CN207062052U - A kind of counter-infiltration ultrapure water production system - Google Patents
A kind of counter-infiltration ultrapure water production system Download PDFInfo
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- CN207062052U CN207062052U CN201720092807.1U CN201720092807U CN207062052U CN 207062052 U CN207062052 U CN 207062052U CN 201720092807 U CN201720092807 U CN 201720092807U CN 207062052 U CN207062052 U CN 207062052U
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- outlet pipe
- water
- counter
- infiltration
- filter
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Abstract
The utility model provides a kind of counter-infiltration ultrapure water production system, including raw water box, raw water pump, sandrock filter, active carbon filter, water softener, the cartridge filter being sequentially connected, the outlet pipe connection high-pressure pump of the cartridge filter, the outlet pipe connection counter-infiltration system of the high-pressure pump, it is characterised in that：The counter-infiltration system is made up of first-stage reverse osmosis device outlet pipe connection second level reverse osmosis apparatus water inlet pipe, the outlet pipe connection ultrapure water system of the counter-infiltration system, the pure water outlet pipe connection Primary UV line sterilizer of ultrapure water system, the outlet pipe connection abacterial water tank of Primary UV sterilizer, the outlet pipe connection carbon dioxide cleaner of abacterial water tank, the outlet pipe of carbon dioxide cleaner is by being sequentially connected two level ultraviolet sterilizer, post-filter, return duct, abacterial water tank after circulating pump, extraction water spot on the outlet pipe connected between post-filter and return duct.
Description
Technical field
Field of water treatment equipment is the utility model is related to, specifically a kind of counter-infiltration ultrapure water production system.
Background technology
In the preparation industry of cosmetics, water is as the integral component that most important solvent is cosmetics, and cosmetics category
In a kind of product for directly contacting human body skin, industry is ultra-pure water to the standard of water used for cosmetic, that is, is required leading in water
Dielectric is almost removed, while the colloidal substance not dissociated in water, gas and organic matter are removed to lower degree in the lump.Detection
Leading indicator be that the resistivity of water is more than 10-18M Ω .cm limiting values, but in general pure water equipment is difficult in industry at present
It is extremely low to produce ultra-pure water either producing water ratio, it is impossible to meet requirements at the higher level prepared by Cosmetic Manufacture.
The content of the invention
In view of the shortcomings of the prior art, the utility model provides a kind of counter-infiltration ultrapure water production system.
The technical solution of the utility model is：A kind of counter-infiltration ultrapure water production system, including be sequentially connected raw water box,
Raw water pump, sandrock filter, active carbon filter, water softener, cartridge filter, the outlet pipe connection of the cartridge filter are high
Press pump, the outlet pipe connection counter-infiltration system of the high-pressure pump, it is characterised in that：The counter-infiltration system is filled by first-stage reverse osmosis
Outlet pipe connection second level reverse osmosis apparatus water inlet pipe composition is put, the outlet pipe connection ultrapure water system of the counter-infiltration system, is surpassed
The pure water outlet pipe connection Primary UV line sterilizer of pure water system, the outlet pipe connection abacterial water tank of Primary UV sterilizer,
The outlet pipe connection carbon dioxide cleaner of abacterial water tank, the outlet pipe of carbon dioxide cleaner by be sequentially connected after circulating pump two level ultraviolet sterilizer,
Post-filter, return duct, abacterial water tank, extraction water spot on the outlet pipe connected between post-filter and return duct.
Described ultrapure water system includes electrodeionization module, the electrodeionization module both ends be respectively arranged with negative electrode and
Anode, the electrodeionization module connect dc source, the electrodeionization inside modules filling ion-exchange resin and electricity is gone
Ion inside modules are provided with cation-exchange membrane and anion-exchange membrane, cation-exchange membrane and the anion-exchange membrane phase
Mutually it is staggered and is cation-exchange membrane close to electrodeionization module negative electrode, is anion-exchange membrane close to anode, institute
State electrodeionization module both ends connection DC power supplier.
The first-stage reverse osmosis device uses artificial pellicle, and the artificial pellicle surface micropore a diameter of 0.5 ~
10mm。
The second level reverse osmosis apparatus uses artificial pellicle, and the artificial pellicle surface is positively charged.
The built-in filler lower floor of sandrock filter is water distribution quartz sand, and upper strata is purity quartzite.
The built-in filler lower floor of active carbon filter is water distribution quartz sand, and upper strata is cocoanut active charcoal.
The beneficial effects of the utility model are：
The utility model is provided with 2 grades of reverse osmosis units, 2 grades of ultraviolet sterilizers, the production water quality of pure water has been effectively ensured
Amount, while ultrapure water system is connected between counter-infiltration system and ultraviolet sterilizer, the ultrapure water system coupled ion is handed over
Technology and electrodialytic technique are changed, reaches the continuous purpose for producing high-quality pure water, production water purity is effectively improved, improves production water
Efficiency.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model,
Wherein, 1- raw water boxs, 2- raw water pumps, 3- sandrock filters, 4- active carbon filters, 5- water softeners, 6- ensured public security
Filter, 7- high-pressure pumps, 8- counter-infiltration systems, 9- ultrapure water systems, 10- Primary UV lines sterilizer, 11- abacterial water tanks, 12- are removed
Carbon device, 13- circulating pumps, 14- two levels ultraviolet sterilizer, 15- post-filters, 16- return ducts, 17- abacterial water tanks, 18- are used
Water spot.
Embodiment
Specific embodiment of the present utility model is described further below in conjunction with the accompanying drawings：
As shown in figure 1, a kind of counter-infiltration ultrapure water production system, including raw water box 1, raw water pump 2, the sandstone being sequentially connected
Filter 3, active carbon filter 4, water softener 5, cartridge filter 6, the outlet pipe connection high-pressure pump 7 of the cartridge filter 6,
The outlet pipe connection counter-infiltration system 8 of the high-pressure pump 7, it is characterised in that：The counter-infiltration system 8 is by first-stage reverse osmosis device
Outlet pipe connection second level reverse osmosis apparatus water inlet pipe composition, the outlet pipe connection ultrapure water system 9 of the counter-infiltration system 8, surpasses
The pure water outlet pipe connection Primary UV line sterilizer 10 of pure water system 9, the outlet pipe connection one-level of Primary UV sterilizer 10
Abacterial water tank 11, the outlet pipe connection carbon dioxide cleaner 12 of one-level abacterial water tank 11, the outlet pipe of carbon dioxide cleaner 12 by after circulating pump 13 according to
Secondary connection two level ultraviolet sterilizer 14, post-filter 15, return duct 16, two level abacterial water tank 17, post-filter 15 with
Extraction water spot 18 on the outlet pipe connected between return duct 16.
Described ultrapure water system 9 includes electrodeionization module, and the electrodeionization module both ends are respectively arranged with negative electrode
And anode, the electrodeionization module connect dc source, the electrodeionization inside modules filling ion-exchange resin and electricity
Deionization inside modules are provided with cation-exchange membrane and anion-exchange membrane, the cation-exchange membrane and anion-exchange membrane
It is interlaced setting and be cation-exchange membrane close to electrodeionization module negative electrode, be anion-exchange membrane close to anode,
The electrodeionization module both ends connect DC power supplier.
The first-stage reverse osmosis device uses artificial pellicle, and the artificial pellicle surface micropore a diameter of 0.5 ~
10mm。
The second level reverse osmosis apparatus uses artificial pellicle, and the artificial pellicle surface is positively charged.
The built-in filler lower floor of sandrock filter 3 is water distribution quartz sand, and upper strata is purity quartzite.
The built-in filler lower floor of active carbon filter 4 is water distribution quartz sand, and upper strata is cocoanut active charcoal.
The utility model carries out structure optimization to existing pure water equipment system, is provided with 2 grades of reverse osmosis units, 2 grades of purples
Outside line sterilizer, the production water quality of pure water is effectively ensured, while has connected between counter-infiltration system 8 and Primary UV sterilizer 10
Ultrapure water system 9, the coupled ion switching technology of ultrapure water system 9 and electrodialytic technique are connect, reaches and continuously produces high-quality
The purpose of pure water, production water purity is effectively improved, improve the efficiency of production water.
Simply illustrate principle of the present utility model and most preferred embodiment described in above-described embodiment and specification, do not taking off
On the premise of the spirit and scope of the utility model, the utility model also has various changes and modifications, these changes and improvements
Both fall within claimed the scope of the utility model.
Claims (5)
1. a kind of counter-infiltration ultrapure water production system, including raw water box, raw water pump, sandrock filter, the activated carbon being sequentially connected
Filter, water softener, cartridge filter, the outlet pipe connection high-pressure pump of the cartridge filter, the outlet pipe of the high-pressure pump
Connect counter-infiltration system, it is characterised in that：The counter-infiltration system connects two-pass reverse osmosis by first-stage reverse osmosis device outlet pipe
Device water inlet pipe forms, and the outlet pipe connection ultrapure water system of the counter-infiltration system, the pure water outlet pipe of ultrapure water system connects
Primary UV line sterilizer, the outlet pipe connection abacterial water tank of Primary UV sterilizer are connect, the outlet pipe connection of abacterial water tank removes
Carbon device, the outlet pipe of carbon dioxide cleaner is by being sequentially connected two level ultraviolet sterilizer, post-filter, return duct, sterile after circulating pump
Water tank, extraction water spot on the outlet pipe connected between post-filter and return duct；
Described ultrapure water system includes electrodeionization module, and the electrodeionization module both ends are respectively arranged with negative electrode and sun
Pole, the electrodeionization module connect dc source, the electrodeionization inside modules filling ion-exchange resin and electricity go from
Submodule is internally provided with cation-exchange membrane and anion-exchange membrane, and the cation-exchange membrane and anion-exchange membrane are mutual
It is staggered and is cation-exchange membrane close to electrodeionization module negative electrode, is anion-exchange membrane close to anode.
2. counter-infiltration ultrapure water production system according to claim 1, it is characterised in that：The first-stage reverse osmosis device is adopted
Manually pellicle, a diameter of 0.5 ~ 10mm of the artificial pellicle surface micropore.
3. counter-infiltration ultrapure water production system according to claim 1, it is characterised in that：The second level reverse osmosis apparatus is adopted
Manually pellicle, the artificial pellicle are the positively charged artificial pellicle in surface.
4. counter-infiltration ultrapure water production system according to claim 1, it is characterised in that：Loaded in the sandrock filter
Material lower floor is water distribution quartz sand, and upper strata is purity quartzite.
5. counter-infiltration ultrapure water production system according to claim 1, it is characterised in that：The active carbon filter is built-in
Filler lower floor is water distribution quartz sand, and upper strata is cocoanut active charcoal.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720092807.1U CN207062052U (en) | 2017-01-22 | 2017-01-22 | A kind of counter-infiltration ultrapure water production system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720092807.1U CN207062052U (en) | 2017-01-22 | 2017-01-22 | A kind of counter-infiltration ultrapure water production system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207062052U true CN207062052U (en) | 2018-03-02 |
Family
ID=61501741
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720092807.1U Expired - Fee Related CN207062052U (en) | 2017-01-22 | 2017-01-22 | A kind of counter-infiltration ultrapure water production system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207062052U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109879500A (en) * | 2019-03-27 | 2019-06-14 | 兆德（南通）电子科技有限公司 | A kind of Ultrapure water treatment technology |
| CN113912223A (en) * | 2020-07-07 | 2022-01-11 | 哈尔滨工业大学 | Step preparation system and method for pure water-ultrapure water |
-
2017
- 2017-01-22 CN CN201720092807.1U patent/CN207062052U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109879500A (en) * | 2019-03-27 | 2019-06-14 | 兆德（南通）电子科技有限公司 | A kind of Ultrapure water treatment technology |
| CN113912223A (en) * | 2020-07-07 | 2022-01-11 | 哈尔滨工业大学 | Step preparation system and method for pure water-ultrapure water |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180302 Termination date: 20220122 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |