CN213895452U - A kind of magnesium aluminum silicate production wastewater recycling system - Google Patents
A kind of magnesium aluminum silicate production wastewater recycling system Download PDFInfo
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- CN213895452U CN213895452U CN202022818688.8U CN202022818688U CN213895452U CN 213895452 U CN213895452 U CN 213895452U CN 202022818688 U CN202022818688 U CN 202022818688U CN 213895452 U CN213895452 U CN 213895452U
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Abstract
本实用新型公开了一种硅酸镁铝生产废水回收利用系统，包括混凝气浮过滤器，混凝气浮过滤器的一侧连通有第三出水管，第三出水管另一端连通有增压泵，增压泵远离第三出水管的一侧连通有第二连通管，第二连通管的另一端连通有砂滤罐，砂滤罐的底部连通有第五连接管，第五连接管另一端连通有精密过滤器，精密过滤器远离第五连接管一侧的底部连通有第四连接管。通过设置混凝气浮过滤器，在污水经混凝气浮过滤器过滤后，经过增压泵加压后通过第二连接管进入砂滤罐过滤后，污水进入精密过滤器过滤后连通至超滤器，第一原水罐过滤液进入高浓度反渗透过滤器过滤后，完善了净化利用流程，提升了环保效率。
The utility model discloses a magnesium-aluminum silicate production wastewater recycling system, comprising a coagulation air flotation filter, one side of the coagulation air flotation filter is connected with a third water outlet pipe, and the other end of the third water outlet pipe is connected with an increasing The pressure pump, the side of the booster pump away from the third water outlet pipe is communicated with a second communication pipe, the other end of the second communication pipe is communicated with a sand filter tank, and the bottom of the sand filter tank is communicated with a fifth connection pipe, and the fifth connection pipe The other end is connected with a precision filter, and the bottom of the side of the precision filter away from the fifth connecting pipe is connected with a fourth connecting pipe. By setting the coagulation air flotation filter, after the sewage is filtered by the coagulation air flotation filter, after being pressurized by the booster pump, it enters the sand filter tank through the second connecting pipe for filtration, and the sewage enters the precision filter and is connected to the ultra-high After the filtrate of the first raw water tank enters the high-concentration reverse osmosis filter for filtration, the purification and utilization process is improved and the environmental protection efficiency is improved.
Description
Technical Field
The utility model belongs to the technical field of sewage treatment, concretely relates to magnesium aluminum silicate waste water recycle system.
Background
Sewage treatment: the sewage is purified to reach the water quality requirement of being discharged into a certain water body or being reused. Sewage treatment is widely applied to various fields such as building, agriculture, traffic, energy, petrifaction, environmental protection, urban landscape, medical treatment, catering and the like, and increasingly enters the daily life of common people, and is classified according to sewage treatment sources, the sewage treatment is generally divided into production sewage treatment and domestic sewage treatment, the production sewage comprises industrial sewage, agricultural sewage, medical sewage and the like, the industrial sewage is the sewage generated by industrial production, and the sewage refers to a complex mixture of inorganic matters and organic matters in various forms, and comprises the following steps: floating and suspended large and small solid particles; ② colloidal and gelatinous dispersions; ③ pure solution.
In recent years, with the increasing requirements of the country on environmental protection, various industrial production plants begin to treat production wastewater, the most widely used method is to filter sewage generated in the production of magnesium aluminum silicate and the like and add adsorption sediments for treatment, but the treatment mode cannot filter from a molecular level, discharged water can cause secondary pollution to the environment, inorganic substances and eutrophic organic substances contained in the sewage can have negative effects on the environment, and a filtering system aiming at the molecular level of magnesium aluminum silicate and the like is urgently needed in order to achieve standard discharge after wastewater treatment.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide a magnesium aluminium silicate waste water recycle system to propose current sewage treatment plant in solving above-mentioned background art in the use, because use at present the most extensive sewage that produces magnesium aluminium silicate etc. filters and adds and adsorb the deposit and handle, nevertheless this treatment mode can't filter from the molecular aspect, thereby the water that leads to discharging can cause secondary pollution's problem to the environment again.
In order to achieve the above object, the utility model provides a following technical scheme: a system for recycling waste water in magnesium aluminum silicate production comprises a coagulation air flotation filter, wherein a third water outlet pipe is communicated with one side of the coagulation air flotation filter, the other end of the third water outlet pipe is communicated with a booster pump, a second communicating pipe is communicated with one side of the booster pump, which is far away from the third water outlet pipe, the other end of the second communicating pipe is communicated with a sand filter tank, the bottom of the sand filter tank is communicated with a fifth connecting pipe, the other end of the fifth connecting pipe is communicated with a precision filter, the bottom of the precision filter, which is far away from the fifth connecting pipe, is communicated with a fourth connecting pipe, the other end of the fourth connecting pipe is communicated with an ultrafilter, the bottom of the ultrafilter is communicated with a fourth communicating pipe, the other end of the fourth communicating pipe is communicated with a second raw water tank, the bottom of the second raw water tank is communicated with a first connecting pipe, and the other end of the first connecting pipe is communicated with a low-concentration reverse osmosis filter, the bottom intercommunication that low dense reverse osmosis filter kept away from second former water pitcher one side has the second outlet pipe, the other end intercommunication of second outlet pipe has the retrieval and utilization water tank, the one side intercommunication that precision filter was kept away from to the ultrafilter has third communicating pipe, the other end intercommunication of third communicating pipe has first former water pitcher, the one side intercommunication that the ultrafilter was kept away from to first former water pitcher has the third connecting pipe, the other end intercommunication of third connecting pipe has high enriched reverse osmosis filter, one side intercommunication that first former water pitcher was kept away from to high enriched reverse osmosis filter has the second connecting pipe, the other end intercommunication of second connecting pipe has standard metering well.
Preferably, the bottom of sand filtration jar and ultrafilter all is fixed with four short stabilizer blades, the equal fixed mounting in bottom of first former water pitcher and second former water pitcher has former water pitcher stabilizer blade.
Preferably, the bottom of one side of the reuse water tank is communicated with a second drain pipe, and one side of the standard metering well is communicated with a first drain pipe.
Preferably, one side of the first raw water tank is communicated with a first raw water tank blow-off pipe, and one side of the second raw water tank is communicated with a second raw water tank blow-off pipe.
Preferably, the bottom of one side of the high-concentration reverse osmosis filter is communicated with a first water outlet pipe, and the first water outlet pipe is communicated with a recycling water tank.
Preferably, the top of one side of the low-concentration reverse osmosis filter is communicated with a first communicating pipe, and the first communicating pipe is communicated with a first raw water tank.
Preferably, the top of the first raw water tank and the top of the second raw water tank are both movably provided with raw water tank sealing covers, and the top of the sand filter tank is movably provided with a filling cover.
Compared with the prior art, the beneficial effects of the utility model are that:
1. by arranging the coagulation air flotation filter, after sewage is filtered by the coagulation air flotation filter, the sewage is communicated to the booster pump through the third water outlet pipe, after being pressurized by the booster pump, the sewage enters the sand filter tank through the second connecting pipe for filtration, the sewage enters the precision filter for filtration and then is communicated to the ultrafilter, the molecular weight of the ultrafilter is greater than ten thousand, the sewage enters the first raw water tank through the fourth communicating pipe on the upper layer, the molecular weight of the sewage enters the second raw water tank through the fourth communicating pipe, then filtered water in the second raw water tank enters the low-concentration reverse osmosis filter for secondary diversion, qualified filtered water enters the reuse water tank for secondary utilization, filtered water enters the first raw water tank through the first communicating pipe, and filtered water enters the high-concentration reverse osmosis filter for filtration, the water that is favorable to retrieving gets into the retrieval and utilization water tank through the first outlet pipe of lower floor intercommunication, recycle, and the water that accords with emission standard after the terminal filtration gets into standard measurement well record, then discharges through first drain pipe, has solved the problem that most of filtration water can not effectively get rid of the inorganic matter in the aquatic and the rich organic matter row after filtering effectively, has perfected the purification and utilization flow, has promoted the environmental protection efficiency.
2. Through setting up the lid that packs, in time add after the filter consumption in the sand filtration jar, productivity ratio has been promoted, design through setting up second former water tank blow off pipe and first former water pipe drain can effectively carry out real-time sampling monitoring to the solution after filtering, in time know the filterable condition, fault-tolerant rate has been improved, can look over the back to the filterable condition through setting up former water tank sealed lid, add the additive that corresponds and conveniently clear up the inside of former water tank, through setting up short stabilizer blade and former water tank stabilizer blade with equipment lifting and then make things convenient for the filtrating to pass through the bottom outflow, the process of filtering has been made things convenient for, efficiency has been perfected.
Drawings
Fig. 1 is a schematic view of a top-down perspective structure of the present invention;
fig. 2 is a schematic view of the three-dimensional appearance structure of the present invention;
fig. 3 is a schematic view of the system flow of the present invention.
In the figure: 1. a coagulation air flotation filter; 2. a filler cover; 3. a sand filtration tank; 4. a precision filter; 5. a raw water tank sealing cover; 6. a second raw water tank; 7. a second raw water tank blow-off pipe; 8. a first connecting pipe; 9. a low-concentration reverse osmosis filter; 10. a second water outlet pipe; 11. a recycling water tank; 12. a second drain pipe; 13. a first drain pipe; 14. a standard metering well; 15. a first water outlet pipe; 16. a second connecting pipe; 17. a first communication pipe; 18. a third connecting pipe; 19. a first raw water tank blow-off pipe; 20. a first raw water tank; 21. a raw water tank support leg; 22. a fourth connecting pipe; 23. a second communicating pipe; 24. a third water outlet pipe; 25. a booster pump; 26. a short leg; 27. a fifth connecting pipe; 28. a third communicating pipe; 29. an ultrafilter; 30. a fourth communicating pipe; 31. a high concentration reverse osmosis filter.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
Referring to fig. 1-3, the present invention provides a technical solution: a system for recycling waste water in magnesium aluminum silicate production comprises a coagulation air flotation filter 1, wherein one side of the coagulation air flotation filter 1 is communicated with a third water outlet pipe 24, the other end of the third water outlet pipe 24 is communicated with a booster pump 25, one side of the booster pump 25, which is far away from the third water outlet pipe 24, is communicated with a second communicating pipe 23, the other end of the second communicating pipe 23 is communicated with a sand filter tank 3, the bottom of the sand filter tank 3 is communicated with a fifth connecting pipe 27, the other end of the fifth connecting pipe 27 is communicated with a precision filter 4, the bottom of the precision filter 4, which is far away from the fifth connecting pipe 27, is communicated with a fourth connecting pipe 22, the other end of the fourth connecting pipe 22 is communicated with an ultrafilter 29, the bottom of the ultrafilter 29 is communicated with a fourth communicating pipe 30, the other end of the fourth communicating pipe 30 is communicated with a second raw water tank 6, the bottom of the second raw water tank 6 is communicated with a first connecting pipe 8, and the other end of the first connecting pipe 8 is communicated with a low-concentration reverse osmosis filter 9, the bottom that low dense reverse osmosis filter 9 kept away from second raw water jar 6 one side communicates has second outlet pipe 10, the other end intercommunication of second outlet pipe 10 has retrieval and utilization water tank 11, one side intercommunication that precision filter 4 was kept away from to ultrafilter 29 has third communicating pipe 28, the other end intercommunication of third communicating pipe 28 has first raw water jar 20, one side intercommunication that ultrafilter 29 was kept away from to first raw water jar 20 has third connecting pipe 18, the other end intercommunication of third connecting pipe 18 has high enriched reverse osmosis filter 31, one side intercommunication that first raw water jar 20 was kept away from to high enriched reverse osmosis filter 31 has second connecting pipe 16, the other end intercommunication of second connecting pipe 16 has standard measurement well 14.
In the embodiment, by arranging the coagulation air-float filter 1, after the sewage is filtered by the coagulation air-float filter 1, the sewage is communicated to the booster pump 25 through the third water outlet pipe 24, after the sewage is pressurized by the booster pump 25, the sewage enters the sand filtration tank 3 through the second connecting pipe 16 and is filtered, the sewage enters the precision filter 4 and is communicated to the ultrafilter 29 after being filtered, molecules with the molecular mass larger than twenty thousand by the pressure molecular permeation membrane of the ultrafilter 29 enter the first raw water tank through the third communicating pipe 28 on the upper layer, molecules with the molecular mass smaller than twenty thousand by ten thousand by the molecular mass enter the second raw water tank 6 through the fourth communicating pipe 30, then the filtered water in the second raw water tank 6 enters the low-concentration reverse osmosis filter 9 and is filtered by the molecular permeation membrane, the qualified filtered water is secondarily guided to enter the reuse water tank 11 for secondary use, and the filtered liquid with the slightly larger molecular mass enters the first raw water tank 20 through the first communicating pipe 17, after the filtrate in the first raw water tank 20 enters the high-concentration reverse osmosis filter 31 for filtration, the recovered water can enter the reuse water tank 11 through the first water outlet pipe 15 communicated with the lower layer for recycling, the water meeting the discharge standard after terminal filtration enters the standard metering well 14 for recording, and then is discharged through the first water outlet pipe 13, thereby effectively solving the problem that most of filtered water cannot effectively remove inorganic matters and rich organic matters in the water after filtration, perfecting the purification and utilization process, improving the environmental protection efficiency, timely adding after the filtrate in the sand filter tank 3 is consumed by arranging the filler cover 2, improving the production efficiency, effectively sampling and monitoring the filtered solution in real time by arranging the second raw water tank drain pipe 7 and the first raw water tank drain pipe 19, timely knowing the filtration condition, improving the fault tolerance rate, and checking the filtration condition by arranging the raw water tank sealing cover 5, corresponding additive and the inside of conveniently clearing up the water pitcher of addition, through setting up short support leg 26 and former water pitcher stabilizer blade 21 with the equipment lifting and then make things convenient for the filtrating to flow through the bottom, made things convenient for and filtered the flow, perfect efficiency.
Specifically, four short legs 26 are fixed to the bottoms of the sand filter tank 3 and the ultrafilter 29, and raw water tank legs 21 are fixed to the bottoms of the first raw water tank 20 and the second raw water tank 6.
In this embodiment, set up short supporting leg 26 and former water tank stabilizer blade 21 and with equipment lifting and then make things convenient for the filtrating to flow through the bottom, made things convenient for the filtration flow, perfect efficiency.
Specifically, the bottom of one side of the reuse water tank 11 is communicated with a second drain pipe 12, and one side of the standard metering well 14 is communicated with a first drain pipe 13.
In this embodiment, the second water discharge pipe 12 is used for conveniently taking out the qualified reuse water in the reuse water tank 11, and the first water discharge pipe 13 discharges the filtered water meeting the discharge standard after filtering.
Specifically, one side of the first raw water tank 20 is communicated with a first raw water tank sewage discharge pipe 19, and one side of the second raw water tank 6 is communicated with a second raw water tank sewage discharge pipe 7.
In this embodiment, can effectively carry out real-time sample monitoring to the solution after filtering through the design of the former raw water tank blow off pipe 7 of second and the former raw water tank blow off pipe 19, in time know filterable condition, improve the fault-tolerant rate.
Specifically, the bottom of one side of the high-concentration reverse osmosis filter 31 is communicated with a first water outlet pipe 15, and the first water outlet pipe 15 is communicated with the reuse water tank 11.
In this embodiment, after the filtrate in the first raw water tank 20 enters the high concentration reverse osmosis filter 31 for filtration, the recovered water can enter the reuse water tank 11 through the first water outlet pipe 15 communicated with the lower layer for recycling.
Specifically, the top of one side of the low-concentration reverse osmosis filter 9 is communicated with a first communicating pipe 17, and the first communicating pipe 17 is communicated with a first raw water tank 20.
In this embodiment, the filtered water in the second raw water tank 6 enters the low-concentration reverse osmosis filter 9, is filtered by the molecular permeable membrane, and then is subjected to secondary diversion to obtain qualified filtered water, and then enters the reuse water tank 11 for secondary utilization, and the filtered water with slightly larger molecular mass enters the first raw water tank 20 through the first communication pipe 17.
Specifically, the top of the first raw water tank 20 and the top of the second raw water tank 6 are both movably provided with a raw water tank sealing cover 5, and the top of the sand filter tank 3 is movably provided with a filling cover 2.
In this embodiment, through packing lid 2, in time add after the filter consumption in sand filtration jar 3, promoted productivity ratio.
The utility model discloses a theory of operation and use flow: when in use, sewage enters the coagulation air flotation filter 1, after being filtered by the coagulation air flotation filter 1, the sewage is communicated to a booster pump 25 through a third water outlet pipe 24, after being pressurized by the booster pump 25, the sewage enters the sand filtration tank 3 through a second connecting pipe 16 and is filtered, the sewage enters the precision filter 4 and is communicated to an ultrafilter 29, molecules with molecular mass larger than two thousand of ten thousand are filtered by a pressure molecular permeation membrane of the ultrafilter 29, the molecules with molecular mass smaller than two thousand of ten thousand enter the first raw water tank through a third communicating pipe 28 on the upper layer, the molecules with molecular mass smaller than two thousand of ten thousand enter the second raw water tank 6 through a fourth communicating pipe 30, then filtered water in the second raw water tank 6 enters the low-concentration reverse osmosis filter 9 and is filtered by a molecular permeation membrane, and then qualified filtered water is secondarily guided to enter the reuse water tank 11 for secondary use, and filtered liquid with slightly larger molecular mass enters the first raw water tank 20 through the first communicating pipe 17, after the filtrate in the first raw water tank 20 enters the high-concentration reverse osmosis filter 31 for filtration, the recovered water can enter the reuse water tank 11 through the first water outlet pipe 15 communicated with the lower layer for recycling, the water meeting the discharge standard after terminal filtration enters the standard metering well 14 for recording, and then is discharged through the first water outlet pipe 13, thereby effectively solving the problem that most of filtered water cannot effectively remove inorganic matters and rich organic matters in the water after filtration, perfecting the purification and utilization process, improving the environmental protection efficiency, timely adding after the filtrate in the sand filter tank 3 is consumed by arranging the filler cover 2, improving the production efficiency, effectively sampling and monitoring the filtered solution in real time by arranging the second raw water tank drain pipe 7 and the first raw water tank drain pipe 19, timely knowing the filtration condition, improving the fault tolerance rate, and checking the filtration condition by arranging the raw water tank sealing cover 5, corresponding additive and the inside of conveniently clearing up the water pitcher of addition, through setting up short support leg 26 and former water pitcher stabilizer blade 21 with the equipment lifting and then make things convenient for the filtrating to flow through the bottom, made things convenient for and filtered the flow, perfect efficiency.
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 invention, the scope of which is defined in the appended claims and their equivalents.
Claims (7)
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022818688.8U CN213895452U (en) | 2020-11-30 | 2020-11-30 | A kind of magnesium aluminum silicate production wastewater recycling system |
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| Application Number | Priority Date | Filing Date | Title |
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| CN202022818688.8U CN213895452U (en) | 2020-11-30 | 2020-11-30 | A kind of magnesium aluminum silicate production wastewater recycling system |
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| CN213895452U true CN213895452U (en) | 2021-08-06 |
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| CN202022818688.8U Active CN213895452U (en) | 2020-11-30 | 2020-11-30 | A kind of magnesium aluminum silicate production wastewater recycling system |
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| Date | Code | Title | Description |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: ZHEJIANG FENGHONG NEW MATERIAL Co.,Ltd. Assignor: Zhejiang Walter New Material Co.,Ltd. Contract record no.: X2025330000343 Denomination of utility model: A recycling system for production wastewater of magnesium aluminum silicate Granted publication date: 20210806 License type: Common License Record date: 20251028 |
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| EE01 | Entry into force of recordation of patent licensing contract | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: Zhejiang Kelei New Material Co.,Ltd. Assignor: Zhejiang Walter New Material Co.,Ltd. Contract record no.: X2025330000388 Denomination of utility model: A recycling system for production wastewater of magnesium aluminum silicate Granted publication date: 20210806 License type: Common License Record date: 20251120 |
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| EE01 | Entry into force of recordation of patent licensing contract |