CN203264364U - 360-degree water feeding rotary underwater filter bed device - Google Patents
360-degree water feeding rotary underwater filter bed device Download PDFInfo
- Publication number
- CN203264364U CN203264364U CN 201320295024 CN201320295024U CN203264364U CN 203264364 U CN203264364 U CN 203264364U CN 201320295024 CN201320295024 CN 201320295024 CN 201320295024 U CN201320295024 U CN 201320295024U CN 203264364 U CN203264364 U CN 203264364U
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- filter bed
- filter
- cover plate
- filtering
- inner cover
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 63
- 238000001914 filtration Methods 0.000 claims abstract description 68
- 239000000463 material Substances 0.000 claims abstract description 15
- 239000000706 filtrate Substances 0.000 claims description 26
- 239000003643 water by type Substances 0.000 claims description 8
- 230000008901 benefit Effects 0.000 abstract description 6
- 230000000694 effects Effects 0.000 abstract description 5
- 238000007599 discharging Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 description 14
- 239000004744 fabric Substances 0.000 description 10
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 8
- 239000010865 sewage Substances 0.000 description 7
- 238000011001 backwashing Methods 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- 239000000725 suspension Substances 0.000 description 5
- 239000006004 Quartz sand Substances 0.000 description 4
- 238000011161 development Methods 0.000 description 4
- 238000009826 distribution Methods 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 238000004140 cleaning Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000000835 fiber Substances 0.000 description 3
- 238000011010 flushing procedure Methods 0.000 description 3
- 239000004576 sand Substances 0.000 description 3
- 239000000919 ceramic Substances 0.000 description 2
- 230000001112 coagulating effect Effects 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 230000007246 mechanism Effects 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 206010003830 Automatism Diseases 0.000 description 1
- 241000894006 Bacteria Species 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 206010067868 Skin mass Diseases 0.000 description 1
- 241000700605 Viruses Species 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
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- 239000000084 colloidal system Substances 0.000 description 1
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- 238000009833 condensation Methods 0.000 description 1
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- 238000011118 depth filtration Methods 0.000 description 1
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- 229910001385 heavy metal Inorganic materials 0.000 description 1
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- 229910052698 phosphorus Inorganic materials 0.000 description 1
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- Filtration Of Liquid (AREA)
Abstract
The utility model relates to the technical field of filtration and in particular relates to a 360-degree water feeding rotary underwater filter bed device. A filter bed device is arranged below a horizontal plane, an air pipe is arranged inside a center pipe, the center pipe is connected with a total water discharging pipe and is provided with a driving device and a plurality of filtering units, the driving device drives the filtering units to rotate at 360 degrees by taking the center pipe as a center, each filtering unit is composed of a filter bed, a filter bed outer cover plate and a filter bed inner cover plate, each filter bed inner cover plate is arranged at the outer ring of the center pipe, each filter bed outer cover plate is arranged at the outer ring of the corresponding filter bed inner cover plate, each filter bed is arranged between the corresponding filter bed inner cover plate and the corresponding filter bed outer cover plate, and a shell is arranged outside each filter bed outer cover plate. Compared with the prior art, the 360-degree water feeding rotary underwater filter bed device has the advantages that the filtration area can be enlarged by multiple times, filter materials are saved and the filtration rate is improved under the same floor area condition; the strength requirement on an external structure and the requirement on suspended matter in fed water are low, the loss of a filtering head is low, backflushing gas is concentrated and high in strength, and a filtering effect is good.
Description
[technical field]
The utility model relates to filtration art, specifically filter bed device under a kind of 360 degree water inlet rotating waters.
[background technology]
In water technology, sewage is by the particulate filter layer time, some suspended materials wherein and colloidal substance just are trapped within hole or on dielectric surface, and this method by granular media layer separatin non-soluble pollution impurity is called granular media filters, and is called for short and filters.Filtration mechanism is thought at present and is mainly contained: sieving effect, settlement action and adsorption-condensation effect.The range of application that water and sewage water filtration are processed is mainly: 1. remove turbidity in former water and colloid etc.; 2. remove the tiny chemical flco that tiny biological floe that the biological treatment second pond do not removed or coagulative precipitation tank are not removed; 3. improve the clearance of SS, turbidity, BOD, COD, phosphorus, heavy metal, bacterium and virus etc.; 4. be that advanced treating and reuse operation (as charcoal absorption, membrane filtration, ion-exchange etc.) are created good condition of water quality.
The form in filter tank is varied, is the most basic pattern with quartz sand as the conventional rapid filter of filtrate.For giving full play to filter material layer impurity trapped ability, double-deck, multilayer and even-granular filter have been developed, upward flow and bidirectional flow filter tank etc.For the gentle minimizing of the Automated water that improves operation filter tank valve, siphon filter, valveless filtering pool, moving flushing cage filter chamber, other hydraulic automatism have occurred and rinsed filter tank, filtering cloth filtering pool etc.On backwashing manner, there is simple water to rinse and the air-water backwashing mode.Staggered carrying out normally filtered and rinsed to the process of filter progress.In sewage disposal there be filter tank commonly used:
1) conventional rapid filter: this is a kind of filter tank of the most generally using both at home and abroad, stable and reliable operation, and large resistance water distribution system, effluent quality is good; But its shortcoming is: valve is many, and operational administrative is cumbersome, generally is used for large and medium-sized Sewage Plant.Filtrate uses quartz sand usually, and quartz sand has enough mechanical strengths, and price is low, and material is easy to get, and is all very stable in neutrality and subacidity water.Filter and mainly utilize the surface area that in filtering layer, bulk material provides, the suspended solid of process coagulating treatment in trap water.When the loss of flood peak of filtering reaches maximum, or the turbidity of filtrate or other predetermined water quality parameter occur when defective, need carry out the backwash in filter tank.Opposite when during backwash, water (flow) direction is with filtration, utilize the percussion of current and the friction between filtrate to remove the suspended solid that filtering layer is held back.
2) the development pattern filter tank of conventional rapid filter: as double-valve filter pool, shutter filter, double layer filter etc.
3) V-type filter tank: the V-type filter tank is a kind of high speed homogenization filter material filter pool of French moral profit full (Degremont) company exploitation, and the significant advantage that holding filth capacity is large, developing result is good is arranged.Individual layer thickening quartz sand filter media is adopted in this filter tank, and deep layer is cut dirty mode.Backwashing manner is air-water backwashing, and is provided with surface cleaning cloth tank, and developing result is good.Water distribution system adopts strainer head, can be not if establish very thin supporting layer.The V-type filter tank is a kind of Novel filter faster of development at present.The shortcoming in this filter tank is that equipment is slightly complicated, and filtration expense, civil engineering specification requirement are higher.
4) gravity valveless filter: valveless filtering pool is to utilize the pipe-line system of design to control the filtering layer resistance, when reaching limit value, and automatic backwash.This filter tank operation all automatically, and is easy to operate, the negative head phenomenon can not occur in running; Without large size valve, cost is than low with the scale general filter chamber.Its shortcoming is to use small resistance water wiring system, low water head recoil Xian, and backwash is inhomogeneous, and phenomenon easily is short-circuited.Pipe fitting is more complicated, and is strict to what install.
5) pressure filter: pressure filter is generally the rapid filter that GB150-1998 is made, and adopts large resistance water distribution system, and backwash is even.Can directly utilize the overbottom pressure water outlet.The varying head constant speed filter, water quality is filtered not as slowing down.Single pool area is little, can only be used for the little water yield Sewage Plant of utilizing without elevation.
In present domestic and international filtering technique research and development, the research emphasis of filtering technique and pond, filter tank type is to increase the filter tank to contain dirty ability, improves filtering velocity, improves effluent quality, secondly simplifies the operation, and improves the level of automation and continued operation.
Start with from changing media performance, researched and produced ceramic grain filter, porcelain sand filter material, fiber filtering etc.Wherein, ceramic grain filter mechanical strength and chemical stability are better, and filtering velocity is large.Fiber filtering has been broken through the restriction that the material footpath of particulate filter can not further dwindle, and makes the diameter of filtrate reach μ m level, has increased specific area and the adsorption capacity of filtrate.Aspect the development of filter tank pattern, occurred:
1) upward flow filter: the filter bed containing filth amount is large, does not produce negative head and air-resistance phenomenon, but filtering velocity can not be too high.During filtration, after filter, water goes out stream on top, pond, can observe at any time the situation of filtrate.Dirt concentrates in the coarse media of bottom mostly, more difficult rinsing well during backwash.
2) continuous filtration pool (device): continuous filter has showed a kind of new filtration and cleaning way, current being considered to, have one of filter of development most, it moves to the cleaning of filtrate outside the filter tank, make filter continuous reforwarding row, without the process that stops production and rinse, the loss of flood peak is lower and relatively constant.The shortcoming of this kind filter is complex structure, and treating capacity is little.
3) the pressure filter filtration of pumping up, flow process is simple, processes operation for small-scale sewage convenient, uses more.
But also there are many problems in present filter tank design and running, as:
1) negative head and air-resistance phenomenon
When the loss of flood peak that is increased to filtering layer when filtration resistance surpassed the filtering cloth head at this place, the negative head phenomenon will appear.Negative head can cause air to discharge, and increases the filtering layer local resistance.When rinsing, air is taken away the part filtrate with water, causes the local large particle diameter column of filtering layer, filters thereby make the phenomenon that is short-circuited.
Vapour lock be due to local accumulation in filter material layer air, reduce to filter the water yield, form the filter material layer crack, filtering water worsens.
2) contamination
There is the dead angle in filtering layer, builds up colloidal substance mud and mutually bond.
3) run hourglass sand
Backwash rate is excessive or the filtrate grating is improper, and backwash can wash away a large amount of filtrates.Or the flushing water maldistribution, supporting layer can be moved, so that filtrate runs off by water distribution system.
Two kinds of methods of general employing such as the filtration of mud-water separation, water at present:
1) traditional filtering method (take sand filter, filtering tank etc. as representative)
It is characterized by: adopt pond type or barrel shape, the inner filtrate of placing, the vertical layout, former water enters filter bed from top to bottom or from bottom to top, by the suspension in the filtrate trap water etc.;
Advantage is: filtering accuracy is higher, and is less demanding to the concentration limit of water inlet suspension;
Shortcoming is: one direction is filtered, and floor space is large, and during backwash, recoil all must be united with air water in the bottom of whole filtering surface, and the air water requirement of strength is high;
2) another filtering technique is the filtering cloth filtering pool technology at present, it is characterized by: adopt filter cloth, as fiber filter cloth or stainless steel filter cloth, also can be placed under water, and can rotate.But it does not adopt depth filtration, deep bed filtration.
Advantage is: floor space is little, and filtering cloth head is lower;
Shortcoming is: holding filth capacity is little, and filtering accuracy is lower, requires the concentration of water inlet suspension lower, and backwash is frequent.
[utility model content]
The purpose of this utility model is to overcome the deficiencies in the prior art, has drawn two kinds of filtering technique advantages of filter material filter pool and filtering cloth filtering pool, with both filtration mechanism combinations, provides filter bed device under a kind of 360 degree water inlet rotating waters.
for achieving the above object, design filter bed device under a kind of 360 degree water inlet rotating waters, comprise shell (1), filter bed (2), filter bed inner cover plate (4), central tube (5), air hose (6), drive unit (7) and total outlet pipe (8), it is characterized in that described filter bed device is arranged at below horizontal plane, be provided with air hose (6) in described central tube (5), central tube (5) connects total outlet pipe (8), central tube (5) is provided with drive unit (7) and some filter elements, described drive unit (7) drives filter element and do 360 degree rotations centered by central tube (5), described filter element is by filter bed (2), filter bed inner cover plate (4) forms, central tube (5) outer ring is provided with filter bed inner cover plate (4), filter bed inner cover plate (4) outer ring is provided with shell (1), be provided with filter bed (2) between filter bed inner cover plate (4) and shell (1).
Described shell (1) outer rim is circle or polygon.
Described central tube (5) outlet water level is lower than horizontal plane.
Described filter bed is provided with filtrate in (2), and described filtrate is the lightweight filtering material.
The utility model has the advantage of:
(1) because 360 degree directions are intake, under same floor space condition, this device filter area can improve 3.14 times;
(2) because the filtrate area of device filtering direction reduces gradually, so: 1) save filtrate; 2) improve filtering velocity; 3) save recoil tolerance; 4) repercussion effect is better;
(3) because be placed under water, and 360 degree direction water inlets, this device requires low to outside structural strength, saved the required tank body of general filtering tank, housing etc., only needs a simple network structure thing, stops filtrate to run off;
(4) need not general filter tank, the required pond body of filtering cloth filtering pool;
(5) filtering accuracy is high, and lower to the requirement of water inlet suspension, water head loss by filtration is little.
(6) only need gas backwash, and required narrow-minded, need not back-flushing;
(7) when recoil, the device rotation, recoil gas forms filtrate each position and strafes recoil, and narrow-minded, gas is concentrated, backwashing strength is large, repercussion effect good (suspension and the biomembrane that fully contact between filtrate, tackle easily come off from filter material surface).
(8) data: per cycle filtration time is 10～12 hours.
[description of drawings]
Fig. 1 is primary structure front view of the present utility model;
Fig. 2 is 1 group of combination example structure top view of the present utility model;
Fig. 3 is 4 groups of combination example structure side views of the present utility model;
As shown in the figure, in figure: a. water level 1. shell 2. filter bed devices (filtrate) are the filter bed inner cover plate 5. central tube 6. air hose 7. total outlet pipes of drive unit 8. 4.;
Specifying Fig. 1 is Figure of abstract of the present utility model.
[specific embodiment]
The utility model is described in further detail below in conjunction with accompanying drawing, and the structure of this device and principle are very clearly concerning this professional people.Should be appreciated that specific embodiment described herein only in order to explaining the utility model, and be not used in restriction the utility model.
Embodiment:
filter bed device under 360 degree water inlet rotating waters, comprise shell (1), filter bed (2), filter bed inner cover plate (4), central tube (5), air hose (6), drive unit (7) and total outlet pipe (8), described filter bed device is arranged at below horizontal plane, be provided with air hose (6) in described central tube (5), central tube (5) connects total outlet pipe (8), central tube (5) is provided with drive unit (7) and some filter elements, described drive unit (7) drives filter element and do 360 degree rotations centered by central tube (5), described filter element is by filter bed (2), filter bed inner cover plate (4) forms, central tube (5) outer ring is provided with filter bed inner cover plate (4), filter bed inner cover plate (4) outer ring is provided with shell (1), be provided with filter bed (2) between filter bed inner cover plate (4) and shell (1).Described shell (1) outer rim is circle or polygon.Described central tube (5) outlet water level is lower than horizontal plane.Described filter bed is provided with filtrate in (2), and described filtrate is the lightweight filtering material, as artificial or natural filtering material, as fibrous nodules, shell class, diatomite etc.
In sewage disposal, this utility model can be placed in second pond, cancel effluent weir and the follow-up filtering technique of second pond of second pond, by the 360 direct water outlets of degree rotating filter bed apparatus central tube, water outlet meets higher standard.
In running water or middle water reuse, also can be placed in sedimentation basin, cancel sedimentation basin and follow-up clarification, filtering technique etc.
Claims (4)
1. spend filter bed device under the water inlet rotating water for one kind 360, comprise shell (1), filter bed device (2), filter bed inner cover plate (4), central tube (5), air hose (6), drive unit (7) and total outlet pipe (8), it is characterized in that described filter bed device is arranged at below horizontal plane, be provided with air hose (6) in described central tube (5), central tube (5) connects total outlet pipe (8), central tube (5) is provided with drive unit (7) and some filter elements, described drive unit (7) drives filter element and do 360 degree rotations centered by central tube (5), described filter element is by filter bed (2), filter bed inner cover plate (4) forms, central tube (5) outer ring is provided with filter bed inner cover plate (4), filter bed inner cover plate (4) outer ring is provided with shell (1), be provided with filter bed (2) between filter bed inner cover plate (4) and shell (1).
2. filter bed device under a kind of 360 degree water inlet rotating waters as claimed in claim 1, is characterized in that described shell (1) outer rim is circle or polygon.
3. filter bed device under a kind of 360 degree water inlet rotating waters as claimed in claim 1, is characterized in that described central tube (5) outlet water level is lower than horizontal plane.
4. filter bed device under a kind of 360 degree water inlet rotating waters as claimed in claim 1, is characterized in that being provided with filtrate in described filter bed (2), and described filtrate is the lightweight filtering material.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320295024 CN203264364U (en) | 2013-05-27 | 2013-05-27 | 360-degree water feeding rotary underwater filter bed device |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320295024 CN203264364U (en) | 2013-05-27 | 2013-05-27 | 360-degree water feeding rotary underwater filter bed device |
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| Publication Number | Publication Date |
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| CN203264364U true CN203264364U (en) | 2013-11-06 |
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| CN 201320295024 Expired - Lifetime CN203264364U (en) | 2013-05-27 | 2013-05-27 | 360-degree water feeding rotary underwater filter bed device |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103272416A (en) * | 2013-05-27 | 2013-09-04 | 上海复旦水务工程技术有限公司 | 360-degree inflow rotation type underwater filter bed device and filtering method |
| CN104261552A (en) * | 2014-09-30 | 2015-01-07 | 中国水产科学研究院渔业机械仪器研究所 | Rotary moving bed biological filtration device |
| CN111558254A (en) * | 2020-04-07 | 2020-08-21 | 华东理工大学 | Method and system for removing short hair fibers in leather-making and fur processing wastewater |
-
2013
- 2013-05-27 CN CN 201320295024 patent/CN203264364U/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103272416A (en) * | 2013-05-27 | 2013-09-04 | 上海复旦水务工程技术有限公司 | 360-degree inflow rotation type underwater filter bed device and filtering method |
| CN104261552A (en) * | 2014-09-30 | 2015-01-07 | 中国水产科学研究院渔业机械仪器研究所 | Rotary moving bed biological filtration device |
| CN104261552B (en) * | 2014-09-30 | 2016-05-11 | 中国水产科学研究院渔业机械仪器研究所 | A kind of revolving moving bed biological filter |
| CN111558254A (en) * | 2020-04-07 | 2020-08-21 | 华东理工大学 | Method and system for removing short hair fibers in leather-making and fur processing wastewater |
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| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: HUICHUAN (SHANGHAI) ENVIRONMENTAL PROTECTION TECHN Free format text: FORMER OWNER: FUDAN WATER ENGINEERING TECHN CO., LTD., SHANGHAI Effective date: 20141118 |
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| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20141118 Address after: 200433, room 1, building 403, Fudan Science Park, Lane 127, Cathay Road, Shanghai, Yangpu District Patentee after: HUICHUAN (SHANGHAI) ENVIRONMENTAL PROTECTION TECHNOLOGY Co.,Ltd. Address before: 4, 200433 floor, building 1, Fudan Science Park, Lane 127, Cathay Road, Shanghai, Yangpu District Patentee before: SHANGHAI FUDAN WATER ENGINEERING TECHNOLOGY Co.,Ltd. |
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| ASS | Succession or assignment of patent right |
Owner name: YIQINGLIU (SHANGHAI) ENVIRONMENTAL PROTECTION TECH Free format text: FORMER OWNER: HUICHUAN (SHANGHAI) ENVIRONMENTAL PROTECTION TECHNOLOGY CO., LTD. Effective date: 20150210 |
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Free format text: CORRECT: ADDRESS; FROM: 200433 YANGPU, SHANGHAI TO: 201401 FENGXIAN, SHANGHAI |
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Effective date of registration: 20150210 Address after: Fengxian District 201401 Shanghai Feng Jin Road No. 469 building 4 room 5041 Patentee after: Yiqingliu (Shanghai) Environmental Protection Technology Co.,Ltd. Address before: 200433, room 1, building 403, Fudan Science Park, Lane 127, Cathay Road, Shanghai, Yangpu District Patentee before: HUICHUAN (SHANGHAI) ENVIRONMENTAL PROTECTION TECHNOLOGY Co.,Ltd. |
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| TR01 | Transfer of patent right |
Effective date of registration: 20171226 Address after: 4, 200433 floor, building 1, Fudan Science Park, Lane 127, Cathay Road, Shanghai, Yangpu District Patentee after: SHANGHAI FUDAN WATER ENGINEERING TECHNOLOGY Co.,Ltd. Address before: Fengxian District 201401 Shanghai Feng Jin Road No. 469 building 4 room 5041 Patentee before: Yiqingliu (Shanghai) Environmental Protection Technology Co.,Ltd. |
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Granted publication date: 20131106 |
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