the electrolysis bath water inlet branch road 3 that described low tension switch 32 is arranged between entering water electromagnetic valve 31 and water inlet 51; low tension switch 32 is used for protecting electrolysis bath; its principle is if stopping running water or hydraulic pressure are too small; low tension switch 32 can inform one signal of controller; termination be will turn off by controller to electrolyzer with electricity, entering water electromagnetic valve 31.
Described controller is also electrically connected entering water electromagnetic valve 31 and NC electromagnetic valve 41, controls water inlet for the detection signal transmitted according to described upper liquid level sensor 8, lower liquid level sensor 9 and low tension switch 32 or cuts off the water supply.Particularly as follows: detection saline solution surplus.When saline solution is less than lower liquid level sensor 9, lower liquid level sensor 9 will give one signal of controller, NC electromagnetic valve 41 will automatically open up, start to supplement saline, when saline solution liquid level reaches upper liquid level sensor 8, upper liquid level sensor 8 will give one signal of controller, and NC electromagnetic valve 41 will be automatically switched off, and stops moisturizing.
The foregoing is only preferred embodiment of the present utility model, be not limited to this utility model, for a person skilled in the art, this utility model can have various modifications and variations.All within spirit of the present utility model and principle, any modification, equivalent substitution and improvement etc. made, within should be included in protection domain of the present utility model.