CN205933456U - Straight drinking water system of full embrane method - Google Patents
Straight drinking water system of full embrane method Download PDFInfo
- Publication number
- CN205933456U CN205933456U CN201620792922.5U CN201620792922U CN205933456U CN 205933456 U CN205933456 U CN 205933456U CN 201620792922 U CN201620792922 U CN 201620792922U CN 205933456 U CN205933456 U CN 205933456U
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- water
- reverse osmosis
- osmosis membrane
- water tank
- embrane method
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Abstract
The utility model provides a straight drinking water system of full embrane method, includes the water consuming point of the former water tank of establishing ties in proper order through the pipeline, raw water pump, ultrafiltration system, middle water tank, high -pressure pump, reverse osmosis membrane, pure water case and straight drinking water the raw water pump with be provided with between the ultrafiltration system and be used for the protection the disc filter of ultrafiltration system, be provided with in the ultrafiltration system and be used for the protection reverse osmosis membrane's milipore filter middle water tank with be provided with between the high -pressure pump and be used for the protection reverse osmosis membrane's antisludging agent device the ultrafiltration system with the last online chemical cleaning device that sets up respectively or share of reverse osmosis membrane. The utility model has the advantages of simple structure, it is few that the number of times is changed to the consumptive material, reverse osmosis membrane long service life, whole system later stage operating cost low grade advantage.
Description
Technical field
The utility model is related to direct drinking process field, more particularly, to a kind of full embrane method drinking water system.
Background technology
With the fast development of modern science and technology, people send out for the requirement more and more higher of living standard quality, industry simultaneously
Exhibition is more serious to water pollution, and water environment goes from bad to worse and leads to the water process of routine cannot go the harmful components in eliminating water completely,
Have a strong impact on the healthy of people.Direct drinking is with municipal tap water after the purification of special process advanced treating, then through smelly
It is sealed in container after oxygen mixing and does not contain any additive, then make water quality reach country by ultraviolet disinfection and drink water gauge
Standard, is then delivered directly to each using food-grade independent tubes and drinks a little, allows the use high-quality that people trusts and can be direct
The water drunk.Raw water, after the purification of special process advanced treating, removes former Organic substance in water, bacterium and virus, retains in water
It is beneficial to the trace element of human body, exports the water can directly drinking raw to user, the water water source of direct drinking is different, in national standard
Under, various available water water sources all can be fabricated to direct drinking as the raw water of direct drinking after carrying out advanced treating.
It is all carbon filter and sand filtration currently used for filter preliminary in the system of manufacture direct drinking, using this traditional mistake
Filter device, needs consumptive material is regularly replaced, complex operation in operation, affects operating efficiency, at reverse osmosis membrane
During reason, lack device and anti-seepage membrane is protected, cause reverse osmosis membrane permanent damage, traditional drinking water system needs fixed
Phase is changed to PP cotton in cartridge filter, complex operation.
In view of above-mentioned defect, the design people, actively research and innovation in addition, to founding a kind of one kind of new structure
Full embrane method drinking water system is so as to have more the value in life.
Content of the invention
For solving above-mentioned technical problem, the utility model purpose is to provide a kind of full embrane method drinking water system, to solve
Consumptive material of the prior art is changed often, and reverse osmosis membrane is fragile, the loaded down with trivial details problem of complex operation.
A kind of full embrane method drinking water system of the present utility model, including the raw water box being sequentially connected in series by pipeline, raw water pump,
The use water spot of ultrafiltration system, intermediate water tank, high-pressure pump, reverse osmosis membrane, pure water tank and direct drinking it is characterised in that:Described former
It is provided with the disc filter for protecting described ultrafiltration system between water pump and described ultrafiltration system, set in described ultrafiltration system
It is equipped with the milipore filter for protecting described reverse osmosis membrane, be provided with for protecting between described intermediate water tank and described high-pressure pump
The antisludging agent device of described reverse osmosis membrane, is respectively provided with or shares one online on described ultrafiltration system and described reverse osmosis membrane
Chemically-cleaning device.
Further, described reverse osmosis membrane water side is respectively arranged with pure water outlet and concentrated water outlet.
Further, described intermediate water tank is provided with refluxing opening, described refluxing opening is connected to described concentrated water outlet.
Further, described milipore filter is provided with automatic flushing device, there is automatic cleaning function.
Further, it is provided with ozone disinfection system in described pure water tank.
Further, described pure water tank and described with being provided with ultraviolet sterilizer between water spot.
By such scheme, the utility model at least has advantages below:
1st, adopt disc filter to replace traditional sand filtration and carbon filter, reduce the replacing of consumptive material during using, operation is more
Plus simple, and 5 μm of granule foreign can be prevented from exceeding enter milipore filter, cause the permanent damage to milipore filter, improve
The service life of milipore filter.
2nd, disc filter filter process is precisely efficient, standardized module, effectively saves and takes up room, has and automatically go out
Water, continuous effluent characteristic, filters and backwash effect will not be deteriorated because of use time, and long service life, using process stabilization.
3rd, milipore filter can effectively prevent from exceeding 0.01 μm of granule foreign entrance reverse osmosis membrane, causes to reverse osmosis membrane forever
Property is damaged long, thus protecting reverse osmosis membrane, adding antisludging agent in pipeline before high-pressure pump can effectively prevent the calcium ions and magnesium ions in water
The dirty stifled reverse osmosis membrane of fouling, extends the life-span of reverse osmosis membrane, and then reaches the effect of operation steady in a long-term.
4th, milipore filter can realize auto-flushing, by automatic flushing device, make in intermediate water tank clear water from produce water channel to
Concentrated water road reverse flow, realizes the anti-cleaning process of milipore filter;By running status, milipore filter is cleaned up, realize milipore filter
Just washed journey;Using medicament, Chemical cleaning is carried out to concentrated water road and film silk surface, realize the wash cycles process of milipore filter;With clear
Water cleans the medicament retaining in milipore filter and detergent line, and cleaning terminates, and the cleaning fluid emptying in pipeline and purge tank completes
Cleaning, is cleaned by automatic, can effectively prevent the loaded down with trivial details, greatly of PP cotton in periodic replacement cartridge filter in conventional solution
Reduce greatly the later stage running cost of whole system.
5th, different filters is organically combined by the utility model, can be applied to the raw water of separate sources
Process, produce the direct drinking meeting sanitary grade, be provided with ozone disinfection system and ultraviolet disinfection simultaneously before EXIT POINT
Device, ultraviolet mainly has sterilization, degrade TOC and abolish the effect such as ozone it is ensured that direct drinking fresh and healthy with water spot.
Described above is only the general introduction of technical solutions of the utility model, in order to better understand skill of the present utility model
Art means, and being practiced according to the content of specification, below with preferred embodiment of the present utility model and coordinate accompanying drawing detailed
Describe in detail bright as after.
Brief description
Fig. 1 is process flow diagram of the present utility model, and the in figure direction of arrow represents water (flow) direction, and rectangle frame represents each
Device, adopts pipeline to be connected in series between each device.
Specific embodiment
With reference to the accompanying drawings and examples, specific embodiment of the present utility model is described in further detail.Below
Embodiment is used for the utility model is described, but is not limited to scope of the present utility model.
As shown in figure 1, a kind of full embrane method drinking water system, including the raw water box being sequentially connected in series by pipeline, raw water pump, surpass
The use water spot of filter system, intermediate water tank, high-pressure pump, reverse osmosis membrane, pure water tank and direct drinking it is characterised in that:In described raw water
It is provided with the disc filter for protecting described ultrafiltration system between pump and described ultrafiltration system, arrange in described ultrafiltration system
There is the milipore filter for protecting described reverse osmosis membrane, be provided with for protecting between described intermediate water tank and described high-pressure pump
State the antisludging agent device of reverse osmosis membrane, described ultrafiltration system and described reverse osmosis membrane are respectively provided with or share onlineization
Learn cleaning device.
Disc filter is formed by filter element parallel combinations, and its filter element is mainly by the ring of one group of with groove or rib
Shape reinforced plastics filter disc is constituted.During filtration, sewage enters from raw water box, and the wheel rim that the groove seamed edge on adjacent filter disc is formed is water
In granule foreign more than 5 μm be retained down;During backwash, water, from outside ring-type disc interiors flow direction, will be trapped on filter disc
Wash dirt gets off, and discharges through sewage draining exit.Disc filter, for long service life, reduces the replacing of consumptive material during using, behaviour
Make simple.Disc filter filter process is precisely efficient, standardized module, effectively saves and takes up room, has full-automatic water outlet,
Continuous effluent characteristic, filters and backwash effect will not be deteriorated because of use time, using process stabilization.
The granule foreign that milipore filter can effectively prevent from exceeding 0.01 μm enters reverse osmosis membrane, causes permanent to reverse osmosis membrane
Property damage, thus protecting reverse osmosis membrane, in pipeline before high-pressure pump plus antisludging agent can effectively prevent the calcium ions and magnesium ions in water from tying
The dirty stifled reverse osmosis membrane of dirt, extends the life-span of reverse osmosis membrane, and then reaches the effect of operation steady in a long-term.Milipore filter can be realized certainly
Dynamic flushing, by automatic flushing device, makes clear water from producing water channel to concentrated water road reverse flow, realizes the counter of milipore filter and cleaned
Journey;By running status, milipore filter is cleaned up, realize the just washed journey of milipore filter;Using medicament to concentrated water road and film silk surface
Carry out Chemical cleaning, realize the wash cycles process of milipore filter;With the medicament retaining in clean water milipore filter and detergent line,
Cleaning terminates, and the cleaning fluid emptying in pipeline and purge tank completes to clean, is cleaned by automatic, can effectively prevent tradition
In periodic replacement cartridge filter in technical scheme, PP cotton is loaded down with trivial details, greatly reduces the later stage running cost of whole system.
Operation principle of the present utility model is as follows:
The raw water of separate sources stores in raw water box, under raw water pump driving effect, is carried out just by disc filter
Step is processed, and, as the pretreatment of ultrafiltration system, the raw water after preliminary treatment passes through ultrafiltration system to get rid of large particulate matter in water
It is further processed, remaining most of organic matter in water, suspension, colloid and microorganism are got rid of in ultrafiltration, former after process
Water is stored in intermediate water tank and carries out final process through the driving effect of high-pressure pump by reverse osmosis membrane, pipeline before high-pressure pump
In be provided with antisludging agent, prevent the dirty stifled reverse osmosis membrane of calcium ions and magnesium ions fouling in water, carry out advanced desalination through reverse osmosis membrane,
Process the pure water producing eventually to be stored in pure water tank, the concentrated water of generation is back to do in intermediate water tank through pipeline to be located further
Reason, after the pure water of generation entered ozone disinfection system and ultraviolet sterilizer disinfects, is pumped into each using water spot through pure water.
The above is only preferred embodiment of the present utility model, be not limited to the utility model it is noted that
For those skilled in the art, on the premise of without departing from the utility model know-why, can also do
Go out some improvement and modification, these improve and modification also should be regarded as protection domain of the present utility model.
Claims (6)
1. a kind of full embrane method drinking water system, including the raw water box being sequentially connected in series by pipeline, raw water pump, ultrafiltration system, centre
The use water spot of water tank, high-pressure pump, reverse osmosis membrane, pure water tank and direct drinking it is characterised in that:In described raw water pump and described ultrafiltration
It is provided with the disc filter for protecting described ultrafiltration system between system, be provided with for protecting in described ultrafiltration system
State the milipore filter of reverse osmosis membrane, be provided between described intermediate water tank and described high-pressure pump for protecting described reverse osmosis membrane
Antisludging agent device, is respectively provided with described ultrafiltration system and described reverse osmosis membrane or shares an in-site chemical cleaning device.
2. a kind of full embrane method drinking water system according to claim 1 it is characterised in that:Described reverse osmosis membrane water side is divided
It is not provided with pure water outlet and concentrated water outlet.
3. a kind of full embrane method drinking water system according to claim 2 it is characterised in that:It is provided with described intermediate water tank
Refluxing opening, described refluxing opening is connected to described concentrated water outlet.
4. a kind of full embrane method drinking water system according to claim 1 it is characterised in that:It is provided with described milipore filter certainly
Dynamic cleaning device, has automatic cleaning function.
5. a kind of full embrane method drinking water system according to claim 1 it is characterised in that:It is provided with smelly in described pure water tank
Oxygen decontamination system.
6. a kind of full embrane method drinking water system according to claim 1 it is characterised in that:Described pure water tank and described use water
It is provided with ultraviolet sterilizer between point.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201620792922.5U CN205933456U (en) | 2016-07-27 | 2016-07-27 | Straight drinking water system of full embrane method |
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CN201620792922.5U CN205933456U (en) | 2016-07-27 | 2016-07-27 | Straight drinking water system of full embrane method |
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CN201620792922.5U Expired - Fee Related CN205933456U (en) | 2016-07-27 | 2016-07-27 | Straight drinking water system of full embrane method |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107746129A (en) * | 2017-11-06 | 2018-03-02 | 江苏天雨环保集团有限公司 | Integrated Treated sewage reusing and pure water equipment |
CN107789989A (en) * | 2017-11-24 | 2018-03-13 | 内蒙古农业大学 | A kind of preventative method for disinfection of reverse osmosis membrane whole process |
CN109851119A (en) * | 2019-04-09 | 2019-06-07 | 南京慧城水处理设备有限公司 | Small-sized concentration water purification system |
-
2016
- 2016-07-27 CN CN201620792922.5U patent/CN205933456U/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107746129A (en) * | 2017-11-06 | 2018-03-02 | 江苏天雨环保集团有限公司 | Integrated Treated sewage reusing and pure water equipment |
CN107789989A (en) * | 2017-11-24 | 2018-03-13 | 内蒙古农业大学 | A kind of preventative method for disinfection of reverse osmosis membrane whole process |
CN107789989B (en) * | 2017-11-24 | 2021-06-01 | 内蒙古农业大学 | Reverse osmosis membrane full-process preventive sterilization method |
CN109851119A (en) * | 2019-04-09 | 2019-06-07 | 南京慧城水处理设备有限公司 | Small-sized concentration water purification system |
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Legal Events
Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170208 Termination date: 20180727 |