CN220317487U - Pressurized reverse osmosis water treatment device - Google Patents
Pressurized reverse osmosis water treatment device Download PDFInfo
- Publication number
- CN220317487U CN220317487U CN202321881505.4U CN202321881505U CN220317487U CN 220317487 U CN220317487 U CN 220317487U CN 202321881505 U CN202321881505 U CN 202321881505U CN 220317487 U CN220317487 U CN 220317487U
- Authority
- CN
- China
- Prior art keywords
- reverse osmosis
- centralized
- bin
- pipeline
- outlet pipe
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 76
- 238000001223 reverse osmosis Methods 0.000 title claims abstract description 57
- 239000012528 membrane Substances 0.000 claims abstract description 36
- 239000007788 liquid Substances 0.000 claims abstract description 33
- 230000007246 mechanism Effects 0.000 claims abstract description 14
- 239000012267 brine Substances 0.000 abstract description 11
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 abstract description 11
- 239000013505 freshwater Substances 0.000 abstract description 6
- 238000000926 separation method Methods 0.000 abstract description 4
- 235000017166 Bambusa arundinacea Nutrition 0.000 abstract description 2
- 235000017491 Bambusa tulda Nutrition 0.000 abstract description 2
- 241001330002 Bambuseae Species 0.000 abstract description 2
- 235000015334 Phyllostachys viridis Nutrition 0.000 abstract description 2
- 239000011425 bamboo Substances 0.000 abstract description 2
- 239000000243 solution Substances 0.000 description 7
- 238000000034 method Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 239000012466 permeate Substances 0.000 description 3
- 239000002904 solvent Substances 0.000 description 3
- 238000001179 sorption measurement Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 230000000903 blocking effect Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 230000004075 alteration Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- -1 i.e. Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000003204 osmotic effect Effects 0.000 description 1
- 238000000053 physical method Methods 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000005381 potential energy Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model belongs to the technical field of reverse osmosis water treatment, and particularly relates to a pressurized reverse osmosis water treatment device, which comprises: the device comprises a hollow centralized pipeline, wherein a centralized bin is arranged at one end of the centralized pipeline, an end cover is detachably connected to one side, away from the centralized pipeline, of the centralized bin, and a water outlet pipe is arranged on the end cover; reverse osmosis RO membrane cylinders are sequentially connected end to end in series, a reverse osmosis membrane cylinder group is formed between the reverse osmosis RO membrane cylinders, the reverse osmosis membrane cylinders are positioned in a centralized pipeline, a central pipe of the reverse osmosis membrane cylinder group is communicated with a water outlet pipe, and a high-concentration liquid outlet pipe is arranged on the lower surface of the centralized pipeline; one end of the centralized pipeline, which is far away from the centralized bin, is connected with a liquid inlet pipe, and a pressurizing mechanism is arranged on a pipeline of the liquid inlet pipe. Through the setting of centrifugal booster pump, will get into the intraductal water pressure boost of feed liquor to promote the quick separation processing of follow-up reverse osmosis RO membrane section of thick bamboo to water, obtain fresh water and brine.
Description
Technical Field
The utility model relates to the technical field of reverse osmosis water treatment, in particular to a pressurized reverse osmosis water treatment device.
Background
The water treatment modes comprise physical treatment and chemical treatment. The water treatment method for human has been quite a few years, and the physical method includes using various filter materials with different pore sizes, removing impurities in water by adsorption or blocking method, wherein the important adsorption method is to use activated carbon for adsorption, and the blocking method is to pass water through the filter materials to prevent the impurities with larger volume from passing through, so as to obtain cleaner water.
Reverse osmosis, also known as reverse osmosis, is a membrane separation operation that separates solvent from solution using pressure differential as the driving force. The feed liquid on one side of the membrane is pressurized and when the pressure exceeds its osmotic pressure, the solvent will reverse permeate against the natural direction of permeation. Thereby obtaining a permeate solvent, i.e., permeate, on the low pressure side of the membrane; the high pressure side gives a concentrated solution, i.e. a concentrate. If the seawater is treated by reverse osmosis, fresh water is obtained on the low pressure side of the membrane and brine is obtained on the high pressure side.
For reverse osmosis water treatment, water is pumped into a water storage tank with a higher position, the water level in the water storage tank is higher, the water flows under the action of gravity of the water, the water pressure is higher, the water enters a reverse osmosis filtering device, and the water is separated into fresh water and brine through the reverse osmosis filtering effect.
At present, the inflow water is generally introduced into a reverse osmosis filter device in a mode of converting gravitational potential energy of the water into kinetic energy, so that the water treatment is relatively slow due to insufficient water filtering pressure.
Disclosure of Invention
The present utility model is directed to a pressurized reverse osmosis water treatment device, which solves the above-mentioned problems of the prior art.
In order to achieve the above purpose, the present utility model provides the following technical solutions: a pressurized reverse osmosis water treatment device comprising:
the device comprises a hollow centralized pipeline, wherein a centralized bin is arranged at one end of the centralized pipeline, an end cover is detachably connected to one side, away from the centralized pipeline, of the centralized bin, and a water outlet pipe is arranged on the end cover;
reverse osmosis RO membrane cylinders are sequentially connected end to end in series, a reverse osmosis membrane cylinder group is formed between the reverse osmosis RO membrane cylinders, the reverse osmosis membrane cylinders are positioned in a centralized pipeline, a central pipe of the reverse osmosis membrane cylinder group is communicated with a water outlet pipe, and a high-concentration liquid outlet pipe is arranged on the lower surface of the centralized pipeline;
one end of the centralized pipeline, which is far away from the centralized bin, is connected with a liquid inlet pipe, and a pressurizing mechanism is arranged on a pipeline of the liquid inlet pipe.
Preferably, the water outlet pipe is movably inserted in the middle of the end cover, one end of the water outlet pipe extends into the centralized pipeline, a limit ring is arranged on the outer wall of the water outlet pipe, and the limit ring is positioned on the inner side of the centralized bin.
Preferably, the high-concentration liquid outlet pipe is positioned at one end of the concentration pipeline, which is close to the concentration bin.
Preferably, one end of the concentration pipeline far away from the concentration bin is provided with an arc temporary bin, and the diameter of the inner wall of the arc temporary bin is smaller than that of the outer wall of the reverse osmosis RO membrane cylinder.
Preferably, the pressurizing mechanism comprises a centrifugal booster pump, the liquid inlet pipe is connected with an outlet of the centrifugal booster pump, an input pipe is connected to an inlet of the centrifugal booster pump, a rotating shaft is connected to the lower side of an input shaft of the centrifugal booster pump, and one end of the rotating shaft is connected with a driving mechanism.
Preferably, the driving mechanism comprises a hollow impeller bin, one end of the rotating shaft extends into the impeller bin, one end of the rotating shaft, which is positioned in the impeller bin, is connected with an impeller, the high-concentration liquid outlet pipe is connected with a driving pipe through a joint, and the opposite side walls of the impeller bin are respectively provided with an impact port and a liquid outlet, and the driving pipe is connected with the impact port.
Preferably, a fixed support rod is connected between the outer wall of the centrifugal booster pump and the outer wall of the impeller bin.
The utility model provides a pressurized reverse osmosis water treatment device, which has at least the following beneficial effects compared with the prior art:
through the setting of centrifugal booster pump, will get into the intraductal water pressure boost of feed liquor to promote the quick separation processing of follow-up reverse osmosis RO membrane section of thick bamboo to water, obtain fresh water and brine.
Through the detachable connection mode of end cover, concentrated storehouse, the installation and the dismantlement effect of anti-cheating that pair of reverse osmosis RO membrane tube are used for depositing brine in the concentrated storehouse for the brine after the separation stays in concentrated storehouse, and exports through high concentration drain pipe.
Drawings
FIG. 1 is a schematic diagram of the structure of the present utility model;
FIG. 2 is a schematic view of the internal structure of the concentration duct and the concentration bin of the present utility model;
fig. 3 is a schematic diagram of the centrifugal booster pump, the input pipe, the impeller bin, the rotating shaft, the impeller and the liquid inlet pipe.
In the figure: 1. a centralized pipeline; 2. a centralized bin; 3. an end cap; 4. a water outlet pipe; 5. a limit ring; 6. a high-concentration liquid outlet pipe; 7. arc temporary storage bin; 8. a reverse osmosis RO membrane cartridge; 9. a centrifugal booster pump; 10. an input tube; 11. an impeller bin; 12. fixing the support rod; 13. a rotating shaft; 14. an impeller; 15. a liquid inlet pipe; 16. a joint; 17. and driving the pipe.
Detailed Description
The following description of the embodiments of the present utility model will be made clearly and completely with reference to the accompanying drawings, in which it is apparent that the embodiments described are only some embodiments of the present utility model, but not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the utility model without making any inventive effort, are intended to be within the scope of the utility model.
In the description of the present utility model, it should be understood that the terms "upper," "lower," "front," "rear," "left," "right," "top," "bottom," "inner," "outer," and the like indicate or are based on the orientation or positional relationship shown in the drawings, merely to facilitate description of the present utility model and to simplify the description, and do not indicate or imply that the devices or elements referred to must have a specific orientation, be configured and operated in a specific orientation, and thus should not be construed as limiting the present utility model.
Examples:
referring to fig. 1-3, the present utility model provides a technical solution: a pressurized reverse osmosis water treatment device comprising:
a hollow centralized pipeline 1, wherein a centralized bin 2 is arranged at one end of the centralized pipeline 1, an end cover 3 is detachably connected to one side, far away from the centralized pipeline 1, of the centralized bin 2, and a water outlet pipe 4 is arranged on the end cover 3;
the reverse osmosis RO membrane cylinders 8 are sequentially connected end to end, a reverse osmosis membrane cylinder group is formed between the reverse osmosis RO membrane cylinders 8, the reverse osmosis membrane cylinders 8 are positioned in the centralized pipeline 1, a central pipe of the reverse osmosis membrane cylinder group is communicated with the water outlet pipe 4, and a high-concentration water outlet pipe 6 is arranged on the lower surface of the centralized pipeline 1;
one end of the centralized pipeline 1 far away from the centralized bin 2 is connected with a liquid inlet pipe 15, and a pressurizing mechanism is arranged on a pipeline of the liquid inlet pipe 15.
When the device is used, water to be separated is input into the centralized pipeline 1 through the liquid inlet pipe 15, the reverse osmosis RO membrane cylinder 8 separates the entered water into fresh water and brine under the action of water pressure in the centralized pipeline 1, the fresh water enters the central pipe of the reverse osmosis RO membrane cylinder 8 and enters the water outlet pipe 4 from the central pipe to be discharged, and brine with higher salt content cannot enter the central pipe and flows out of the high-concentration liquid outlet pipe 6. The reverse osmosis RO membrane cartridge 8 adopts an existing reverse osmosis filter core, and is not described in detail here. The pressurizing mechanism pressurizes the water entering the liquid inlet pipe 15 so that the water enters the liquid inlet pipe as high-pressure water.
Referring to fig. 1-3, the present utility model provides a technical solution: the water outlet pipe 4 is movably inserted in the middle of the end cover 3, one end of the water outlet pipe 4 extends into the centralized pipeline 1, a limit ring 5 is arranged on the outer wall of the water outlet pipe 4, and the limit ring 5 is positioned on the inner side of the centralized bin 2.
When in use, the water outlet pipe 4 is limited on the end cover 3 by the setting of the limit ring 5, so that the water outlet pipe 4 cannot be separated from the end cover 3. The water outlet pipe 4 and the end cover 3 are movably connected, and the water outlet pipe 4 is propped against each other after being contacted with the central pipe, so that the connection is stable. If the water outlet pipe 4 and the end cover 3 are fixedly connected, the water outlet pipe 4 and the reverse osmosis RO membrane cylinder 8 are not easy to be connected in a fine adjustment way.
Referring to fig. 1-3, the present utility model provides a technical solution: the high-concentration liquid outlet pipe 6 is positioned at one end of the concentration pipeline 1 close to the concentration bin 2. One end of the concentration pipeline 1 far away from the concentration bin 2 is provided with an arc temporary storage bin 7, and the diameter of the inner wall of the arc temporary storage bin 7 is smaller than that of the outer wall of the reverse osmosis RO membrane cylinder 8.
The arc temporary storage bin 7 is arranged, so that water entering the centralized pipeline 1 through the liquid inlet pipe 15 is firstly distributed to the arc temporary storage bin 7, and then uniformly distributed to all parts in the reverse osmosis RO membrane cylinder 8 from the arc temporary storage bin 7.
Referring to fig. 1-3, the present utility model provides a technical solution: the pressurizing mechanism comprises a centrifugal booster pump 9, the liquid inlet pipe 15 is connected with an outlet of the centrifugal booster pump 9, an input pipe 10 is connected to an inlet of the centrifugal booster pump 9, a rotating shaft 13 is connected to the lower side of an input shaft of the centrifugal booster pump 9, and one end of the rotating shaft 13 is connected with a driving mechanism. The driving mechanism comprises a hollow impeller bin 11, one end of a rotating shaft 13 extends into the impeller bin 14, one end of the rotating shaft 13 positioned in the impeller bin 11 is connected with an impeller 14, a high-concentration liquid outlet pipe 6 is connected with a driving pipe 17 through a joint 16, impact ports and liquid outlet ports are respectively formed in two opposite side walls of the impeller bin 11, and the driving pipe 17 is connected with the impact ports. A fixed support rod 12 is connected between the outer wall of the centrifugal booster pump 9 and the outer wall of the impeller bin 11.
Brine output from the high-concentration liquid outlet pipe 6 enters the impeller bin 11 through the driving pipe 17, in the impeller bin 11, the brine pushes the impeller bin 14, so that the impeller bin 14 rotates, the impeller bin 14 drives a centrifugal pump wheel in the centrifugal booster pump 9 to rotate through the rotating shaft 13, water entering the centrifugal booster pump 9 is pressurized, and the pressurized water enters the centralized pipeline 1 through the liquid inlet pipe 15. The centrifugal booster pump 9 is not driven by a motor, and the centrifugal pump wheel is driven to rotate by brine, so that the booster effect is achieved.
While the fundamental and principal features of the utility model and advantages of the utility model have been shown and described, it will be apparent to those skilled in the art that the utility model is not limited to the details of the foregoing exemplary embodiments, but may be embodied in other specific forms without departing from the spirit or essential characteristics thereof; the present embodiments are therefore to be considered in all respects as illustrative and not restrictive, the scope of the utility model being indicated by the appended claims rather than by the foregoing description, and all changes which come within the meaning and range of equivalency of the claims are therefore intended to be embraced therein.
Although embodiments of the present utility model have been shown and described, it will be understood by those skilled in the art that various changes, modifications, substitutions and alterations can be made therein without departing from the principles and spirit of the utility model, the scope of which is defined in the appended claims and their equivalents.
Claims (7)
1. A pressurized reverse osmosis water treatment device, comprising:
the centralized pipeline (1) is hollow, one end of the centralized pipeline (1) is provided with a centralized bin (2), one side, far away from the centralized pipeline (1), of the centralized bin (2) is detachably connected with an end cover (3), and the end cover (3) is provided with a water outlet pipe (4);
reverse osmosis RO membrane cylinders (8) are sequentially connected in series from end to end, a reverse osmosis membrane cylinder group is formed between the reverse osmosis RO membrane cylinders (8), the reverse osmosis RO membrane cylinders (8) are positioned in a centralized pipeline (1), a central pipe of the reverse osmosis membrane cylinder group is communicated with a water outlet pipe (4), and a high-concentration water outlet pipe (6) is arranged on the lower surface of the centralized pipeline (1);
one end of the centralized pipeline (1) far away from the centralized bin (2) is connected with a liquid inlet pipe (15), and a pressurizing mechanism is arranged on a pipeline of the liquid inlet pipe (15).
2. A pressurized reverse osmosis water treatment device according to claim 1, characterized in that: the water outlet pipe (4) is movably inserted in the middle of the end cover (3), one end of the water outlet pipe (4) extends into the centralized pipeline (1), a limit ring (5) is arranged on the outer wall of the water outlet pipe (4), and the limit ring (5) is positioned on the inner side of the centralized bin (2).
3. A pressurized reverse osmosis water treatment device according to claim 1, characterized in that: the high-concentration liquid outlet pipe (6) is positioned at one end of the concentration pipeline (1) close to the concentration bin (2).
4. A pressurized reverse osmosis water treatment device according to claim 1, characterized in that: one end of the concentration pipeline (1) far away from the concentration bin (2) is provided with an arc temporary storage bin (7), and the diameter of the inner wall of the arc temporary storage bin (7) is smaller than that of the outer wall of the reverse osmosis RO membrane cylinder (8).
5. A pressurized reverse osmosis water treatment device according to claim 1, characterized in that: the centrifugal booster pump is characterized in that the booster mechanism comprises a centrifugal booster pump (9), a liquid inlet pipe (15) is connected with an outlet of the centrifugal booster pump (9), an input pipe (10) is connected to an inlet of the centrifugal booster pump (9), a rotating shaft (13) is connected to the lower side of an input shaft of the centrifugal booster pump (9), and a driving mechanism is connected to one end of the rotating shaft (13).
6. A pressurized reverse osmosis water treatment apparatus according to claim 5, further comprising: the driving mechanism comprises a hollow impeller bin (11), one end of a rotating shaft (13) extends into the impeller bin (11), one end of the rotating shaft (13) located in the impeller bin (11) is connected with an impeller (14), a high-concentration liquid outlet pipe (6) is connected with a driving pipe (17) through a joint (16), and an impact port and a liquid outlet are respectively formed in two opposite side walls of the impeller bin (11), and the driving pipe (17) is connected with the impact port.
7. A pressurized reverse osmosis water treatment device according to claim 6, characterized in that: a fixed supporting rod (12) is connected between the outer wall of the centrifugal booster pump (9) and the outer wall of the impeller bin (11).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202321881505.4U CN220317487U (en) | 2023-07-18 | 2023-07-18 | Pressurized reverse osmosis water treatment device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202321881505.4U CN220317487U (en) | 2023-07-18 | 2023-07-18 | Pressurized reverse osmosis water treatment device |
Publications (1)
Publication Number | Publication Date |
---|---|
CN220317487U true CN220317487U (en) | 2024-01-09 |
Family
ID=89411909
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202321881505.4U Active CN220317487U (en) | 2023-07-18 | 2023-07-18 | Pressurized reverse osmosis water treatment device |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN220317487U (en) |
-
2023
- 2023-07-18 CN CN202321881505.4U patent/CN220317487U/en active Active
Similar Documents
Publication | Publication Date | Title |
---|---|---|
WO2009062364A1 (en) | A seawater desalination system using cavitating jet technique | |
CN112221193A (en) | Chinese-medicinal material draws equipment based on ceramic membrane is concentrated | |
CN220317487U (en) | Pressurized reverse osmosis water treatment device | |
CN210001679U (en) | Full-film micro-concentrated water nanofiltration machine | |
CN218539373U (en) | High-efficient pure water preparation device | |
CN208594140U (en) | A kind of high-performance ultrafiltration membrane treatment appts of micro-polluted surface water | |
CN101665292B (en) | Purification treatment technique of drinking water and treatment system thereof | |
CN207062089U (en) | A kind of full-automatic nanofiltration and counter-infiltration sewage disposal system | |
CN201424393Y (en) | Seawater desalinization device | |
CN201770562U (en) | Recovery combination processing system for confecting polymer of produced wastewater | |
CN206590989U (en) | A kind of counter-infiltration sewage disposal device | |
CN212833089U (en) | Reverse osmosis device for industrial pure water | |
CN205687675U (en) | Reverse osmosis membrane brackish water desalination system | |
CN208471614U (en) | One kind being used for production of instant tea reverse osmosis membrane unit | |
CN214653998U (en) | Two-stage reverse osmosis water purifier | |
CN217340844U (en) | Ultralow-pressure large-flux reverse osmosis membrane device | |
CN204307531U (en) | A kind of eccentric rotary film filter | |
CN209815819U (en) | Pure water making system of waste water high pressure protection | |
CN104492271B (en) | A kind of eccentric rotary film filter | |
CN216303466U (en) | Waste water reverse osmosis treatment device for treating phthalic acid by using biological activated carbon | |
CN206395882U (en) | One kind dialysis water treatment system | |
CN208667181U (en) | A kind of reverse osmosis wastewater treatment equipment | |
CN219098943U (en) | Tubular ultrafiltration membrane filter assembly | |
CN215102152U (en) | High salt waste water reverse osmosis membrane dense water treatment facilities that contains | |
CN201512444U (en) | Purification treatment system for drinking water |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant |