CN216404145U - Reverse osmosis membrane penetrating fluid discharge system - Google Patents
Reverse osmosis membrane penetrating fluid discharge system Download PDFInfo
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- CN216404145U CN216404145U CN202123238721.0U CN202123238721U CN216404145U CN 216404145 U CN216404145 U CN 216404145U CN 202123238721 U CN202123238721 U CN 202123238721U CN 216404145 U CN216404145 U CN 216404145U
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Abstract
The utility model relates to the technical field of reverse osmosis membrane penetrating fluid discharge systems, in particular to a reverse osmosis membrane penetrating fluid discharge system which comprises a penetrating fluid collecting tank, a grid filtering tank, a first sedimentation tank, a liquid collecting tank, a micro-treatment tank, a second sedimentation tank, a hydrolysis acidification tank, an aeration tank, a disinfection tank, a clear water tank and a sludge tank, wherein the output end of the penetrating fluid collecting tank is connected to the first sedimentation tank, the output end of the first sedimentation tank is connected to the liquid collecting tank, the output end of the liquid collecting tank is connected to the micro-treatment tank, the output end of the micro-treatment tank is connected to the second sedimentation tank, the output end of the second sedimentation tank is connected to the hydrolysis acidification tank, the penetrating fluid collecting tank is convenient for collecting penetrating fluid in a centralized manner, then the penetrating fluid is guided into the grid filtering tank through a lifting pump, the penetrating fluid is primarily filtered through a grid filtering device, and the blockage of subsequent treatment caused by impurities in the penetrating fluid is avoided, then the penetrating fluid is led into the first sedimentation tank again, and the penetrating fluid is subjected to primary sedimentation treatment.
Description
Technical Field
The utility model relates to the technical field of reverse osmosis membrane penetrating fluid discharge systems, in particular to a reverse osmosis membrane penetrating fluid discharge system.
Background
The reverse osmosis system is widely applied to the water treatment industry, is used for removing most of salt-containing substances in water treatment, and has the advantages of environmental protection, economy, simple and convenient system and low consumption of chemical agents, so the reverse osmosis system is in a large-scale application trend in recent years.
However, the existing reverse osmosis membrane penetrating fluid has poor treatment effect in the discharging process, and the direct discharging easily causes pollution to the environment and the atmosphere.
SUMMERY OF THE UTILITY MODEL
Technical problem to be solved
In view of the deficiencies of the prior art, the present invention provides a reverse osmosis membrane permeate discharge system.
(II) technical scheme
In order to achieve the purpose, the utility model provides the following technical scheme: a reverse osmosis membrane penetrating fluid discharge system comprises a penetrating fluid collecting tank, a grid filter tank, a first sedimentation tank, a liquid collecting tank, a micro-treatment tank, a second sedimentation tank, a hydrolysis acidification tank, an aeration tank, a disinfection tank, a clean water tank and a sludge tank, wherein the penetrating fluid collecting tank output end is connected to the first sedimentation tank, the first sedimentation tank output end is connected to the liquid collecting tank, the liquid collecting tank output end is connected to the micro-treatment tank, the micro-treatment tank output end is connected to the second sedimentation tank, the second sedimentation tank output end is connected to the hydrolysis acidification tank, the hydrolysis acidification tank output end is connected to the aeration tank, the aeration tank output end is connected to the disinfection tank, the disinfection tank output end is connected to the clean water tank,
in order to improve the treatment effect of the first sedimentation tank, the utility model is improved in that a suspended substance collecting tank is arranged on one side of the first sedimentation tank, a classification treatment tank is arranged at one end of the suspended substance collecting tank, and the classification treatment tank is communicated with the suspended substance collecting tank.
In order to improve the treatment efficiency of the system, the utility model improves that one end of the first sedimentation tank is provided with a first sludge pump, one end of the second sedimentation tank is provided with a second sludge pump, and the first sludge pump and the second sludge pump are both communicated with the sludge tank.
In a further improvement of the utility model, a lift pump is arranged between the penetrating fluid collecting tank and the grid filtering tank.
Furthermore, the utility model is improved in that an aeration device is arranged in the aeration tank, and a plurality of disinfection devices are arranged in the disinfection tank.
Furthermore, the utility model improves that the first sedimentation tank and the second sedimentation tank are both inclined plate sedimentation tanks.
(III) advantageous effects
Compared with the prior art, the utility model provides a reverse osmosis membrane penetrating fluid discharge system, which has the following beneficial effects:
the reverse osmosis membrane penetrating fluid discharge system is characterized in that a penetrating fluid collecting tank is convenient to collect penetrating fluid, the penetrating fluid is guided into a grid filtering tank through a lifting pump, the penetrating fluid is preliminarily filtered through a grid filtering device, the penetrating fluid is prevented from being blocked by impurities in the penetrating fluid during subsequent treatment, then the penetrating fluid is guided into a first settling tank again, preliminary sedimentation treatment is carried out on the penetrating fluid, suspended substances generated by the penetrating fluid are collected through a suspended substance collecting tank and are subsequently classified and intensively treated through a classification treatment tank, sludge generated by the first settling tank is pumped into a sludge tank through a first sludge pump, the penetrating fluid after sedimentation is sequentially guided into a liquid collecting tank and a micro-treatment tank and then is guided into a second settling tank for secondary sedimentation, and sludge precipitated by the second settling tank is pumped into the sludge tank through a second sludge pump, the sludge is convenient to be treated in a centralized manner, the convenience is improved, penetrating fluid can be treated sequentially through the hydrolysis acidification tank, the aeration tank and the disinfection tank, is introduced into the clean water tank through aeration and disinfection, and is discharged after reaching the standard.
Drawings
FIG. 1 is a schematic structural view of the present invention;
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
Referring to fig. 1, a reverse osmosis membrane permeate discharging system comprises a permeate collecting tank, a grid filtering tank, a first sedimentation tank, a liquid collecting tank, a micro-treatment tank, a second sedimentation tank, a hydrolysis acidification tank, an aeration tank, a disinfection tank, a clean water tank and a sludge tank, wherein an output end of the permeate collecting tank is connected to the first sedimentation tank, an output end of the first sedimentation tank is connected to the liquid collecting tank, an output end of the liquid collecting tank is connected to the micro-treatment tank, an output end of the micro-treatment tank is connected to the second sedimentation tank, an output end of the second sedimentation tank is connected to the hydrolysis acidification tank, an output end of the hydrolysis acidification tank is connected to the aeration tank, an output end of the aeration tank is connected to the disinfection tank, an output end of the disinfection tank is connected to the clean water tank,
further, first sedimentation tank one side is provided with the suspended substance collecting pit, suspended substance collecting pit one end is provided with the classification pond, communicate with each other between classification pond and the suspended substance collecting pit, can carry out effectual processing to the suspended substance in the first sedimentation tank, improve the quality that the penetrant was handled.
Further, first sedimentation tank one end is provided with first sludge pump, second sedimentation tank one end is provided with the second sludge pump, first sludge pump and second sludge pump all communicate with each other with the sludge impoundment, are convenient for extract the mud in first sedimentation tank and the second sedimentation tank, make things convenient for the concentrated processing of mud.
Furthermore, a lifting pump is arranged between the penetrating fluid collecting tank and the grid filtering tank, so that the penetrating fluid can be conveniently guided into the grid filtering tank.
Furthermore, aeration devices are arranged in the aeration tank, and a plurality of disinfection devices are arranged in the disinfection tank, so that the treatment efficiency of penetrating fluid can be improved.
Further, first sedimentation tank and second sedimentation tank are the inclined plate sedimentation tank, can effectual improvement infiltration liquid efficiency and the effect of deposiing, and can be convenient for deposit mud and discharge, improve the convenience.
In summary, the operating principle and the operating process of the reverse osmosis membrane permeate discharging system are that, when in use, firstly the permeate collecting tank is convenient for collecting and storing the permeate, then the permeate is guided into the grid filtering tank by the lifting pump, the permeate is primarily filtered by the grid filtering device, so as to avoid the blockage of impurities in the permeate to subsequent treatment, then the permeate is guided into the first settling tank again, primary settling treatment is carried out on the permeate, suspended substances generated by the permeate are collected by the suspended substance collecting tank and are subsequently classified and concentrated by the classification treating tank, sludge generated by the first settling tank is pumped into the sludge tank by the first sludge pump, the permeate after the completion of the settling is guided into the liquid collecting tank and the micro-treating tank in sequence and then is guided into the second settling tank for secondary settling, and sludge settled by the second settling tank is pumped into the sludge tank by the second sludge pump, the reverse osmosis membrane penetrating fluid discharge system has the advantages of small occupied area, high treatment effect, low cost, high penetrating fluid treatment efficiency, no secondary pollution and strong practicability.
Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments 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 (6)
1. A reverse osmosis membrane permeate discharge system characterized by: including penetrant collecting tank, grid filtering ponds, first sedimentation tank, collecting tank, micro-processing pond, second sedimentation tank, hydrolysis acidification pool, aeration tank, disinfection pond, clean water basin and sludge impoundment, penetrant collecting tank output is connected to first sedimentation tank, first sedimentation tank output is connected to the collecting tank, the collecting tank output is connected to the micro-processing pond, micro-processing pond output is connected to the second sedimentation tank, second sedimentation tank output is connected to hydrolysis acidification pool, hydrolysis acidification pool output is connected to the aeration tank, the aeration tank output is connected to the disinfection pond, the disinfection pond output is connected to the clean water basin.
2. A reverse osmosis membrane permeate discharge system according to claim 1 wherein: the device comprises a first sedimentation tank, a suspended matter collecting tank, a classification treatment tank and a suspended matter collecting tank, wherein the suspended matter collecting tank is arranged on one side of the first sedimentation tank, the classification treatment tank is arranged at one end of the suspended matter collecting tank, and the classification treatment tank is communicated with the suspended matter collecting tank.
3. A reverse osmosis membrane permeate discharge system according to claim 1 wherein: first sedimentation tank one end is provided with first sludge pump, second sedimentation tank one end is provided with the second sludge pump, first sludge pump and second sludge pump all communicate with each other with the sludge impoundment.
4. A reverse osmosis membrane permeate discharge system according to claim 1 wherein: and a lifting pump is arranged between the penetrating fluid collecting tank and the grid filtering tank.
5. A reverse osmosis membrane permeate discharge system according to claim 1 wherein: the aeration tank is internally provided with an aeration device, and the disinfection tank is internally provided with a plurality of disinfection devices.
6. A reverse osmosis membrane permeate discharge system according to claim 1 wherein: the first sedimentation tank and the second sedimentation tank are both inclined plate sedimentation tanks.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202123238721.0U CN216404145U (en) | 2021-12-21 | 2021-12-21 | Reverse osmosis membrane penetrating fluid discharge system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202123238721.0U CN216404145U (en) | 2021-12-21 | 2021-12-21 | Reverse osmosis membrane penetrating fluid discharge system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN216404145U true CN216404145U (en) | 2022-04-29 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202123238721.0U Active CN216404145U (en) | 2021-12-21 | 2021-12-21 | Reverse osmosis membrane penetrating fluid discharge system |
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| CN (1) | CN216404145U (en) |
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2021
- 2021-12-21 CN CN202123238721.0U patent/CN216404145U/en active Active
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