CN110204103B - Suspension medium layer filtering system based on hydraulic fluidization layering - Google Patents
Suspension medium layer filtering system based on hydraulic fluidization layering Download PDFInfo
- Publication number
- CN110204103B CN110204103B CN201910619690.1A CN201910619690A CN110204103B CN 110204103 B CN110204103 B CN 110204103B CN 201910619690 A CN201910619690 A CN 201910619690A CN 110204103 B CN110204103 B CN 110204103B
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- China
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- filtering device
- water inlet
- water
- layering
- weir
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- 238000001914 filtration Methods 0.000 title claims abstract description 83
- 239000000725 suspension Substances 0.000 title claims abstract description 21
- 238000005243 fluidization Methods 0.000 title claims abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 121
- 238000010992 reflux Methods 0.000 claims abstract description 22
- 238000002156 mixing Methods 0.000 claims description 11
- 238000003756 stirring Methods 0.000 claims description 6
- 239000003814 drug Substances 0.000 abstract description 16
- 239000010865 sewage Substances 0.000 abstract description 13
- 238000005189 flocculation Methods 0.000 abstract description 4
- 230000016615 flocculation Effects 0.000 abstract description 4
- 239000012535 impurity Substances 0.000 abstract description 4
- 230000000694 effects Effects 0.000 abstract description 2
- 238000005265 energy consumption Methods 0.000 abstract description 2
- 238000012423 maintenance Methods 0.000 abstract description 2
- 229910019142 PO4 Inorganic materials 0.000 description 6
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 6
- 239000010452 phosphate Substances 0.000 description 6
- 239000012530 fluid Substances 0.000 description 5
- 241000195493 Cryptophyta Species 0.000 description 4
- 229940079593 drug Drugs 0.000 description 4
- 230000001112 coagulating effect Effects 0.000 description 3
- 238000004062 sedimentation Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 239000007788 liquid Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/5281—Installations for water purification using chemical agents
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/105—Phosphorus compounds
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Filtration Of Liquid (AREA)
Abstract
The invention relates to a suspension medium layer filtering system based on hydraulic fluidization layering, and belongs to the technical field of sewage treatment. The device comprises a filtering device, a reflux pump, a water inlet dosing system and a main body bracket; the filtering device is arranged on the main body bracket, and the main body bracket is arranged on the ground; the water inlet dosing system, the reflux pump and the filtering device form a circulation loop. The invention adopts the medium layer for filtering, forms the suspension medium layer through the hydraulic flow state, effectively removes suspended impurities in sewage by utilizing the net capturing and flocculation effects of the medium layer, reduces the content of suspended matters in effluent, improves the effluent quality, and has the characteristics of low energy consumption, low medicine consumption and convenient operation and maintenance.
Description
Technical Field
The invention relates to a suspension medium layer filtering system based on hydraulic fluidization layering, in particular to a filtering system for treating secondary effluent of a sewage treatment plant or black and odorous water body in a city, and belongs to the technical field of sewage treatment.
Background
At present, a secondary effluent treatment device of a sewage treatment plant designed and used at home and abroad is mainly used for further removing suspended matters, phosphate and other substances in a coagulating sedimentation or direct filtration mode, so that the stability of the effluent quality reaches the standard; the black and odorous water body is treated mainly by in-situ coagulating sedimentation or direct filtration to remove algae, suspended matters, phosphate and other substances in the water body, so as to improve the phenomenon of black and odorous water body. Along with the improvement of the national sewage treatment industry standard and the urban black and odorous water body treatment requirements, the removal requirements of suspended matters, phosphate, algae and the like in sewage are also improved, the existing coagulating sedimentation or direct filtration treatment methods have respective limitations, and no filtration method and device for removing suspended matters, phosphate and algae in sewage through a suspending medium layer are seen in the market at present.
Disclosure of Invention
The invention aims to overcome the defects, and provides a suspension medium layer filtering system based on hydraulic fluid layering, which is used for treating secondary effluent of a sewage treatment plant or urban black and odorous water body, and suspended matters, phosphate, algae and other substances in sewage are removed through filtering of the suspension medium layer formed by hydraulic fluid layering.
According to the technical scheme, the suspension medium layer filtering system based on the hydraulic fluid state layering comprises a filtering device, a reflux pump, a water inlet dosing system and a main body bracket; the filtering device is arranged on the main body bracket, and the main body bracket is arranged on the ground; the water inlet dosing system, the reflux pump and the filtering device form a circulation loop.
Further, the device comprises a filtering device, a reflux pump, a water inlet dosing system and a main body bracket; the filtering device is arranged on the main body bracket, and the main body bracket is arranged on the ground; the water inlet dosing system, the reflux pump and the filtering device form a circulation loop.
Further, the filtering device comprises a water outlet weir, a water outlet, an overflow port, a reflux port, an emptying port and a water inlet; the inside of the filtering device is provided with a water outlet weir which is connected with a water outlet, and one side of the filtering device is provided with an overflow port; the water inlets are positioned at two sides of the bottom of the filtering device;
the bottom of the filtering device is provided with a return port and an emptying port; the reflux port is connected with the water inlet and drug adding system through a reflux pump; the drain is connected to a drain system through a drain pipe.
Further, the overflow port is higher than the water outlet weir.
Further, the water outlet weir is arranged at the inner side of the top end of the upper part of the filtering device, is connected with the inner wall of the upper half part of the filtering device, and forms a box-shaped space with an upper opening with the inner wall of the filtering device; the water outlet weir is a saw-tooth weir or a horizontal weir.
Further, the water outlet weir is annular, water outlets are symmetrically arranged on the inner bottom surface, and the water outlets extend to the outer wall of the filtering device to discharge water through pipelines.
Further, the water inlets are positioned at two sides of the bottom end of the filtering device; the water inlet direction and the filtering device are tangentially arranged, and the water inlets at two sides are symmetrically arranged and are connected with the water inlet medicine adding system through pipelines.
Further, the inner diameter of the upper half part of the filtering device is gradually enlarged from bottom to top, and the lower half part is in an inverted conical funnel shape.
Further, the water inlet and drug adding system comprises a drug adding barrel, a water inlet pump, a pipeline mixer, a mixing motor and a water inlet pipe; the water inlet pipe is connected with a water inlet pump, the water inlet pump is connected with a pipeline mixer, and the pipeline mixer is connected with a filtering device;
further, the dosing barrel is respectively connected with the pipeline mixer and the reflux pump; the top of the dosing barrel is provided with a mixing motor, the mixing motor is connected with a stirring device, and the stirring device is arranged inside the dosing barrel.
Further, the water inlet dosing system comprises a pipeline mixer; and the two water inlets are connected with the pipeline mixer.
The invention has the beneficial effects that: the invention adopts the medium layer for filtering, forms the suspension medium layer through the hydraulic flow state, effectively removes suspended impurities in sewage by utilizing the net capturing and flocculation effects of the medium layer, reduces the content of suspended matters in effluent, improves the effluent quality, and has the characteristics of low energy consumption, low medicine consumption and convenient operation and maintenance.
Drawings
Fig. 1 is a schematic diagram of the structure of the present invention.
Fig. 2 is a front view of the filter device of the present invention.
Fig. 3 is a top view of the filter device of the present invention.
Reference numerals illustrate: 1. the filter device comprises a filter device 2, a water outlet weir, 3, a water outlet, 4, an overflow port, 5, a backflow port, 6, an emptying port, 7, a water inlet, 8, a dosing barrel, 9, a water inlet pump, 10, a pipeline mixer, 11, a mixing motor, 12, a backflow pump, 13, a water inlet pipe, 14, a water inlet system, 15 and a main body support.
Detailed Description
As shown in fig. 1-3, the suspension medium layer filtering system based on the hydraulic fluid state layering comprises a filtering device 1, a reflux pump 12, a water inlet dosing system 14 and a main body bracket 15; the filtering device 1 is arranged on a main body bracket 15, and the main body bracket 15 is arranged on the ground; the water inlet dosing system 14, the reflux pump 12 and the filtering device 1 form a circulation loop.
The filtering device 1 comprises a water outlet weir 2, a water outlet 3, an overflow port 4, a return port 5, an emptying port 6 and a water inlet 7; an effluent weir 2 is arranged in the filtering device 1, the effluent weir 2 is connected with a water outlet 3, and an overflow port 4 is arranged on one side of the filtering device 1; the water inlets 7 are positioned at two sides of the bottom of the filtering device 1;
the bottom of the filtering device 1 is provided with a return port 5 and an emptying port 6; the reflux port 5 is connected with a water inlet dosing system 14 through a reflux pump 12; the drain 6 is connected to a drain system via a drain pipe.
The height of the overflow 4 is higher than that of the water outlet weir 2.
The water outlet weir 2 is arranged at the inner side of the top end of the upper part of the filtering device 1, is connected with the inner wall of the upper half part of the filtering device 1, and forms a box-shaped space with an upper opening with the inner wall of the filtering device 1; the water outlet weir 2 is a saw-tooth weir or a horizontal weir.
The water outlet weir 2 is annular, water outlets 3 are symmetrically arranged on the inner bottom surface, and the water outlets 3 extend to the outer wall of the filtering device 1 through pipelines to discharge water.
The water outlet weir 2 is L-shaped in cross section, one side of the L-shape is fixed on the inner wall of the upper part of the filtering device 1, and forms a U-shaped groove with the filtering device 1.
The water inlets 7 are positioned at two sides of the bottom end of the filtering device 1; the water inlet direction is tangential to the filter device 1, the water inlets 7 on two sides are symmetrically arranged, and are connected with the water inlet dosing system 14 through pipelines.
The inner diameter of the upper half part of the filtering device 1 is gradually enlarged from bottom to top, and the lower half part is in an inverted conical funnel shape.
The water inlet dosing system 14 comprises a dosing barrel 8, a water inlet pump 9, a pipeline mixer 10, a mixing motor 11 and a water inlet pipe 13; the water inlet pipe 13 is connected with the water inlet pump 9, the water inlet pump 9 is connected with the pipeline mixer 10, and the pipeline mixer 10 is connected with the filtering device 1;
the dosing barrel 8 is respectively connected with the pipeline mixer 10 and the reflux pump 15; the top of the dosing barrel 8 is provided with a mixing motor 11, the mixing motor 11 is connected with a stirring device, and the stirring device is arranged inside the dosing barrel 8.
The water-in dosing system 14 includes a pipe mixer 10; both water inlets 7 are connected to a pipe mixer 10.
When the invention works, the water inlet pump 9 draws sewage to be treated from the water inlet pipe 13 to enter the pipeline mixer 10, the sewage in the pipeline mixer 10 is mixed with the evenly mixed medicament, and the mixture enters the filter device 1 through the water inlet 10. The water inlet and the medicament are fully mixed, which is a precondition for forming a suspension medium layer. Because the number of the water inlets 7 is 2, the water inlets are respectively positioned at two sides of the filtering device 1, the water flow entering the water inlets 7 can tangentially form vortex, which is favorable for flocculation reaction after the water inlet and the medicament are mixed, and a suspension medium layer with upper and lower layers is formed.
Then, the water inlet dosing system 14 supplies materials to the filtering device 1, the inner diameter of the inverted circular truncated cone body at the upper half part of the main body of the filtering device 1 is gradually enlarged from bottom to top, the rising flow velocity of water to be treated can be gradually reduced, and the height and the density of the formed suspension medium layer are controlled; the lower half part is in an inverted cone funnel shape, and the settled residual suspended medium layer impurities can be collected and then returned to the dosing system 14 through the return port 5 or uniformly discharged out of the system through the emptying port 6.
The medicament in the water inlet medicament adding system 17 is mainly flocculant or medicament with the same function, and forms a suspension medium layer through mixing and flocculation of the medicament and water inlet, and the suspension medium layer with a filtering function can be formed through the combined action of the medicament and the water inlet medicament and the hydraulic fluid state formed by the structure of the filtering device 1, so that the water inlet is effectively filtered and phosphate is removed. At this time, the liquid passing through the filter layer enters the water outlet weir 2 and is discharged through the water outlet 3; when the liquid height is higher than the water outlet weir 2, overflow is carried out through an overflow port 4; the water discharged from the water outlet 3 enters a subsequent disinfection system or a discharged water body, and the overflow water discharged from the overflow port 4 flows back to the front end of the system.
The impurities in the residual suspended medium layer which is settled at the bottom of the filtering device 1 are refluxed to the dosing barrel 8 through the action of the reflux pump 12, so that the drug consumption of the device is reduced while the suspended medium quantity in the filtering device 1 is ensured, and the running cost is saved. The drain 6 is connected to a drain system via a drain pipe.
Claims (6)
1. Suspension medium layer filtration system based on water conservancy flow regime layering, characterized by: comprises a filtering device (1), a reflux pump (12), a water inlet dosing system (14) and a main body bracket (15); the filtering device (1) is arranged on a main body bracket (15), and the main body bracket (15) is arranged on the ground; the water inlet dosing system (14), the reflux pump (12) and the filtering device (1) form a circulation loop;
the filtering device (1) comprises a water outlet weir (2), a water outlet (3), an overflow port (4), a reflux port (5), an emptying port (6) and a water inlet (7); an effluent weir (2) is arranged in the filtering device (1), the effluent weir (2) is connected with a water outlet (3), and an overflow port (4) is arranged at one side of the filtering device (1); the water inlets (7) are positioned at two sides of the bottom of the filtering device (1);
the bottom of the filtering device (1) is provided with a return port (5) and an emptying port (6); the reflux port (5) is connected with a water inlet dosing system (14) through a reflux pump (12); the emptying port (6) is connected to a drainage system through an emptying pipe;
the water inlets (7) are positioned at two sides of the bottom end of the filtering device (1); the water inlet direction and the filtering device (1) are tangentially arranged, the water inlets (7) at two sides are symmetrically arranged, and are connected with the water inlet dosing system (14) through pipelines;
the water inlet and dosing system (14) comprises a dosing barrel (8), a water inlet pump (9), a pipeline mixer (10), a mixing motor (11) and a water inlet pipe (13); the water inlet pipe (13) is connected with the water inlet pump (9), the water inlet pump (9) is connected with the pipeline mixer (10), and the pipeline mixer (10) is connected with the filtering device (1);
the dosing barrel (8) is respectively connected with the pipeline mixer (10) and the reflux pump (12); the top of the dosing barrel (8) is provided with a mixing motor (11), the mixing motor (11) is connected with a stirring device, and the stirring device is arranged inside the dosing barrel (8).
2. The waterpower fluidization layering-based suspension media layer filtration system as claimed in claim 1, wherein: the height of the overflow port (4) is higher than that of the water outlet weir (2).
3. The waterpower fluidization layering-based suspension media layer filtration system as claimed in claim 1, wherein: the water outlet weir (2) is arranged at the inner side of the top end of the upper part of the filtering device (1), is connected with the inner wall of the upper half part of the filtering device (1), and forms a box-shaped space with an upper opening with the inner wall of the filtering device (1); the water outlet weir (2) is a saw-tooth weir or a horizontal weir.
4. A suspension media layer filtration system based on a hydraulic fluidization layering as recited in claim 3, wherein: the water outlet weir (2) is annular, water outlets (3) are symmetrically arranged on the inner bottom surface, and the water outlets (3) extend to the outer wall of the filtering device (1) through pipelines to discharge water.
5. The waterpower fluidization layering-based suspension media layer filtration system as claimed in claim 1, wherein: the inner diameter of the upper half part of the filtering device (1) is gradually enlarged from bottom to top, and the lower half part is in an inverted conical funnel shape.
6. The waterpower fluidization layering-based suspension media layer filtration system as claimed in claim 1, wherein: the water inlet dosing system (14) comprises a pipeline mixer (10); the two water inlets (7) are connected with a pipeline mixer (10).
Priority Applications (1)
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CN201910619690.1A CN110204103B (en) | 2019-07-10 | 2019-07-10 | Suspension medium layer filtering system based on hydraulic fluidization layering |
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CN201910619690.1A CN110204103B (en) | 2019-07-10 | 2019-07-10 | Suspension medium layer filtering system based on hydraulic fluidization layering |
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CN110204103A CN110204103A (en) | 2019-09-06 |
CN110204103B true CN110204103B (en) | 2024-01-19 |
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CN113735202A (en) * | 2021-08-31 | 2021-12-03 | 安徽普氏生态环境工程有限公司 | Water separator device capable of accurately controlling water inlet proportion and adjusting method |
CN114950186A (en) * | 2022-06-13 | 2022-08-30 | 西安交通大学 | Nuclear crystal condensation induction granulation salt separation crystallization water treatment device with tangential water inlet/dosing/circulating water inlet structure |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101011638A (en) * | 2006-12-27 | 2007-08-08 | 株洲滴水恩环保科技有限责任公司 | Filter method and apparatus for highly effective coagulation suspending layer |
CN103787527A (en) * | 2014-01-21 | 2014-05-14 | 碧海舟(北京)石油化工设备有限公司 | Oily sewage air floatation suspension layer filtering device |
CN105129947A (en) * | 2015-10-10 | 2015-12-09 | 许建民 | Device for processing pollutant which can hardly be degraded biologically |
CN210559781U (en) * | 2019-07-10 | 2020-05-19 | 中国市政工程华北设计研究总院有限公司 | Suspension medium layer filtering system based on hydraulic flow state layering |
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2019
- 2019-07-10 CN CN201910619690.1A patent/CN110204103B/en active Active
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101011638A (en) * | 2006-12-27 | 2007-08-08 | 株洲滴水恩环保科技有限责任公司 | Filter method and apparatus for highly effective coagulation suspending layer |
CN103787527A (en) * | 2014-01-21 | 2014-05-14 | 碧海舟(北京)石油化工设备有限公司 | Oily sewage air floatation suspension layer filtering device |
CN105129947A (en) * | 2015-10-10 | 2015-12-09 | 许建民 | Device for processing pollutant which can hardly be degraded biologically |
CN210559781U (en) * | 2019-07-10 | 2020-05-19 | 中国市政工程华北设计研究总院有限公司 | Suspension medium layer filtering system based on hydraulic flow state layering |
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