CN109304057A - V-type filter tank - Google Patents
V-type filter tank Download PDFInfo
- Publication number
- CN109304057A CN109304057A CN201811476716.3A CN201811476716A CN109304057A CN 109304057 A CN109304057 A CN 109304057A CN 201811476716 A CN201811476716 A CN 201811476716A CN 109304057 A CN109304057 A CN 109304057A
- Authority
- CN
- China
- Prior art keywords
- filter tank
- guide rail
- liquid level
- type filter
- plate
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 59
- 239000007788 liquid Substances 0.000 claims abstract description 44
- 238000004220 aggregation Methods 0.000 claims abstract description 37
- 230000002776 aggregation Effects 0.000 claims abstract description 37
- 239000000706 filtrate Substances 0.000 claims abstract description 12
- 230000007246 mechanism Effects 0.000 claims description 17
- 239000000463 material Substances 0.000 claims description 9
- 238000001514 detection method Methods 0.000 claims description 7
- 239000013013 elastic material Substances 0.000 claims description 6
- 229910001220 stainless steel Inorganic materials 0.000 claims description 4
- 239000010935 stainless steel Substances 0.000 claims description 4
- 230000000855 fungicidal effect Effects 0.000 abstract description 5
- 239000000417 fungicide Substances 0.000 abstract description 5
- 239000010865 sewage Substances 0.000 abstract description 4
- 238000009395 breeding Methods 0.000 abstract 1
- 230000001488 breeding effect Effects 0.000 abstract 1
- 238000000034 method Methods 0.000 description 14
- 230000008569 process Effects 0.000 description 12
- 238000010926 purge Methods 0.000 description 6
- 238000005406 washing Methods 0.000 description 6
- 238000009826 distribution Methods 0.000 description 4
- 238000001914 filtration Methods 0.000 description 4
- 238000011001 backwashing Methods 0.000 description 3
- 238000001556 precipitation Methods 0.000 description 3
- 241000195493 Cryptophyta Species 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 2
- 239000002131 composite material Substances 0.000 description 2
- 238000011010 flushing procedure Methods 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 239000004576 sand Substances 0.000 description 2
- 244000043261 Hevea brasiliensis Species 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 229920003052 natural elastomer Polymers 0.000 description 1
- 229920001194 natural rubber Polymers 0.000 description 1
- 239000012286 potassium permanganate Substances 0.000 description 1
- 238000004080 punching Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 229920003051 synthetic elastomer Polymers 0.000 description 1
- 239000005061 synthetic rubber Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 238000004078 waterproofing Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D35/00—Filtering devices having features not specifically covered by groups B01D24/00 - B01D33/00, or for applications not specifically covered by groups B01D24/00 - B01D33/00; Auxiliary devices for filtration; Filter housing constructions
- B01D35/16—Cleaning-out devices, e.g. for removing the cake from the filter casing or for evacuating the last remnants of liquid
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Filtration Of Liquid (AREA)
Abstract
The present invention provides a kind of V-type filter tanks, it is related to technical field of sewage, V-type filter tank provided by the invention includes filter tank ontology and multiple aggregation removal devices, filter tank ontology has multiple for accommodating the filter tank of filtrate, multiple filter tanks are arranged in a one-to-one correspondence with multiple aggregation removal devices, aggregation removal device includes scraper component and liquid level regulation device, liquid level regulation device is connect with filter tank ontology, to adjust the peak level that filter tank can accommodate, the top that scraper component is set to filter tank ontology is used to remove the aggregation of the filter tank water surface.V-type filter tank provided by the invention can remove the aggregation in filter tank, solve the problems, such as the breeding of filter tank water surface aggregation, reduce fungicide and add, the indexs such as when effectively reducing artificial, power consumption and plugman.
Description
Technical field
The present invention relates to technical field of sewage, more particularly, to a kind of V-type filter tank.
Background technique
V-type filter tank is a kind of form of rapid filter, because it is intake, groove shape is in the shape of the letter V and gains the name, and is also equal grain filtrate
Filter tank.
Traditional V-type filter tank generally as potassium permanganate composites subsequent processing, especially at iron and steel enterprise's composite wastewater
It in reason, but runs after a certain period of time, a large amount of algae (summer is especially prominent) can be accumulated in the pond of V-type filter tank, the reason for this is that preceding
The presence of microorganism, suspended matter, colloid etc. in the water outlet of the pond Duan Gaomi, into traditional V-type filter tank after can be gathered in its water surface, warp
The amount is strengthened after going through a cycle of operation, precipitation position program is executed when filter tank backwash, the accumulation can be with dampening at this time
The variation of position is spread in filter tank pool wall, and over time, the microorganism etc. in accumulation obtains mass propagation, especially in summer,
Microbial reproduction is more prominent, or even algae occur etc., V-type filter tank influent load is thereby increased, filter sand service life is shortened,
And influence environment.
The existing method for solving the problems, such as this is exactly to add fungicide in the highly dense pond of leading portion, reinforce manual cleaning and shorten anti-
Wash the period.But the costs such as when using such mode that can accordingly increase medicament, artificial, power consumption and plugman, it is clear that no
The social development demand for meeting environmental protection and energy saving, reducing supplies consumption.
Summary of the invention
The purpose of the present invention is to provide a kind of V-type filter tanks, can remove the aggregation in filter tank, solve the filter tank water surface
The problem of aggregation is bred, reduces fungicide and adds, the indexs such as when effectively reducing artificial, power consumption and plugman.
To achieve the above object, the present invention the following technical schemes are provided:
The present invention provides a kind of V-type filter tank, including filter tank ontology and multiple aggregation removal devices, the filter tank ontology tool
There are multiple filter tanks for being used to accommodate filtrate, multiple filter tanks are arranged in a one-to-one correspondence with multiple aggregation removal devices, institute
Stating aggregation removal device includes scraper component and liquid level regulation device, and the liquid level regulation device and the filter tank ontology connect
It connects, to adjust the peak level that the filter tank can accommodate, the scraper component is set to the top of the filter tank ontology for going
Except the aggregation of the filter tank water surface.
Further, the liquid level regulation device includes fixed plate and push plate, and the fixed plate and the filter tank ontology connect
It connects, the push plate is slidably connected with the fixed plate.
Further, the liquid level regulation device further includes driving mechanism, and the driving mechanism is for driving the push plate
It is moved relative to the fixed plate.
Further, the scraper component includes guide rail and scraper plate, and the scraper plate is slidably connected with the guide rail.
Further, actuator is equipped between the guide rail and the scraper plate, the actuator is for driving the scraper plate
It is slided along the guide rail.
Further, the guide rail includes the first guide rail being slidably connected with described scraper plate one end and another with the scraper plate
The second guide rail that one end is slidably connected.
Further, the extending direction of first guide rail and second guide rail is each parallel to the transversal of the filter tank
Face.
Further, material of the scraper plate close to described filter tank one end is elastic material.
Further, material of the scraper plate far from described filter tank one end is stainless steel.
Further, the liquid level detection device for further including control system and being arranged in a one-to-one correspondence with multiple filter tanks, institute
It states liquid level detection device to connect with the control system, the control system connects with multiple aggregation removal devices respectively
It connects.
V-type filter tank provided by the invention can generate it is following the utility model has the advantages that
When stating V-type filter tank in use, each filter tank is correspondingly arranged on an aggregation removal device, i.e., each is poly-
Collection object removal device is used to remove the aggregation of the water surface in corresponding filter tank.Sewage is discharged into first when specifically used each
It is filtered in filter tank, liquid level regulation device is in middle position at this time;After filtering, air water back washing is carried out to the filtrate in filter tank
It washes, liquid level regulation device is in low level at this time;After flushing, liquid level regulation device is reconciled to a high position, at this time in filter tank
Water level is in highest state, and the sundries such as suspended matter green alga in water are swum on the water surface, then removes filter tank by scraper component
The aggregation of the water surface.
For compared with the existing technology, V-type filter tank provided by the invention can remove the aggregation in filter tank, solve filter
The problem of water face aggregation is bred, reduces fungicide and adds, extends backwash cycle, effectively reduces artificial, power consumption
And the indexs such as when plugman, filter tank environment are greatly improved, while liquid level regulation device can effectively reduce qualified production water
Unreasonable emission problem.
Detailed description of the invention
It, below will be to specific in order to illustrate more clearly of the specific embodiment of the invention or technical solution in the prior art
Embodiment or attached drawing needed to be used in the description of the prior art be briefly described, it should be apparent that, it is described below
Attached drawing is some embodiments of the present invention, for those of ordinary skill in the art, before not making the creative labor
It puts, is also possible to obtain other drawings based on these drawings.
Fig. 1 is the top view in V-type filter tank provided in an embodiment of the present invention;
Fig. 2 is the ground floor plan in V-type filter tank provided in an embodiment of the present invention;
Fig. 3 is A-A sectional view provided in an embodiment of the present invention;
Fig. 4 is B-B sectional view provided in an embodiment of the present invention;
Fig. 5 is C-C sectional view provided in an embodiment of the present invention;
Fig. 6 is D-D sectional view provided in an embodiment of the present invention.
Icon: the filter tank 1- ontology;2- aggregation removal device;21- scraper component;211- guide rail;2111- first
Guide rail;The second guide rail of 2112-;212- scraper plate;213- actuator;22- liquid level regulation device;221- fixed plate;222-
Push plate;223- driving mechanism;3- liquid level detection device;4- pond body;5- is always intake distributing channel;The filter tank 6- water inlet weir plate;
7-V type intake chamber;8- air water distributes pipe duct;9- backwash drainage ditch;10- trapped well;11- filtrate;12- inlet valve;
Outlet valve after 13- filter;14- backwash inlet valve;15- backwash intake valve;16- backwash drain valve;17- backwash exhaust valve.
Specific embodiment
Technical solution of the present invention is clearly and completely described below in conjunction with attached drawing, it is clear that described implementation
Example is a part of the embodiment of the present invention, instead of all the embodiments.Based on the embodiments of the present invention, ordinary skill
Personnel's every other embodiment obtained without making creative work, shall fall within the protection scope of the present invention.
In the description of the present invention, it should be noted that term " center ", "upper", "lower", "left", "right", "vertical",
The orientation or positional relationship of the instructions such as "horizontal", "inner", "outside" be based on the orientation or positional relationship shown in the drawings, merely to
Convenient for description the present invention and simplify description, rather than the device or element of indication or suggestion meaning must have a particular orientation,
It is constructed and operated in a specific orientation, therefore is not considered as limiting the invention.In addition, term " first ", " second ",
" third " is used for descriptive purposes only and cannot be understood as indicating or suggesting relative importance.
In the description of the present invention, it should be noted that unless otherwise clearly defined and limited, term " installation ", " phase
Even ", " connection " shall be understood in a broad sense, for example, it may be being fixedly connected, may be a detachable connection, or be integrally connected;It can
To be mechanical connection, it is also possible to be electrically connected;It can be directly connected, can also can be indirectly connected through an intermediary
Connection inside two elements.For the ordinary skill in the art, above-mentioned term can be understood at this with concrete condition
Concrete meaning in invention.
Below in conjunction with attached drawing, detailed description of the preferred embodiments.It should be understood that this place is retouched
The specific embodiment stated is merely to illustrate and explain the present invention, and is not intended to restrict the invention.
Fig. 1 is the top view in V-type filter tank provided in an embodiment of the present invention;Fig. 2 is V-type filter tank provided in an embodiment of the present invention
Ground floor plan;Fig. 3 is A-A sectional view provided in an embodiment of the present invention;Fig. 4 is that B-B provided in an embodiment of the present invention is cutd open
Face figure;Fig. 5 is C-C sectional view provided in an embodiment of the present invention;Fig. 6 is D-D sectional view provided in an embodiment of the present invention.
The purpose of the present embodiment is that provide a kind of V-type filter tank, as shown in Figures 1 to 6, including filter tank ontology 1 and multiple
Aggregation removal device 2, filter tank ontology 1 have multiple for accommodating the filter tank of filtrate, multiple filter tanks and the removal of multiple aggregations
Device 2 is arranged in a one-to-one correspondence, and aggregation removal device 2 includes scraper component 21 and liquid level regulation device 22, liquid level regulation device
22 connect with filter tank ontology 1, and to adjust the peak level that filter tank can accommodate, scraper component 21 is set to the top of filter tank ontology 1
For removing the aggregation of the filter tank water surface.
When stating V-type filter tank in use, each filter tank is correspondingly arranged on an aggregation removal device, i.e., each is poly-
Collection object removal device is used to remove the aggregation of the water surface in corresponding filter tank.As shown in fig. 6, represented by the liquid level of the top
It is a high position, is low level represented by the liquid level of bottom, is middle position between the liquid level of the top and the liquid level of bottom.Tool
Body using when sewage is discharged into each filter tank is filtered first, liquid level regulation device is in middle position at this time;After filtering,
Air-water backwashing is carried out to the filtrate in filter tank, liquid level regulation device is in low level at this time;After flushing, liquid level is adjusted and is filled
It sets and reconciles to a high position, the water level in filter tank is in highest state at this time, and the sundries such as suspended matter green alga in water are swum on the water surface,
The aggregation of the filter tank water surface is then removed by scraper component.
For compared with the existing technology, V-type filter tank provided in this embodiment can remove the aggregation in filter tank, solve
The problem of filter tank water surface aggregation is bred, reduces fungicide and adds, extends backwash cycle, effectively reduce artificial, electric
Consumption and indexs, filter tank environment are greatly improved when plugman etc., while liquid level regulation device can effectively reduce and qualified produce water
Unreasonable emission problem.
As shown in Figures 1 to 6, above-mentioned filter tank ontology includes pond body 4, total water inlet distributing channel 5, filter tank water inlet weir plate 6, V-type
Outlet valve 13, backwash after intake chamber 7, air water distribution pipe duct 8, backwash drainage ditch 9, trapped well 10, filtrate 11, inlet valve 12, filter
Inlet valve 14, backwash intake valve 15, backwash drain valve 16, backwash exhaust valve 17.Wherein: total water inlet distributing channel 5, filter tank influent weir
Plate 6 and V-type intake chamber 7 are connect with pond body 4;Air water distribution pipe duct 8 is connected to the bottom in filter tank;Backwash drainage ditch 9 is for being discharged
Backwash water;Trapped well 10 is connect with pond body 4 for filtered water purification to be discharged;Filtrate 11 is set in filter tank;After inlet valve 12, filter
Outlet valve 13, backwash inlet valve 14, backwash intake valve 15, backwash drain valve 16 and backwash exhaust valve 17 pass through pipeline and pond respectively
Body connection.
It is specifically using, is carrying out producing water running process first, at this point, 12 standard-sized sheet of inlet valve, outlet valve 13 is opened after filter,
Its valve is closed.In the process filter tank water inlet by always intake distributing channel 5 through inlet valve 12, filter tank water inlet weir plate 6 again through side opening into
Enter V-type intake chamber 7 and enter filter tank surface, water is produced after the filter filtered by homogeneous filtering material filtering layer and passes through the bottom plate inflow with strainer head
Bottom space imports air water by square hole and distributes pipe duct 8, then converges through trapped well 10 into subsequent water processing establishment.Liquid in the process
Position regulating device is in middle position.
Backwash process is then carried out, backwash precipitation position process, air purge process, gas washing step and washing work are specifically included
Sequence.In the process of backwash precipitation position, inlet valve 12 is closed, and 13 aperture of outlet valve increases and water level is made to be down to setting position after filter,
Liquid level is controlled during this always between sand face and purging open height, liquid level regulation device 22 minimizes position, this process can
Reduce outer displacement as far as possible under the premise of ensuring backwash effect.Air purge process is then carried out, backwash drain valve 16 is opened;
Starting fan opens backwash intake valve 15 after a period of time, inlet valve 12 is opened to half-open position, carries out air purge.In the process,
Top aperture of the air through air water distribution pipe duct 8 is sprayed, by 11 surface impurity of filtrate even into filter tank bottom by strainer head
It cleans and suspends in water, backwash drainage ditch 9 is poured by surface sweep washing water.Gas washing step is then carried out, backwash is started
Pump, opens backwash inlet valve 14, and air water washes a period of time.In the process, backwashing water also enters air water distribution pipe duct 8, gas and water
Filter tank bottom water distributing area is flowed into through aperture and square hole respectively, through strainer head even into filter tank, filtrate is further rinsed,
Surface purging continues to carry out.Washing step is then carried out, backwash intake valve 15 is closed, blower is closed after several seconds, opens backwash
Exhaust valve 17 after washing a period of time, closes backwash water pump, backwash inlet valve 14.In the process, stopping gas punching, independent water rushes,
Surface purging continues, and impurities in water is finally all poured to backwash drainage ditch 9.
Water surface aggregation removing step is then carried out, liquid level regulation device 22 is in a high position, and inlet valve 12 is still located at this time
In half-open position, water level constantly rises, and when rising to highest liquid level, starts scraper component 21, scraper component 21 is in filter tank water
The sundries (including remaining suspended matter, green alga etc.) of water surface remaining is struck off from intaking to drain-side to backwash drainage ditch 9, then in face
It is retracted into influent side, closes backwash drain valve 16.
Wherein, as shown in fig. 6, liquid level regulation device 22 includes fixed plate 221 and push plate 222, fixed plate 221 and filter tank sheet
Body 1 connects, and push plate 222 is slidably connected with fixed plate 221.Fixed plate 221 is equipped with the sliding slot for accommodating push plate 222, push plate
222 protrude into sliding slot and are slidably connected with fixed plate 221, the glide direction of push plate 222 along vertical direction, to increase or decrease
The height of filter tank upper edge.
Specifically, push plate 222 relative to the sliding of fixed plate 221 can using manually adjust and also using it is automatic, half from
It is dynamic to adjust.When using manually adjusting, fixed plate 221 is equipped with multiple rows of card slot, and multiple rows of card slot is distributed in the difference of fixed plate 221
Highly, push plate 222 is equipped with the fixture block for being caught in any one row's card slot.Can be manually adjusted when use fixture block be caught in it is a certain
It arranges in card slot, realizes the adjusting of push plate height.
When using automatic, semi-automatic adjusting, liquid level regulation device 22 further includes driving mechanism 223, and driving mechanism 223 is used
It is moved in drive push plate 222 relative to fixed plate 221.
It should be noted that all, to be able to drive push plate 222 relative to the structure that fixed plate 221 moves can be above-mentioned
Driving mechanism 223 mentioned by embodiment.Such as: driving mechanism 223 is hydraulic mechanism or driving mechanism 223 is aerostatic press
Perhaps driving mechanism 223 is nut screw mechanism to structure or driving mechanism 223 is linear motor, etc..
In at least one embodiment, driving mechanism 223 is linear motor, and linear motor drives push plate 222 relative to solid
Fixed board 221 moves, and linear motor does water-proofing treatment.
In some embodiments, in order to guarantee that scraper component 21 can be stable removes the sundries of water surface remaining, board group is scraped
Part 21 includes guide rail 211 and scraper plate 212, and scraper plate 212 is slidably connected with guide rail 211.
Specifically, scraper plate 212 can be used relative to the sliding of guide rail 211 and be manually adjusted or using automatic, semi-automatic
It adjusts.When using manually adjusting, scraper plate 212 can be manually pushed, so that scraper plate 212 is slided along guide rail 211.
When using automatic, semi-automatic adjusting, actuator 213 is equipped between guide rail 211 and scraper plate 212, actuator 213 is used
It is slided in drive scraper plate 212 along guide rail 211.
It is noted that all, to be able to drive scraper plate 212 along the structure that guide rail 211 slides can be above-described embodiment institute
The actuator 213 referred to.Such as: actuator 213 is that perhaps actuator 213 is air pressure mechanism or actuator to hydraulic mechanism
213 be nut screw mechanism or actuator 213 is linear motor, etc..
In at least one embodiment, actuator 213 is traveling trolley.
In some embodiments, guide rail 211 can only include a guide rail, and middle part and the guide rail of scraper plate 212 are slidably connected.
In some other embodiments, as shown in Figure 1, in order to enable the structure of guide rail 211 is more secured, guide rail 211
Including the first guide rail 2111 being slidably connected with 212 one end of scraper plate and the second guide rail being slidably connected with 212 other end of scraper plate
2112.First guide rail 2111 and the second guide rail 2112 can jointly be supported scraper plate 212.
On the basis of the above embodiments, in order to enable scraper plate 212 can directly scrape water surface aggregation into backwash draining
The extending direction of canal, the first guide rail 2111 and the second guide rail 2112 each parallel to the cross section in filter tank, lead along first by scraper plate 212
When rail 2111 and the second guide rail 2112 move, the direction of motion is parallel to the cross section in filter tank, can intake and scrape to drain-side certainly
Except the sundries of water surface remaining, directly the sundries of water surface remaining is scraped into backwash drainage ditch 9.
Wherein, in order to avoid hitting in 212 course of work of scraper plate with liquid level regulation device 22, scraper plate 212 is close to filter
The material of pond one end is elastic material.Elastic material has preferable elasticity, even if push plate 222 obtains top and is slightly above scraper plate 212
Bottom, elastic material can produce certain deformation, do not influence the normal work of scraper component 21.
Specifically, elastic material can may be synthetic rubber for natural rubber.
On the basis of the above embodiments, in order to enable scraper plate 212 can firmly with guide rail 211 or actuator 213
Connection, material of the scraper plate 212 far from filter tank one end is stainless steel.Stainless steel intensity with higher can guarantee that scraper plate 212 is steady
Fixed connect with guide rail 211 or actuator 213.
In some embodiments, above-mentioned V-type filter tank further includes control system and the liquid that is arranged in a one-to-one correspondence with multiple filter tanks
Level detecting apparatus 3, liquid level detection device 3 are connect with control system, and control system connects with multiple aggregation removal devices 2 respectively
It connects.Liquid level detection device 3 is used to detect the liquid level in filter tank, and liquid level information is sent to control system, and control system is used for
The working condition of aggregation removal device 2 is controlled according to liquid level information.Control system may include PLC control cabinet, PLC control cabinet
Specifically include air switch, PLC, power supply, relay and connecting terminal etc..
Finally, it should be noted that the above embodiments are only used to illustrate the technical solution of the present invention., rather than its limitations;To the greatest extent
Pipe present invention has been described in detail with reference to the aforementioned embodiments, those skilled in the art should understand that: its according to
So be possible to modify the technical solutions described in the foregoing embodiments, or to some or all of the technical features into
Row equivalent replacement;And these are modified or replaceed, various embodiments of the present invention technology that it does not separate the essence of the corresponding technical solution
The range of scheme.
Claims (10)
1. a kind of V-type filter tank, which is characterized in that including filter tank ontology (1) and multiple aggregation removal devices (2), the filter tank
Ontology (1) has multiple filter tanks for being used to accommodate filtrate, and multiple filter tanks and multiple aggregation removal devices (2) are one by one
It is correspondingly arranged, the aggregation removal device (2) includes scraper component (21) and liquid level regulation device (22), and the liquid level is adjusted
Device (22) is connect with the filter tank ontology (1), to adjust the peak level that the filter tank can accommodate, the scraper component
(21) it is used to remove the aggregation of the filter tank water surface set on the top of the filter tank ontology (1).
2. V-type filter tank according to claim 1, which is characterized in that the liquid level regulation device (22) includes fixed plate
(221) it is connect with push plate (222), the fixed plate (221) with the filter tank ontology (1), the push plate (222) and the fixation
Plate (221) is slidably connected.
3. V-type filter tank according to claim 2, which is characterized in that the liquid level regulation device (22) further includes driving machine
Structure (223), the driving mechanism (223) is for driving the push plate (222) to move relative to the fixed plate (221).
4. V-type filter tank according to claim 1, which is characterized in that the scraper component (21) includes guide rail (211) and scrapes
Plate (212), the scraper plate (212) are slidably connected with the guide rail (211).
5. V-type filter tank according to claim 4, which is characterized in that between the guide rail (211) and the scraper plate (212)
Equipped with actuator (213), the actuator (213) is for driving the scraper plate (212) to slide along the guide rail (211).
6. V-type filter tank according to claim 4, which is characterized in that the guide rail (211) includes and the scraper plate (212)
The first guide rail (2111) that one end is slidably connected and the second guide rail being slidably connected with the scraper plate (212) other end
(2112)。
7. V-type filter tank according to claim 6, which is characterized in that first guide rail (2111) and second guide rail
(2112) cross section of the extending direction each parallel to the filter tank.
8. V-type filter tank according to claim 4, which is characterized in that material of the scraper plate (212) close to described filter tank one end
Material is elastic material.
9. V-type filter tank according to claim 8, which is characterized in that material of the scraper plate (212) far from described filter tank one end
Material is stainless steel.
10. V-type filter tank according to claim 1, which is characterized in that further include control system and with multiple filter tanks one
One liquid level detection device (3) being correspondingly arranged, the liquid level detection device (3) connect with the control system, the control system
System is connect with multiple aggregation removal devices (2) respectively.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201811476716.3A CN109304057B (en) | 2018-12-04 | 2018-12-04 | V-shaped filter tank |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201811476716.3A CN109304057B (en) | 2018-12-04 | 2018-12-04 | V-shaped filter tank |
Publications (2)
Publication Number | Publication Date |
---|---|
CN109304057A true CN109304057A (en) | 2019-02-05 |
CN109304057B CN109304057B (en) | 2024-04-30 |
Family
ID=65222364
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201811476716.3A Active CN109304057B (en) | 2018-12-04 | 2018-12-04 | V-shaped filter tank |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN109304057B (en) |
Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR200376637Y1 (en) * | 2004-12-07 | 2005-03-11 | 조창균 | Scum disposal equipment for filtration/sewage disposal plant |
CN101830533A (en) * | 2010-05-31 | 2010-09-15 | 哈尔滨工业大学 | V-shaped air floating filter with deslagging function |
CN204039095U (en) * | 2014-06-26 | 2014-12-24 | 广州市顺骏环保节能科技有限公司 | For the efficient air-floating apparatus of sewage disposal |
CN105060476A (en) * | 2015-08-14 | 2015-11-18 | 得利满水处理系统(北京)有限公司 | V-shaped filter tank for deep denitrogenation |
CN205199127U (en) * | 2015-12-21 | 2016-05-04 | 杭州启澄科技有限公司 | Effluent water sump suspended solid remove device |
CN107485899A (en) * | 2017-09-12 | 2017-12-19 | 杭州东方雨虹建筑材料有限公司 | A kind of automatic filtering unit |
CN107601752A (en) * | 2016-07-12 | 2018-01-19 | 天津宏晟新环保科技有限公司 | A kind of effluent treatment plant with anti-sludge blocking function |
CN209254293U (en) * | 2018-12-04 | 2019-08-16 | 中冶沈勘秦皇岛工程设计研究总院有限公司 | V-type filter tank |
-
2018
- 2018-12-04 CN CN201811476716.3A patent/CN109304057B/en active Active
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR200376637Y1 (en) * | 2004-12-07 | 2005-03-11 | 조창균 | Scum disposal equipment for filtration/sewage disposal plant |
CN101830533A (en) * | 2010-05-31 | 2010-09-15 | 哈尔滨工业大学 | V-shaped air floating filter with deslagging function |
CN204039095U (en) * | 2014-06-26 | 2014-12-24 | 广州市顺骏环保节能科技有限公司 | For the efficient air-floating apparatus of sewage disposal |
CN105060476A (en) * | 2015-08-14 | 2015-11-18 | 得利满水处理系统(北京)有限公司 | V-shaped filter tank for deep denitrogenation |
CN205199127U (en) * | 2015-12-21 | 2016-05-04 | 杭州启澄科技有限公司 | Effluent water sump suspended solid remove device |
CN107601752A (en) * | 2016-07-12 | 2018-01-19 | 天津宏晟新环保科技有限公司 | A kind of effluent treatment plant with anti-sludge blocking function |
CN107485899A (en) * | 2017-09-12 | 2017-12-19 | 杭州东方雨虹建筑材料有限公司 | A kind of automatic filtering unit |
CN209254293U (en) * | 2018-12-04 | 2019-08-16 | 中冶沈勘秦皇岛工程设计研究总院有限公司 | V-type filter tank |
Also Published As
Publication number | Publication date |
---|---|
CN109304057B (en) | 2024-04-30 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN209254293U (en) | V-type filter tank | |
CN202951317U (en) | Automatic-cleaning precision filter | |
CN110510729A (en) | Cleaning control method, system and corresponding moving bed biological filter tank reactor assembly | |
CN104140172B (en) | A kind of Seawater desalination pretreatment method | |
CN207307284U (en) | A kind of rectangular sedimentation tank equipped with chain-belt type mud scraper for sewage treatment plant | |
CN102489061A (en) | Ultrasonic cleaning filter-screen filtering device | |
CN205867668U (en) | Swash plate washing unit | |
CN109304057A (en) | V-type filter tank | |
CN201713404U (en) | Recirculated cooling water treatment device | |
CN204147638U (en) | Fibre turntable filter chamber | |
CN208055012U (en) | A kind of sewage denitrification processing system | |
CN208212676U (en) | For advanced treatment of wastewater and the partially submerged turntable filter chamber of Treated sewage reusing | |
CN110839582A (en) | Runway type aquaculture pond and aquaculture system | |
CN105854619A (en) | Pulsed gas generator | |
CN211470913U (en) | High-efficient type filtering pond back flush structure of adjustable water level | |
CN211486826U (en) | Water purification and filtration system capable of reducing backwashing water consumption | |
CN205516875U (en) | High turbidity slurrying waste water ultrasonic processing equipment | |
CN105986433B (en) | Washing machine | |
CN208632198U (en) | A kind of MBR film sewage treatment device | |
CN107935174A (en) | A kind of sewage denitrification processing system | |
CN203862023U (en) | Regular dirt and sundry removing and processing device for sewage water | |
CN202936248U (en) | Aeration flusher of membrane bioreactor submerged membrane component | |
CN110734125A (en) | High-efficiency filter tank backwashing method and structure with adjustable water level | |
CN206184093U (en) | Fiber rotary disc filter | |
CN112915626B (en) | High-pressure steam non-stop online backwashing ballast water treatment device |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant |