CN216584443U - Melt and spout cloth pure water and stay level water processing system - Google Patents
Melt and spout cloth pure water and stay level water processing system Download PDFInfo
- Publication number
- CN216584443U CN216584443U CN202122761283.XU CN202122761283U CN216584443U CN 216584443 U CN216584443 U CN 216584443U CN 202122761283 U CN202122761283 U CN 202122761283U CN 216584443 U CN216584443 U CN 216584443U
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- water
- barrel
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- point
- pump
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 165
- 239000004744 fabric Substances 0.000 title claims abstract description 16
- 230000007246 mechanism Effects 0.000 claims abstract description 31
- 238000001914 filtration Methods 0.000 claims abstract description 27
- 238000005070 sampling Methods 0.000 claims abstract description 14
- 239000008399 tap water Substances 0.000 claims abstract description 11
- 235000020679 tap water Nutrition 0.000 claims abstract description 11
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 19
- 239000006004 Quartz sand Substances 0.000 claims description 14
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 14
- 238000007670 refining Methods 0.000 claims description 11
- 239000000498 cooling water Substances 0.000 claims description 10
- 230000008878 coupling Effects 0.000 claims description 3
- 238000010168 coupling process Methods 0.000 claims description 3
- 238000005859 coupling reaction Methods 0.000 claims description 3
- 230000000694 effects Effects 0.000 claims description 3
- 238000001223 reverse osmosis Methods 0.000 abstract description 18
- 239000002245 particle Substances 0.000 abstract description 12
- 238000011084 recovery Methods 0.000 abstract description 8
- 229910021642 ultra pure water Inorganic materials 0.000 description 8
- 239000012498 ultrapure water Substances 0.000 description 8
- 238000004519 manufacturing process Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 229910052799 carbon Inorganic materials 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 239000000463 material Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 239000004594 Masterbatch (MB) Substances 0.000 description 1
- 229920001410 Microfiber Polymers 0.000 description 1
- 241000700605 Viruses Species 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000004750 melt-blown nonwoven Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000003658 microfiber Substances 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000000271 synthetic detergent Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
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Abstract
The utility model provides a melt-blown fabric pure water stagewise water treatment system which comprises a raw water barrel, an RO (reverse osmosis) barrel and a point-of-use water barrel, wherein a primary filtering mechanism is arranged between the raw water barrel and the RO barrel, a secondary filtering mechanism is arranged between the RO barrel and the point-of-use water barrel, tap water in the raw water barrel effectively removes suspended matters and the like in water through the primary filtering mechanism, then reverse osmosis is carried out in the RO barrel to obtain RO pure water, and particles with the particle size of 0.01 mu m or more in water are filtered through the secondary filtering mechanism. Meanwhile, by selectively closing or opening the four joints of the four-way valve, the RO pure water subjected to reverse osmosis of the RO barrel can be sampled by one sampling valve or the water in the point-of-use water barrel can be sampled, the sampling structure of the system is simplified, and when the water sample is detected to be inconsistent, the water in the point-of-use water barrel can be conveyed to the RO barrel again through the recovery water barrel by the high-pressure pump for reverse osmosis, so that the water is recovered and reused.
Description
Technical Field
The utility model relates to the field of melt-blown fabric manufacturing, in particular to a melt-blown fabric pure water stagewise water treatment system.
Background
The meltblown fabric is a meltblown nonwoven fabric produced by drawing a polymer melt stream extruded from die orifices with a high velocity stream of hot air to form microfibers which are collected on a collecting screen or roller and bonded to itself. After the melt-blown cloth is formed, ultrapure water is sprayed to the base cloth added with the special water electret master batch, static electricity is generated through friction between water and the cloth surface, and thus the electret effect is achieved. Ultrapure water is generally filtered by tap water, the ultrapure water in the prior art has a complex structure and high manufacturing cost, and when the ultrapure water is unqualified, the ultrapure water is inconvenient to be reprocessed and cannot be recycled, so that the waste of water resources is caused.
SUMMERY OF THE UTILITY MODEL
The utility model provides a melt-blown pure water stagnating water treatment system to solve the problems that the structure of ultrapure water in the prior art is complex, the manufacturing cost is high, and when the ultrapure water is unqualified, the ultrapure water is inconvenient to be reprocessed.
The technical scheme adopted by the utility model for solving the technical problems is as follows: a melt-blown fabric pure water stagnating water treatment system comprises a raw water bucket, an RO bucket and a point-of-use water bucket, wherein a primary filtering mechanism is arranged between the raw water bucket and the RO bucket, and tap water in the raw water bucket enters the RO bucket after being filtered by the primary filtering mechanism; and a double-effect filtering mechanism is arranged between the RO barrel and the point-of-use bucket, and RO pure water discharged from the RO barrel enters the point-of-use bucket after being filtered by the double-effect filtering mechanism.
Further: the primary filter mechanism comprises a raw water pressure pump, a quartz sand filter and an activated carbon filter, tap water in the raw water barrel passes through the raw water pressure pump and is pumped into the quartz sand filter, a water outlet of the quartz sand filter is communicated with a water inlet of the activated carbon filter, and the quartz sand filter and the tap water filtered by the activated carbon filter are pumped into the RO barrel through the RO pump.
Further: the two-effect filtering mechanism comprises an RO water pressurizing pump and a refining filter, RO pure water in the RO barrel is pumped into the refining filter through the RO water pressurizing pump, and a water outlet of the refining filter is connected with the point-of-use water barrel.
Further: two imitate filter mechanism still includes sampling valve, hose, cross and retrieves the cask, be provided with the thief hatch on the point of use cask, the cross is connected respectively the delivery port of hose, sampling valve, RO bucket with the thief hatch, all be provided with the valve on four joints of cross, the other end of hose is connected with the high-pressure pump, the other end of high-pressure pump is connected retrieve the cask, and can with water pumping in the hose is delivered to in retrieving the cask, it passes through the tube coupling to retrieve the cask the RO bucket.
Further: the water pump is connected with the point of use bucket, the other end of the point of use water pump is connected with the cooling water bucket, and the point of use water pump can be with the water pump in the point of use bucket is delivered to in the cooling water bucket.
Further: the water treatment system is also provided with a drain pipe, overflow ports are arranged on the raw water bucket, the RO bucket, the using point bucket and the cooling water bucket, and the overflow ports are connected with the drain pipe.
The melt-blown cloth pure water stagnating water treatment system has the beneficial effects that the primary filtering mechanism and the secondary filtering mechanism are arranged, tap water in the raw water barrel effectively removes suspended matters, organic matters, colloidal particles and the like in water through the primary filtering mechanism, then reverse osmosis is carried out in the RO barrel to obtain RO pure water, and particles with the particle size of 0.01 mu m or more in water are filtered through the secondary filtering mechanism, so that pure water is obtained and sent to a pure water column pole for melt-blown cloth in a water barrel at a use point. Meanwhile, by selectively closing or opening the four joints of the four-way valve, the RO pure water subjected to reverse osmosis of the RO barrel can be sampled by one sampling valve or the water in the point-of-use water barrel can be sampled, the sampling structure of the system is simplified, and when the water sample is detected to be inconsistent, the water in the point-of-use water barrel can be conveyed to the RO barrel again through the recovery water barrel by the high-pressure pump for reverse osmosis, so that the water is recovered and reused.
Drawings
The utility model is further illustrated with reference to the following figures and examples.
FIG. 1 is a schematic diagram of a meltblown pure water staged water treatment system of the present invention.
In the figure, 1, a raw water barrel, 2, an RO water barrel, 3, a point-of-use water barrel, 4, a raw water pressure pump, 5, a quartz sand filter, 6, an activated carbon filter, 7, an RO water pressure pump, 8, a refining filter, 9, a sampling valve, 10, a hose, 11, a cross joint, 12, a recovery water barrel, 13, a sampling port, 14, a high-pressure pump, 15, a point-of-use water pump, 16, a cooling water barrel, 17, a drain pipe, 18, an overflow port, 20 and an RO pump.
Detailed Description
Reference will now be made in detail to embodiments of the present invention, examples of which are illustrated in the accompanying drawings, wherein like or similar reference numerals refer to the same or similar elements or elements having the same or similar function throughout. The embodiments described below with reference to the accompanying drawings are illustrative only for the purpose of explaining the present invention, and are not to be construed as limiting the present invention. On the contrary, the embodiments of the utility model include all changes, modifications and equivalents coming within the spirit and terms of the claims appended hereto.
In the description of the present invention, it is to be understood that the terms "center", "longitudinal", "lateral", "length", "width", "thickness", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", "axial", "radial", "circumferential", and the like, indicate orientations and positional relationships based on the orientations and positional relationships shown in the drawings, and are used merely for convenience of description and for simplicity of description, and do not indicate or imply that the device or element being referred to must have a particular orientation, be constructed and operated in a particular orientation, and therefore, should not be considered as limiting the present invention.
Furthermore, the terms "first," "second," and the like are used for descriptive purposes only and are not to be construed as indicating or implying relative importance. In the description of the present invention, it is to be noted that, unless otherwise explicitly specified or limited, the terms "connected" and "connected" are to be interpreted broadly, e.g., as being fixed or detachable or integrally connected; can be mechanically or electrically connected; may be directly connected or indirectly connected through an intermediate. The specific meanings of the above terms in the present invention can be understood in specific cases to those skilled in the art. In addition, in the description of the present invention, "a plurality" means two or more unless otherwise specified.
Any process or method descriptions in flow charts or otherwise described herein may be understood as representing modules, segments, or portions of code which include one or more executable instructions for implementing specific logical functions or steps of the process, and alternate implementations are included within the scope of the preferred embodiment of the present invention in which functions may be executed out of order from that shown or discussed, including substantially concurrently or in reverse order, depending on the functionality involved, as would be understood by those reasonably skilled in the art of the present invention.
As shown in fig. 1, the utility model provides a melt-blown fabric pure water stagnating water treatment system, which comprises a raw water barrel 1, an RO barrel 2 and a point-of-use water barrel 3, wherein a primary filtering mechanism is arranged between the raw water barrel 1 and the RO barrel 2, and tap water in the raw water barrel 1 enters the RO barrel 2 after being filtered by the primary filtering mechanism; and a double-effect filtering mechanism is arranged between the RO barrel 2 and the using point bucket 3, and RO pure water discharged from the RO barrel 2 enters the using point bucket 3 after being filtered by the double-effect filtering mechanism.
Tap water in the raw water barrel 1 is effectively removed of suspended matters, organic matters, colloidal particles and the like in water through a primary filtering mechanism, then reverse osmosis is carried out in an RO barrel 2 to obtain RO pure water, particles with the particle size of 0.01 mu m and above in water are filtered through a secondary filtering mechanism, and the pure water is sent to a pure water column pole of a using point water barrel 3 for melt-blown cloth.
The primary filter mechanism includes raw water force (forcing) pump 4, quartz sand filter 5 and active carbon filter 6, the running water warp in the raw water bucket 1 raw water force (forcing) pump 4 pump send extremely in the quartz sand filter 5, quartz sand filter 5's delivery port with the water inlet of active carbon filter 6 is linked together, process quartz sand filter 5 with running water after the active carbon filter 6 filters passes through RO pump 20 pump send extremely in the RO bucket 2. Suspended matters, organic matters, colloidal particles, microorganisms, chlorine, odor, partial heavy metal ions and the like in the water can be removed through the quartz sand filter 5; the activated carbon filter 6 can adsorb fine substances in various liquids to remove contaminants such as synthetic detergents, bacteria, viruses, and radioactivity.
The double-effect filtering mechanism comprises an RO water pressurizing pump 7 and a refining filter 8, RO pure water in the RO barrel 2 is pumped into the refining filter 8 through the RO water pressurizing pump 7, and a water outlet of the refining filter 8 is connected with the point-of-use water barrel 3. The refining filter 8 can remove water, oil mist and solid particles, and 100% of the particles with the particle size of 0.01 mu m or more.
Two effect filtering mechanism still includes sampling valve 9, hose 10, cross 11 and recovery cask 12, be provided with sample connection 13 on the use point cask 3, cross 11 connects respectively the delivery port of hose 10, sampling valve 9, RO bucket 2 with sample connection 13, all be provided with the valve on four joints of cross 11, the other end of hose 10 is connected with high-pressure pump 14, high-pressure pump 14's the other end is connected recovery cask 12, and can with water among the hose 10 is delivered to in the recovery cask 12, recovery cask 12 passes through the tube coupling RO bucket 2.
By selectively closing or opening the four joints of the four-way valve 11, one sampling valve 9 can sample RO pure water subjected to reverse osmosis of the RO barrel 2 or water in the point-of-use water barrel 3, the sampling structure of the system is simplified, and when the water sample is detected to be inconsistent, the water in the point-of-use water barrel 3 can be conveyed to the RO barrel 2 again through the recovery water barrel 12 for reverse osmosis by the high-pressure pump 14.
A point-of-use water pump 15 is connected to the point-of-use water bucket 3, a cooling water bucket 16 is connected to the other end of the point-of-use water pump 15, and the point-of-use water pump 15 can pump water in the point-of-use water bucket 3 into the cooling water bucket 16. The structure can recycle the waste water generated in the production process and the stationary stage.
The water treatment system is also provided with a drain pipe 17, overflow ports 18 are arranged on the raw water barrel 1, the RO barrel 2, the using point water barrel 3 and the cooling water barrel 16, and the overflow ports 18 are connected with the drain pipe 17. By arranging the overflow port 18, redundant water can be discharged when the water level reaches the upper limit, so that the water level height in each barrel body is controlled, and the safety of the system is improved.
In the description herein, references to the description of the term "one embodiment," "some embodiments," "an example," "a specific example," or "some examples," etc., mean that a particular feature, structure, material, or characteristic described in connection with the embodiment or example is included in at least one embodiment or example of the utility model. In this specification, a schematic representation of the term does not necessarily refer to the same embodiment or example. Furthermore, the particular features, structures, materials, or characteristics described may be combined in any suitable manner in any one or more embodiments or examples.
In light of the foregoing description of the preferred embodiment of the present invention, many modifications and variations can be made by the worker in the light of the above teachings without departing from the spirit of the utility model. The technical scope of the present invention is not limited to the content of the specification, and must be determined according to the scope of the claims.
Claims (6)
1. The utility model provides a melt-blown fabric pure water resides level water processing system which characterized in that: the RO water purifier comprises a raw water bucket (1), an RO bucket (2) and a point-of-use water bucket (3), wherein a primary filtering mechanism is arranged between the raw water bucket (1) and the RO bucket (2), and tap water in the raw water bucket (1) enters the RO bucket (2) after being filtered by the primary filtering mechanism; and a double-effect filtering mechanism is arranged between the RO barrel (2) and the using point bucket (3), and RO pure water discharged from the RO barrel (2) enters the using point bucket (3) after being filtered by the double-effect filtering mechanism.
2. The meltblown pure water staged water treatment system as recited in claim 1, further comprising: the primary filter mechanism comprises a raw water pressure pump (4), a quartz sand filter (5) and an activated carbon filter (6), tap water in a raw water barrel (1) passes through the raw water pressure pump (4) to be pumped into the quartz sand filter (5), a water outlet of the quartz sand filter (5) is communicated with a water inlet of the activated carbon filter (6), and the quartz sand filter (5) and tap water filtered by the activated carbon filter (6) are pumped into the RO barrel (2) through an RO pump (20).
3. The meltblown pure water staged water treatment system as recited in claim 1, further comprising: the double-effect filtering mechanism comprises an RO water pressurizing pump (7) and a refining filter (8), RO pure water in the RO barrel (2) is pumped into the refining filter (8) through the RO water pressurizing pump (7), and a water outlet of the refining filter (8) is connected with the point-of-use water barrel (3).
4. The meltblown pure water staged water treatment system as recited in claim 1, further comprising: two effect filtering mechanism still includes sampling valve (9), hose (10), cross (11) and retrieves cask (12), be provided with sample connection (13) on service point cask (3), cross (11) are connected respectively the delivery port of hose (10), sampling valve (9), RO bucket (2) with sample connection (13), all be provided with the valve on four connectors of cross (11), the other end of hose (10) is connected with high-pressure pump (14), the other end of high-pressure pump (14) is connected retrieve cask (12), and can with the water pump in hose (10) extremely in retrieving cask (12), retrieve cask (12) through the tube coupling RO bucket (2).
5. The meltblown pure water staged water treatment system as recited in claim 1, further comprising: the water pump is characterized in that a point-of-use water pump (15) is connected onto the point-of-use water bucket (3), the other end of the point-of-use water pump (15) is connected with a cooling water bucket (16), and the point-of-use water pump (15) can pump water in the point-of-use water bucket (3) into the cooling water bucket (16).
6. The meltblown pure water staged water treatment system as recited in claim 5, further comprising: the water treatment system is also provided with a drain pipe (17), overflow ports (18) are arranged on the raw water barrel (1), the RO barrel (2), the using point water barrel (3) and the cooling water barrel (16), and the overflow ports (18) are connected with the drain pipe (17).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN202122761283.XU CN216584443U (en) | 2021-11-11 | 2021-11-11 | Melt and spout cloth pure water and stay level water processing system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN202122761283.XU CN216584443U (en) | 2021-11-11 | 2021-11-11 | Melt and spout cloth pure water and stay level water processing system |
Publications (1)
Publication Number | Publication Date |
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CN216584443U true CN216584443U (en) | 2022-05-24 |
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Application Number | Title | Priority Date | Filing Date |
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CN202122761283.XU Expired - Fee Related CN216584443U (en) | 2021-11-11 | 2021-11-11 | Melt and spout cloth pure water and stay level water processing system |
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Country | Link |
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CN (1) | CN216584443U (en) |
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2021
- 2021-11-11 CN CN202122761283.XU patent/CN216584443U/en not_active Expired - Fee Related
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Granted publication date: 20220524 |