CN206127026U - Combined type electro adsorption circulation water treatment system - Google Patents
Combined type electro adsorption circulation water treatment system Download PDFInfo
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- CN206127026U CN206127026U CN201621070326.2U CN201621070326U CN206127026U CN 206127026 U CN206127026 U CN 206127026U CN 201621070326 U CN201621070326 U CN 201621070326U CN 206127026 U CN206127026 U CN 206127026U
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Abstract
The utility model provides a combined type electro adsorption circulation water treatment system, include: terminal equipment, water quality monitoring device, electro adsorption water treatment ware, water filter equipment and water circle device, terminal equipment respectively with water quality monitoring device and electro adsorption water treatment ware are connected water filter equipment electro adsorption water treatment ware and water filter equipment respectively with the water quality monitoring device is connected, water quality monitoring device and water filter equipment are connected to through water circle device respectively terminal equipment. The utility model discloses a processing terminal equipment cooling water is come to electrochemistry and secondary filter's mode, can significantly reduce even without the medicament, and when the incrustation scale was appeared in addition, the salt content of aquatic also can descend, brings the benefit for subsequent processing or retrieval and utilization to can practice thrift a large amount of water consumptions, the blowdown water yield has significantly reduced.
Description
Technical field
This utility model is related to a kind of water treatment system, more particularly to a kind of Combined type electric sorption cycle water treatment system.
Background technology
In terminal units such as traditional air-conditioner hosts to method for treating water, chemical agent can be added in recirculated water, it is to avoid
Recirculated cooling water fouling, but final these medicaments can cause the salinity in waste water to increase, i.e., and conductivity is raised；And according to environmental protection
Require, need waste water recycling, adding medicament will be so that desalination pressure rise, deteriorating water quality, this be one；Second, traditional
During chemical method processing cycle cooling water, due to Ca2+、Mg2+、CO3 2- and SO4 2- wait still in water, and chemical agent
Controlled concentration is required, so cycles of concentration is probably at 2-3 times, the water yield required for displacement is than larger.
The content of the invention
Technical problem to be solved in the utility model is to need offer one kind to greatly reduce even without medicament, section
About water consumption, and the effectively Combined type electric sorption cycle water treatment system of reduction water amount of blowdown.
In this regard, this utility model provides a kind of Combined type electric sorption cycle water treatment system, including：Terminal unit, water quality
Monitoring device, electro-adsorption hydrotreater, water filtering device and water circle device, the terminal unit respectively with the water quality monitoring
Device is connected with electro-adsorption hydrotreater, electro-adsorption hydrotreater and water filtering device described in water filtering device respectively with it is described
Water monitoring device is connected, and the water monitoring device and water filtering device are connected to the end by water circle device respectively
End equipment.
Further improvement of the utility model is that the terminal unit includes air-conditioner host.
Further improvement of the utility model is that the water monitoring device includes body, fan blade and the hydraulic turbine, described
The hydraulic turbine is arranged on the body, and the fan blade is arranged on the hydraulic turbine.
Further improvement of the utility model is, also including the first butterfly valve, the terminal unit is connected by the first butterfly valve
It is connected to the body.
Further improvement of the utility model is, also including the second butterfly valve, the terminal unit is connected by the second butterfly valve
It is connected to the hydraulic turbine.
Further improvement of the utility model is that the outlet and water inlet of the terminal unit are respectively arranged with the 3rd
Butterfly valve and the 6th butterfly valve.
Further improvement of the utility model is that the water inlet of the electro-adsorption hydrotreater is provided with the 4th butterfly valve.
Further improvement of the utility model is that the water filtering device includes water filtration sewage draining exit and first circulation
Pump, the water monitoring device is connected to the first circulation pump by water filtration sewage draining exit, and the first circulation pump is connected to
The water circle device.
Further improvement of the utility model is that the water filtering device also includes the 5th butterfly valve, the first circulation
Pump is connected by the 5th butterfly valve with the water circle device.
Further improvement of the utility model is that the water circle device includes second circulation pump and the 3rd circulating pump,
The water monitoring device is connected to terminal unit by second circulation pump and the 3rd circulating pump respectively.
Compared with prior art, the beneficial effects of the utility model are：By the way of electrochemistry and secondary filter come
The cooling water of processing terminal equipment, can greatly reduce even without medicament, and while incrustation scale precipitation, the salinity in water
Also can decline, be that subsequent treatment or reuse bring benefit；Because this utility model is directly by Ca2+、Mg2+、CO3 2- and SO4 2-
Plasma is directly separated out from water, as long as therefore C 1 content is less than controlled concentration, the cycles of concentration of recirculated water just can improve
To 8-10 times, and then substantial amounts of water consumption is saved, be also considerably reduced water amount of blowdown.
Description of the drawings
Fig. 1 is a kind of system structure diagram of embodiment of this utility model.
Specific embodiment
Below in conjunction with the accompanying drawings, preferably embodiment of the present utility model is described in further detail.
As shown in figure 1, this example provides a kind of Combined type electric sorption cycle water treatment system, including：Terminal unit 1, water quality
Monitoring device 2, electro-adsorption hydrotreater 3, water filtering device 4 and water circle device 5, the terminal unit 1 respectively with the water
Matter monitoring device 2 is connected with electro-adsorption hydrotreater 3, electro-adsorption hydrotreater 3 and water filtering device described in water filtering device 4
4 are connected respectively with the water monitoring device 2, and the water monitoring device 2 and water filtering device 4 are filled respectively by water circulation
Put 5 and be connected to the terminal unit 1.Terminal unit 1 preferably includes air-conditioner host described in this example.
As shown in figure 1, water monitoring device 2 described in this example includes body 21, fan blade 22 and the hydraulic turbine 23, the hydraulic turbine
23 are arranged on the body 21, and the fan blade 22 is arranged on the hydraulic turbine 23；This example also includes the first butterfly valve 6 and second
Butterfly valve 7, the terminal unit 1 is connected to the body 21 by the first butterfly valve 6, and the terminal unit 1 is connected by the second butterfly valve 7
It is connected to the hydraulic turbine 23.The outlet and water inlet of terminal unit 1 described in this example is respectively arranged with the 3rd butterfly valve 8 and the 6th butterfly
Valve 9, the water inlet of the electro-adsorption hydrotreater 3 is provided with the 4th butterfly valve 10.
As shown in figure 1, water filtering device 4 described in this example includes water filtration sewage draining exit 41, the butterfly of first circulation pump 42 and the 5th
Valve 43, the water monitoring device 2 is connected to the first circulation pump 42, the first circulation pump by water filtration sewage draining exit 41
42 are connected by the 5th butterfly valve 43 with the water circle device 5.
As shown in figure 1, water circle device 5 described in this example includes the circulating pump 52 of second circulation pump 51 and the 3rd, the water quality
Monitoring device 2 is connected to terminal unit 1 by the circulating pump 52 of second circulation pump 51 and the 3rd respectively.
This example processes the cooling water of the terminal units such as air-conditioner host 1 by the way of electrochemistry and secondary filter, utilizes
Electrochemical means cause the incrustation ion Ca in recirculated water2+、Mg2+、CO3 2- and SO4 2- wait to form dirty class in electro-adsorption water process
Separate out in advance in device 3, dirt is formed on the heat exchanger of air-conditioner host so as to avoid；And secondary filter is done using filter material, will
The contaminant filters such as the float in water are clean, the nucleus that incrustation scale attachment is generated reduced, so as to reduce the generation of incrustation scale.This example is adopted
Advanced electrochemical water treatment technology, i.e., employ the advance scale removal desalting system of electro-adsorption in electro-adsorption hydrotreater 3, electricity
Certain operating current is maintained in the Galvanosorptive reaction room of absorption hydrotreater 3, in reaction chamber wall negative electrode height is formed about
The hydroxide ion of concentration, this elevated pH environment allows the advance fouling of mineral and salt of easy fouling, and separates out from water,
Reaction chamber wall is adsorbed in, its pH environment is about 13 or so.
Electrochemical reaction described in this example is completed by electro-adsorption hydrotreater 3, and secondary filter then passes through water
Come what is completed, this example employs water monitoring device 2 to defecator 4, and water process will be reduced after condition of water quality has been reached
Flow, so as to reduce unnecessary loss.
This example, come the cooling water of processing terminal equipment 1, can be greatly reduced very by the way of electrochemistry and secondary filter
Extremely without medicament, and while incrustation scale precipitation, the salinity in water also can decline, and be that subsequent treatment or reuse bring benefit；
Because this example is directly by Ca2+、Mg2+、CO3 2- and SO4 2- plasma directly from water separate out, as long as therefore C 1 content do not surpass
Controlled concentration is crossed, the cycles of concentration of recirculated water just can bring up to 8-10 times, and then save substantial amounts of water consumption, also just significantly
Reduce water amount of blowdown.
The specific embodiment of the above is better embodiment of the present utility model, not limits this practicality with this new
Type is embodied as scope, and scope of the present utility model includes being not limited to this specific embodiment, all according to this utility model
Shape, the equivalence changes made of structure in protection domain of the present utility model.
Claims (10)
1. a kind of Combined type electric sorption cycle water treatment system, it is characterised in that include：Terminal unit, water monitoring device, electricity
Absorption hydrotreater, water filtering device and water circle device, the terminal unit is inhaled respectively with the water monitoring device and electricity
Attached water processor is connected, and electro-adsorption hydrotreater and water filtering device described in water filtering device are filled respectively with the water quality monitoring
Put and be connected, the water monitoring device and water filtering device are connected to the terminal unit by water circle device respectively.
2. Combined type electric sorption cycle water treatment system according to claim 1, it is characterised in that the terminal unit bag
Include air-conditioner host.
3. Combined type electric sorption cycle water treatment system according to claim 1, it is characterised in that the water quality monitoring dress
Put including body, fan blade and the hydraulic turbine, the hydraulic turbine is arranged on the body, and the fan blade is arranged at the hydraulic turbine
On.
4. Combined type electric sorption cycle water treatment system according to claim 3, it is characterised in that also including the first butterfly
Valve, the terminal unit is connected to the body by the first butterfly valve.
5. Combined type electric sorption cycle water treatment system according to claim 3, it is characterised in that also including the second butterfly
Valve, the terminal unit is connected to the hydraulic turbine by the second butterfly valve.
6. the Combined type electric sorption cycle water treatment system according to claim 1 to 5 any one, it is characterised in that institute
The outlet and water inlet for stating terminal unit is respectively arranged with the 3rd butterfly valve and the 6th butterfly valve.
7. the Combined type electric sorption cycle water treatment system according to claim 1 to 5 any one, it is characterised in that institute
The water inlet for stating electro-adsorption hydrotreater is provided with the 4th butterfly valve.
8. the Combined type electric sorption cycle water treatment system according to claim 1 to 5 any one, it is characterised in that institute
Water filtering device is stated including water filtration sewage draining exit and first circulation pump, the water monitoring device is connected by water filtration sewage draining exit
To the first circulation pump, the first circulation pump is connected to the water circle device.
9. Combined type electric sorption cycle water treatment system according to claim 8, it is characterised in that the water filtering device
Also include the 5th butterfly valve, the first circulation pump is connected by the 5th butterfly valve with the water circle device.
10. the Combined type electric sorption cycle water treatment system according to claim 1 to 5 any one, it is characterised in that institute
Water circle device is stated including second circulation pump and the 3rd circulating pump, the water monitoring device is respectively by second circulation pump and the
Three circulating pumps are connected to terminal unit.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621070326.2U CN206127026U (en) | 2016-09-21 | 2016-09-21 | Combined type electro adsorption circulation water treatment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621070326.2U CN206127026U (en) | 2016-09-21 | 2016-09-21 | Combined type electro adsorption circulation water treatment system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206127026U true CN206127026U (en) | 2017-04-26 |
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ID=58570235
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621070326.2U Active CN206127026U (en) | 2016-09-21 | 2016-09-21 | Combined type electro adsorption circulation water treatment system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206127026U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113336372A (en) * | 2021-06-17 | 2021-09-03 | 桂林理工大学 | Domestic sewage purification treatment device and method |
-
2016
- 2016-09-21 CN CN201621070326.2U patent/CN206127026U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113336372A (en) * | 2021-06-17 | 2021-09-03 | 桂林理工大学 | Domestic sewage purification treatment device and method |
| CN113336372B (en) * | 2021-06-17 | 2022-08-16 | 桂林理工大学 | Domestic sewage purification treatment device and method |
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