CN208200514U - Three groups of formula circulating water cultivation biological filter systems of zero-emission type - Google Patents
Three groups of formula circulating water cultivation biological filter systems of zero-emission type Download PDFInfo
- Publication number
- CN208200514U CN208200514U CN201820363495.8U CN201820363495U CN208200514U CN 208200514 U CN208200514 U CN 208200514U CN 201820363495 U CN201820363495 U CN 201820363495U CN 208200514 U CN208200514 U CN 208200514U
- Authority
- CN
- China
- Prior art keywords
- water
- pond
- pipe
- filler
- denitrification
- 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.)
- Active
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
The utility model provides a kind of three groups of formula circulating water cultivation biological filter systems of zero-emission type, it is characterized by: this system is made of three independent ponds that by-pass filtration pond, secondary filtration pond and denitrification filtering ponds are interconnected, bottom of pond portion is in funnel type, and inside is provided with inclined tube biologic packing material;For breeding water when flowing through three ponds, the nitrobacteria that the nitrification filler in pond is grown under aerobic environment using filler surface is by the mineralized nitrogen in water at nontoxic nitrate;The denitrifying bacteria that denitrification filler is grown under oxygen-free environment using filler surface is by nitrate transformation at nitrogen, carbon dioxide and water.To realize the degradation to harmful components such as residual bait, excrement, ammonia nitrogen, nitrous acid and nitrate in circulating water cultivation water body, while the degassing to water and oxygenation are realized again.Its effect allows aquaculture zero-emission to become possible, while having the characteristics that low energy consumption, easy manipulation, easy to maintain, filter effect is significant, equipment operating cost is low.
Description
Technical field
The utility model relates to the instrument fields in terms of aquaculture water process, specifically a kind of to support for recirculated water
Grow in water treatment system for excrement, residual bait, ammonia nitrogen, nitrite, nitrate, etc. harmful substances carry out biofiltration (decomposition)
And supplement the water treatment system of dissolved oxygen in water.
Background technique
Used Biofiltration apparatus is many kinds of on present society, different, most all to be used in Aquatic-animal fish bowl
Or based on the small device in terms of research institutions, the production grade water filtration device that can be really used on circulating water cultivation is less it
It is again few.And at present Biofiltration apparatus used for aquiculture used in home and abroad both in decomposing in breeding water body
Excrement, ammonia nitrogen and nitrite, and final decomposition product nitrate retains can not eradicate in water always, as cultivation is given birth to
The progress of production, the excreta of institute's aquaculture organism, which nitrifies, to be decomposed, and nitrate can accumulate always the maximum tolerance of institute's health object in water
Degree directly threatens going on smoothly for breeding production.Therefore all such systems all can only be by way of partially changing water
To keep the concentration of nitrate in water body not interfere with the normal growth of biology.The above problem causes biofiltration to become circulation
Technical bottleneck in water cultivation, constrains development of the aquaculture on the directions such as batch production, interiorization, high density fish culture, special
It is not in the environmental issue and country got worse under the strict demand of aquaculture discharge, the invention patent is that aquatic products people opens
Open up out a suitable national conditions instantly, long-range pioneering channel.
Summary of the invention
The utility model provides a kind of three groups of formula circulating water cultivation biological filter systems of zero-emission type, and the purpose is to be directed to
Solving society, above existing aquaculture organisms filter plant operating is unstable, can not reduce nitrate, Maintenance Difficulty, volume are big, make
The problems such as valence is high, energy consumption is high makes biofiltration process while realizing that oxygenation row carbon dioxide, excreta are decomposed entirely, taken up little area, easily
It operates, is easy to maintain, reaching the final purpose of the real totally enclosed type circulating water cultivation of energy-saving and emission-reduction.
The technical solution of the utility model is:
A kind of three groups of formula circulating water cultivation biological filter systems of zero-emission type, this system is by by-pass filtration pond, second level mistake
Three independent pond compositions that filter tank and denitrification filtering ponds are interconnected, it is characterised in that: the by-pass filtration bottom of pond portion
In funnel type, funnel type bottom of pond lowest point is provided with main water inlet tube, what the bottom of pond of funnel type was conducive to generate in backwash process
Solid dirt concentrates near main water inlet tube, and is discharged to outside pond by main water inlet tube.Above the main water inlet tube, it is located at leakage
Bucket type bottom of pond open top is provided with Pneumatic support a Pneumatic support a and plays the role of recoil inflation and hold up nitrification filler.It is described
By-pass filtration pond the overflow pipe a for being connected to secondary filtration pond is provided on the pool wall at top, entered by main water inlet tube
The water in by-pass filtration pond, it is most of that secondary filtration pond is all flowed by overflow pipe a.Inside the by-pass filtration pond, overflow pipe a with
Completely nitrification filler is filled between Pneumatic support a, nitrification filler surface has nitrobacteria through cultivating growth.The nitrification filler leans on
Nearly top position is provided with denitrification filtering ponds water inlet pipe, and denitrification filtering ponds water inlet pipe water inlet is embedded in nitrification filler, separately
Outer one end water outlet is connected to the bottom of pond pipe of denitrification filtering ponds, between the inlet and outlet of denitrification filtering ponds water inlet pipe
It is provided with flow control valve, the water that such design allows small part to have been subjected to the nitrification processing of by-pass filtration pond passes through water-head certainly
It is dynamic to be flowed into denitrification filtering ponds, and its flow can be controlled by flow control valve.
The denitrification filtering bottom of pond portion is in funnel type, and funnel type bottom of pond lowest point is provided with bottom of pond pipe, funnel type pond
The solid dirt that bottom is conducive to generate in backwash process is concentrated near bottom of pond pipe, and is discharged to outside pond by sewage draining exit.Institute
Above the bottom of pond pipe stated, funnel type bottom of pond open top is provided with Pneumatic support c, and Pneumatic support c plays recoil inflation and support
The effect of denitrification filler.The denitrification filtering ponds are provided on the pool wall at top is connected to overflowing for secondary filtration pond
Water pipe b is finally flowed into secondary filtration pond by overflow pipe b after water enters denitrification filtering ponds from bottom of pond pipe.The spilling water
The pipeline lowest point of pipe b is lower than the pipeline lowest point of overflow pipe a, this makes the water level in by-pass filtration pond be higher than denitrification filtering ponds
Water level, water can be flowed into denitrification filtering ponds automatically by denitrification filtering ponds water inlet pipe.Inside the denitrification filtering ponds,
Full denitrification filler is filled between overflow pipe b and Pneumatic support c, denitrification filler surface has denitrifying bacteria through cultivating growth.
It is provided with a point water sieve plate b between overflow pipe b at the top of the denitrification filler, dividing water sieve plate b is porous plate structure, leaching
It is in underwater.It is described divide below water sieve plate b be provided with circulation water inlet pipe between denitrification filler, this avoid recycle into
Water pipe is drawn to pond inner top and contacts and oxygenous water with air, to ensure that denitrification filler is in the environment of no oxygen
In.The circulation water inlet pipe other end is connected with circulating pump, and circulating pump water outlet is connected with recirculation return pipe, circulating backwater
Pipe other end is connected to bottom of pond pipe, and the water of pond inner top is pumped into bottom of pond by circulating pump again, water iterative cycles in pond, from
And increase the contact probability of water and denitrifying bacteria, allow the nitrate in water decomposes more thoroughly.The recirculation return pipe
Circulating pump position is provided with chemical feed pipe, is provided with check valve on chemical feed pipe, is anti-nitration reaction addition by this chemical feed pipe
Required chemical reagent.
The secondary filtration bottom of pond portion is in funnel type, and funnel type bottom of pond lowest point is provided with primary flow pipe, funnel type
The solid dirt that bottom of pond is conducive to generate in backwash process concentrates near primary flow pipe, and is discharged to pond by primary flow pipe
Outside.Above the primary flow pipe, the slightly higher position of funnel type bottom of pond open top is provided with Pneumatic support b, and Pneumatic support b rises
To the effect of recoil inflation and support drop filter filler.The secondary filtration pond is provided with porous point of water sieve close to top position
Plate a divides the position water sieve plate a to be slightly below overflow pipe b, this water for allowing overflow pipe a and overflow pipe b to flow out can pass fully through a point water sieve
Plate a, and uniform sprinkle is on drop filter filler.Described divides the full drop filter of filling between water sieve plate a and Pneumatic support b bracket to fill out
Material, drop, which filters growth on filler, nitrobacteria.Air inlet is provided between the Pneumatic support b and funnel type bottom of pond open top
Pipe, air inlet pipe one end nozzle are opened inside secondary filtration pond, air blower are connected on other end nozzle, air blower is made a gift to someone a large amount of
Air is lauched and contacts with each other with sprinkle, has not only taken away the pernicious gases such as the carbon dioxide in water, oxygen is also added to water
In, saturation dissolved oxygen state has been reached while so that water is realized degasifying effect.
Nitrification filler, denitrification filler and the drop filter filler is fixed ripple inclined tube filler.
Pneumatic support a, Pneumatic support b and the Pneumatic support c is made by hollow tube, between hollow tube
It is connected to completely, is evenly distributed with aeration aperture on hollow tube wall, when being in recoil state, high pressure gas is uniform by aeration aperture
It is dispersed in filler bottom, and is risen on the water surface, to have the function that stir inner bucket water, cleaning filler.
Compared with prior art, the utility model has the following beneficial effects:
1, the pond that the utility model plays Water condition effect using three be interconnected is realized at one stroke to feeding
It grows and is decomposed with the denitrification of water, nitrification decomposition, oxygenation, remove removing carbon dioxide, decompose multiple important steps such as excrement and residual bait, most
Final product is nontoxic nitrogen, carbon dioxide and water, truly realizes the purpose for decomposing aquaculture organism excreta completely,
Solves the technical bottleneck in circulating water cultivation water process.
2, the biological bacteria that all biologic packing material surfaces of the utility model are grown all is that automatic growth goes out in the breeding process
Come, without complicated biofilm process, such biological bacteria decomposition efficiency is more stable, is suitable for the local water body ring locating for it
Border, and disposably decomposed excrement in breeding water body, residual bait, ammonia nitrogen, nitrite, nitrate etc. in a manner of scientific environmental protection and have
The purpose of evil substance, reduces unnecessary equipment and facility in traditional handicraft, reduces equipment cost and operating cost, and
This equipment also have many advantages, such as it is easy to install, easy to maintain, take up little area, obvious processing effect, complied with low-carbon environment-friendly, energy-saving and emission-reduction
The following industry development trend.
3, the by-pass filtration pond of the utility model and the biologic packing material of denitrification filtering ponds are totally submerged in water, are loaded
Biofilter material not only play the role of by Microbe membrane decompose be dissolved in water harmful substance, also act bonding,
Filter, hoard, decomposing the effect of bulky grain solid excreta in water.The function that equipment incidentally filters is increased, while also being increased
The maintenance period of equipment allows what equipment can be more stable to play effectiveness.
4, the design of the circulating pump of denitrification filtering ponds allows after denitrification filler in the utility model, but still contains nitre
The breeding water of hydrochlorate repeatedly flows through denitrification filler again, so that it is more thorough to decompose the nitrate in water, and can allow
Denitrification filler maintains steady operation under oxygen-free environment.
5, this equipment after a period of use due to the biomembrane that is grown on sheet biologic packing material surface can gradually aging, lead
Cause filter effect decline, it is therefore desirable to equipment is backwashed, when backwash, need to only be filled with a large amount of compressed gas from gas tube,
Water agitation in entire bucket is got up, so that it may by the biomembrane of aging in inclined tube filler surface and hoard between biologic packing material
Wash dirt get off.This backwash process is easy to operate, and required time is short, only needs simple controlled valve smoothly complete
At backwash ensure that the stability of whole equipment filter effect.
Detailed description of the invention
Fig. 1 is the perspective side elevation view of the utility model;
Fig. 2 is the isometric side view of the utility model Pneumatic support;
Fig. 3 is the side view that the utility model divides water sieve plate.
In the figure 1: by-pass filtration pond, 2: nitrification filler, 3: overflow pipe a, 4: main water inlet tube, 5: Pneumatic support a, 6:
Recoil valve a, 7: recoil tracheae a, 8: denitrification filtering ponds water inlet pipe, 9: flow control valve, 10: water level line a, 11: second level mistake
Filter tank, 12: drop filter filler, 13: air inlet pipe, 14 primary flow pipes, 15: Pneumatic support b, 16: recoil valve b, 17: recoil tracheae b,
18: air blower, 19: divide water sieve plate a, 20: water level line b, 21: denitrification filtering ponds, 22: denitrification filler, 23: overflow pipe b,
24: bottom of pond pipe, 25: Pneumatic support c, 26: recoil valve c, 27: recoil tracheae c, 28: circulation water inlet pipe, 29: divide water sieve plate b,
30: water level line c, 31: water circulating pump, 32: chemical feed pipe, 33: check valve, 34: recirculation return pipe, 35: blowdown valve, 36: sewage draining exit,
37: sieve plate edge, 38: sieve plate, 39: water hole, 40: aeration aperture, 41: Pneumatic support, 42: recoil tracheae.
Specific embodiment
Embodiment with reference to the accompanying drawing, the present invention will be further described.Following embodiment will be helpful to this field
Technical staff further understands the utility model, but does not limit the utility model in any form.It should be pointed out that ability
For the those of ordinary skill in domain, without departing from the concept of the premise utility, various modifications and improvements can be made.
These are all within the protection scope of the present invention.
As shown in Figure 1, three groups of formula circulating water cultivation biological filter systems of zero-emission type, this system by by-pass filtration pond,
Three independent pond compositions that secondary filtration pond and denitrification filtering ponds are interconnected, it is characterised in that: the by-pass filtration
Pond, secondary filtration pond and denitrification filtering ponds be include being not limited to other geometries such as cylindric, prism-shaped, three ponds
Bottom is in funnel type, is provided with Pneumatic support above funnel type bottom of pond, is provided with biologic packing material in the pond above bracket,
Biologic packing material is fixed ripple inclined tube filler.
The by-pass filtration bottom of pond portion is in funnel type, and funnel type bottom of pond lowest point is provided with main water inlet tube;The master
Pneumatic support a is provided with above water inlet pipe;The by-pass filtration pond is provided on the pool wall at top is connected to second level mistake
The overflow pipe a in filter tank;Inside the by-pass filtration pond, completely nitrification filler is filled between overflow pipe a and Pneumatic support a;Described
It nitrifies filler and top position is provided with denitrification filtering ponds water inlet pipe, denitrification filtering ponds water inlet pipe water inlet is embedded in nitrification
In filler, other end is connected to bottom of pond pipe, is provided with flow control valve among pipeline;It is connected on the Pneumatic support a
Recoil tracheae a, and the recoil end tracheae a is provided with recoil valve a.
The denitrification filtering bottom of pond portion is in funnel type, and funnel type bottom of pond lowest point is provided with bottom of pond pipe;The pond
Pneumatic support c is provided with above bottom tube;The denitrification filtering ponds are provided on the pool wall at top is connected to second level mistake
The overflow pipe b in filter tank;The pipeline lowest point of the overflow pipe b is lower than the pipeline lowest point of overflow pipe a;The denitrification filtering
Full denitrification filler is filled inside pond, between overflow pipe b and Pneumatic support c;At the top of the described denitrification filler with overflow pipe b it
Between be provided with a point water sieve plate b;Described dividing below water sieve plate b is provided with circulation water inlet pipe between denitrification filler;Described
Circulation water inlet pipe other end is connected with circulating pump, and circulating pump water outlet is connected with recirculation return pipe;The recirculation return pipe
Circulating pump position is provided with chemical feed pipe, is provided with check valve on chemical feed pipe;The recirculation return pipe other end connection
To bottom of pond pipe;Recoil tracheae c is connected on the Pneumatic support c, the recoil end tracheae c is provided with recoil valve c.
The secondary filtration bottom of pond portion is in funnel type, and funnel type bottom of pond lowest point is provided with primary flow pipe;The master
Pneumatic support b is provided with above outlet pipe;The secondary filtration pond is provided with a point water sieve plate a close to top position, divides water sieve
The position plate a is slightly below overflow pipe b;Full drop filter filler is filled in described dividing between water sieve plate a and Pneumatic support b bracket;Described
Recoil tracheae b is connected on Pneumatic support b, the recoil end tracheae b is provided with recoil valve b;It is set below the Pneumatic support b
It is equipped with air inlet pipe, air inlet pipe one end nozzle is opened inside secondary filtration pond, is connected with air blower on other end nozzle.
Shown in Fig. 2, the Pneumatic support a, Pneumatic support b are identical with Pneumatic support c structure, are this structure as shown in the figure
Look up the isometric side view in direction.Pneumatic support is made by square tube, is interconnected inside square tube, the connection between each square tube
Place is fully sealed;Pneumatic support is fixed in pond below biologic packing material, is evenly distributed on the tube wall towards bottom of pond direction several
Play the aeration aperture of aeration;The recoil tracheae for playing the role of air inlet is provided on Pneumatic support.
Shown in Fig. 3, it is the side view of this structure as shown in the figure that described, which divides water sieve plate a identical with water sieve plate b structure is divided,.
Water sieve plate is divided, along constituting, several water holes to be uniformly distributed on the sieve plate, water hole plays by sieve plate and the sieve plate of its surrounding
Water is allowed to flow uniformly through the effect of sieve plate.
The working principle of the utility model is as follows:
1, sewage enters by-pass filtration pond by the main water inlet tube below by-pass filtration pond when system works, later sewage
Nitrification filler uniformly and is slowly flowed through, the impurity such as excrement in water can be stuck on nitrification filler, be grown by nitrification filler surface
Microorganism decomposed, while the nitrobacteria that molten ammonia nitrogen in water can be grown by nitrification filler surface is converted to nitrous acid
Salt is further converted to nitrate, nitrifying process net reaction at this time are as follows: NH4++1.83O2+1.98HCO3 -→
0.021C5H7O2N+0.98NO3 -+1.04H2O+1.884H2CO3
The constantly upper length of water level in by-pass filtration pond, reaches position shown in water level line a, at this moment most of water can be from spilling water
Pipe a overflows into the dividing on water sieve plate a of secondary filtration pond.
2, the denitrification filtering of denitrification filtering bottom of pond portion is connected to due to being embedded with inside the nitrification filler in by-pass filtration pond
Pond water inlet pipe, and the position of overflow pipe b is lower than the position of overflow pipe a, therefore the water level in denitrification filtering ponds is lower than level-one
Pool water level is filtered, causes have a small amount of water that can ceaselessly flow through denitrification pond automatically, is flowed into secondary filtration pond from overflow pipe b
Divide on water sieve plate a.This part water is flowed into from the bottom of pond pipe of denitrification filtering bottom of pond portion, then slowly flows through denitrification filler, this
When denitrification filler surface on the denitrifying bacteria that grows the molten nitrate by water is resolved into nitrogen, carbon dioxide and water,
Denitrification process net reaction is (by taking methanol is carbon source as an example):
NO3 -+1.08CH3OH+0.24H2CO3→0.056C5H7O2N+0.47N2↑+1.68H2O+HCO3 -
Since its content can may not be reduced to by the breeding water containing nitrate when once flowing through denitrification filler
Ideal concentration, therefore water circulating pump is set, the water for having flowed through denitrification filler is drawn onto denitrification filler by water circulating pump again
Below, it so that water be allow to flow through denitrification filler back and forth, allows denitrification filtering to carry out with this more thorough, gives full play to
The denitrification function of equipment.Since denitrifying bacteria needs just can normally reduce nitrate under anaerobic, following
It is provided with a point water sieve plate b above the water inlet of ring water inlet pipe, has been connect with air with preventing water circulating pump to be drawn above apertured partition
Touching and dissolved with the water of oxygen, it is ensured that denitrification filtering ponds are in an oxygen-free environment, and anti-nitration reaction can be gone on smoothly.
The switch size of flow control valve is adjusted by measuring nitrate content in the water that flows out of overflow pipe b, thus
Determine flow through denitrification filler water how much.Flow control valve is turned down if nitrate content is excessively high, water is increased with this
In reaction time between the denitrifying bacteria of denitrification filler surface growth, further decrease nitrate content;If nitric acid
Salt content is too low, opens big flow control valve, is reduced with this anti-between water and the denitrifying bacteria of denitrification filler surface growth
Between seasonable, the water of anti-nitration reaction processing is increased.The size specifically adjusted need to be when breeding production be normally carried out, by not
The nitrate content of water obtains optimum valve regulation scheme at disconnected tracking overflow pipe b.
Chemical reagent needed for anti-nitration reaction (by taking methanol as an example) is added in denitrification filtering ponds by chemical feed pipe, circulation
Water pump is mixed into methanol uniformly in the water in pond.Check valve prevents the aqueous reflux in denitrification pond to chemical feed pipe.
3, the water for flowing through by-pass filtration pond and flowing through denitrification filtering ponds eventually flows to be located at dividing at the top of secondary filtration pond
On water sieve plate a, water sieve plate a is divided to make the uniform sprinkle of water on inclined tube filler, finally collect in secondary filtration pond bottom of pond, gone out from master
Water pipe flows out this system.In the process, water constantly collides with inclined tube filler when flowing through hanging inclined tube filler, most
The big possible surface area for increasing water, the nitrobacteria grown on inclined tube filler further divide the harmful substance in water
Solution.
Large quantity of air is blown into secondary filtration bottom of pond portion by air inlet pipe by air blower at the same time, using inclined tube filler
It is discharged at the top of from pond.Air comes into full contact with the water that sprinkle gets off, and the pernicious gases such as carbon dioxide in water are taken out of, and by oxygen
Gas is added in water.This process realizes the degassing to water and the effect of dissolved oxygen.
4, it after equipment has worked a period of time, is decomposed according to the change of water quality of filtering ponds Inlet and outlet water and filtering ponds
Total solid substance amount, to determine when to backwash this filtering ponds.
When backwashing by-pass filtration pond: closing water inlet and the flow control valve of main water inlet tube, the position meeting of by-pass filtration pool inner water
In overflow pipe a most lower edge, recoil valve a is opened at this time, and a large amount of high pressure gas are sprayed from the aeration aperture on Pneumatic support a, will
Water agitation in entire pond is got up, so that the biomembrane for nitrifying aging in filler surface be rinsed;By multi-time inflating
The sewage in pond is all exhausted from main water inlet tube afterwards, then reopens water inlet and the flow control valve of main water inlet tube, allows system
It is restored to filtration condition.
When backwashing denitrification filtering ponds: closing flow control valve and water circulating pump, denitrification filtering pool water level can be in
Overflow pipe b most lower edge opens recoil valve c at this time, and a large amount of high pressure gas are sprayed from the aeration aperture on Pneumatic support c, will be entire
Water agitation in pond is got up, so that the biomembrane of aging in denitrification filler surface be rinsed;It is dynamic by multi-time inflating
After work, open after blowdown valve all exhausts the water in pond from sewage draining exit, turn off blowdown valve, reopen flow control valve with
Water circulating pump allows denitrification filtering ponds to be restored to filtration condition.
When backwashing secondary filtration pond: closing the water outlet of primary flow pipe, when water level rises to overflow pipe b most lower edge, close
The water inlet of main water inlet tube is closed, opens recoil valve b at this time, a large amount of high pressure gas are sprayed from the aeration aperture on Pneumatic support b, will be whole
Water agitation in a pond is got up, so that the biomembrane of aging in inclined tube filler surface be rinsed;After multi-time inflating
Sewage in pond is all exhausted from primary flow pipe, then reopens the water inlet of main water inlet tube and the water outlet of primary flow pipe, allows and is
System is restored to filtration condition.
Claims (4)
1. a kind of three groups of formula circulating water cultivation biological filter systems of zero-emission type, this system is by by-pass filtration pond, secondary filtration
Three independent ponds compositions that pond and denitrification filtering ponds are interconnected, it is characterised in that: the by-pass filtration pond, second level mistake
Filter tank and denitrification filtering ponds be include being not limited to cylindric, prism-shaped geometry, three basin bottoms are in funnel
Type, funnel type bottom of pond top are provided with Pneumatic support, biologic packing material are provided in the pond above bracket, biologic packing material is
Fixed inclined tube filler;The by-pass filtration pond funnel type bottom of pond lowest point is provided with main water inlet tube, sewage to be processed
It is entered in system by main water inlet tube, most of water is flowed into secondary filtration from the overflow pipe a at top after flowing through nitrification filler
Pond is divided on water sieve plate a, and least a portion of water enters denitrification filtering ponds via denitrification filtering ponds water inlet pipe, enters anti-nitre
The water conservancy water circulating pump for changing filtering ponds makes it pass through denitrification filler repeatedly, is finally flowed into secondary filtration pond from overflow pipe b
Divide on water sieve plate a, divide water sieve plate a make water sprinkle and under, water droplet, which flows through, later concentrates on bottom of pond after drop filter filler, and from it is main go out
Water pipe outflow system.
2. three groups of formula circulating water cultivation biological filter systems of zero-emission type according to claim 1, it is characterised in that: institute
The by-pass filtration bottom of pond portion stated is in funnel type, and funnel type bottom of pond lowest point is provided with main water inlet tube;Above the main water inlet tube
It is provided with Pneumatic support a;The by-pass filtration pond is provided with the spilling water for being connected to secondary filtration pond on the pool wall at top
Pipe a;Inside the by-pass filtration pond, completely nitrification filler is filled between overflow pipe a and Pneumatic support a;The nitrification filler leans on
Nearly top position is provided with denitrification filtering ponds water inlet pipe, and denitrification filtering ponds water inlet pipe water inlet is embedded in nitrification filler, separately
Outer one end is connected to bottom of pond pipe, is provided with flow control valve among pipeline;Recoil tracheae a is connected on the Pneumatic support a,
The recoil end tracheae a is provided with recoil valve a.
3. three groups of formula circulating water cultivation biological filter systems of zero-emission type according to claim 1, it is characterised in that: institute
For the denitrification filtering bottom of pond portion stated in funnel type, funnel type bottom of pond lowest point is provided with bottom of pond pipe;It is set above the bottom of pond pipe
It is equipped with Pneumatic support c;The denitrification filtering ponds are provided with the spilling water for being connected to secondary filtration pond on the pool wall at top
Pipe b;The pipeline lowest point of the overflow pipe b is lower than the pipeline lowest point of overflow pipe a;Inside the denitrification filtering ponds, overflow
Full denitrification filler is filled between water pipe b and Pneumatic support c;It is provided between overflow pipe b at the top of the denitrification filler
Divide water sieve plate b;Described dividing below water sieve plate b is provided with circulation water inlet pipe between denitrification filler;The circulation water inlet
Pipe other end is connected with circulating pump, and circulating pump water outlet is connected with recirculation return pipe;The recirculation return pipe is close to circulation
Pump position is provided with chemical feed pipe, is provided with check valve on chemical feed pipe;The recirculation return pipe other end is connected to bottom of pond pipe;
Recoil tracheae c is connected on the Pneumatic support c, the recoil end tracheae c is provided with recoil valve c.
4. three groups of formula circulating water cultivation biological filter systems of zero-emission type according to claim 1, it is characterised in that: institute
The secondary filtration bottom of pond portion stated is in funnel type, and funnel type bottom of pond lowest point is provided with primary flow pipe;Above the primary flow pipe
It is provided with Pneumatic support b;The secondary filtration pond is provided with a point water sieve plate a close to top position, divides the position water sieve plate a slightly lower
In overflow pipe b;Full drop filter filler is filled in described dividing between water sieve plate a and Pneumatic support b bracket;On the Pneumatic support b
It is connected with recoil tracheae b, the recoil end tracheae b is provided with recoil valve b;It is provided with air inlet pipe below the Pneumatic support b,
Air inlet pipe one end nozzle is opened inside secondary filtration pond, is connected with air blower on other end nozzle.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201820363495.8U CN208200514U (en) | 2018-03-17 | 2018-03-17 | Three groups of formula circulating water cultivation biological filter systems of zero-emission type |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201820363495.8U CN208200514U (en) | 2018-03-17 | 2018-03-17 | Three groups of formula circulating water cultivation biological filter systems of zero-emission type |
Publications (1)
Publication Number | Publication Date |
---|---|
CN208200514U true CN208200514U (en) | 2018-12-07 |
Family
ID=64528342
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201820363495.8U Active CN208200514U (en) | 2018-03-17 | 2018-03-17 | Three groups of formula circulating water cultivation biological filter systems of zero-emission type |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN208200514U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110272122A (en) * | 2018-03-17 | 2019-09-24 | 顾向前 | Three groups of formula circulating water cultivation biological filter systems of zero-emission type |
CN110745943A (en) * | 2019-10-30 | 2020-02-04 | 苏州工业园区清源华衍水务有限公司 | Method for denitrification based on short-term hunger and denitrification biological filter system |
-
2018
- 2018-03-17 CN CN201820363495.8U patent/CN208200514U/en active Active
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110272122A (en) * | 2018-03-17 | 2019-09-24 | 顾向前 | Three groups of formula circulating water cultivation biological filter systems of zero-emission type |
CN110272122B (en) * | 2018-03-17 | 2024-03-08 | 顾向前 | Zero-emission three-group biological filtration system for circulating water culture |
CN110745943A (en) * | 2019-10-30 | 2020-02-04 | 苏州工业园区清源华衍水务有限公司 | Method for denitrification based on short-term hunger and denitrification biological filter system |
CN110745943B (en) * | 2019-10-30 | 2021-11-02 | 苏州工业园区清源华衍水务有限公司 | Method for denitrification based on short-term hunger and denitrification biological filter system |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US6447681B1 (en) | Aquaculture wastewater treatment system and method of making same | |
CN201733730U (en) | Grouper factory circulating water aquaculture device | |
CN205528306U (en) | Float water processing system that water treatment facilities and this equipment of application are synthesized to formula | |
CN101606506A (en) | The circulating water culture system of intensification | |
CN1120658C (en) | Closed circulation cultivation system | |
CN106396298A (en) | Purification device for treating poultry farming wastewater through solar bio-floating bed | |
CN110547238B (en) | A kind of aquaculture ecosystem and control method thereof | |
CN100554182C (en) | A kind of external membrane bioreactor system of sewage disposal and method of disposing of sewage thereof of being used for | |
CN208200514U (en) | Three groups of formula circulating water cultivation biological filter systems of zero-emission type | |
CN110720420A (en) | Take water farming systems of anaerobism denitrification facility | |
CN213416601U (en) | Aquaculture circulating water treatment system | |
CN114380454A (en) | TMBR sewage treatment process based on MABR and MBR | |
CN206720966U (en) | A factory high-density aquaculture system | |
CN109516559A (en) | Integrated sewage disposal equipment for reclaiming | |
WO2016159870A1 (en) | Moving bed bioreactor and water treatment process | |
CN209507740U (en) | Integrated sewage disposal equipment for reclaiming | |
DE10043595B4 (en) | water filters | |
CN105000761B (en) | The method removing nitrogen in high density fish culture recirculated water | |
CN111357703A (en) | Water body culture and planting circulating ecological system | |
CN217202420U (en) | TMBR sewage treatment system based on MABR and MBR | |
CN212770055U (en) | Biochemical treatment system for breeding tail water | |
CN215123371U (en) | Circulating water fishpond system | |
CN206219375U (en) | A kind of processing system for livestock breeding wastewater | |
CN110272122A (en) | Three groups of formula circulating water cultivation biological filter systems of zero-emission type | |
CN210642011U (en) | Circulating seawater culture system based on microalgae-strain bioreactor |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant |