CN206109148U - Portable aquaculture wastewater treatment integration equipment - Google Patents
Portable aquaculture wastewater treatment integration equipment Download PDFInfo
- Publication number
- CN206109148U CN206109148U CN201621053840.5U CN201621053840U CN206109148U CN 206109148 U CN206109148 U CN 206109148U CN 201621053840 U CN201621053840 U CN 201621053840U CN 206109148 U CN206109148 U CN 206109148U
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- CN
- China
- Prior art keywords
- abr
- wastewater purification
- integration apparatus
- pond
- filler
- 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.)
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- 230000010354 integration Effects 0.000 title claims abstract description 17
- 238000009360 aquaculture Methods 0.000 title abstract 2
- 244000144974 aquaculture Species 0.000 title abstract 2
- 238000004065 wastewater treatment Methods 0.000 title abstract 2
- 238000004062 sedimentation Methods 0.000 claims abstract description 24
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 24
- 239000000945 filler Substances 0.000 claims abstract description 20
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 20
- 230000003647 oxidation Effects 0.000 claims abstract 3
- 239000002351 wastewater Substances 0.000 claims description 26
- 238000000746 purification Methods 0.000 claims description 17
- 238000005273 aeration Methods 0.000 claims description 16
- 239000007788 liquid Substances 0.000 claims description 14
- 230000001174 ascending effect Effects 0.000 claims description 8
- 238000007667 floating Methods 0.000 claims description 7
- 229910000975 Carbon steel Inorganic materials 0.000 claims description 3
- 238000005452 bending Methods 0.000 claims description 3
- 239000010962 carbon steel Substances 0.000 claims description 3
- 238000005660 chlorination reaction Methods 0.000 claims description 2
- 239000000725 suspension Substances 0.000 claims description 2
- 230000003197 catalytic effect Effects 0.000 claims 1
- 238000004659 sterilization and disinfection Methods 0.000 claims 1
- 239000002028 Biomass Substances 0.000 abstract description 4
- 230000000813 microbial effect Effects 0.000 abstract description 4
- 230000000694 effects Effects 0.000 abstract description 3
- 244000005700 microbiome Species 0.000 abstract description 3
- 238000000034 method Methods 0.000 description 12
- 238000009395 breeding Methods 0.000 description 7
- 230000001488 breeding effect Effects 0.000 description 7
- 230000008569 process Effects 0.000 description 6
- 239000010865 sewage Substances 0.000 description 6
- 239000010802 sludge Substances 0.000 description 6
- 244000144972 livestock Species 0.000 description 5
- 238000012856 packing Methods 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000000706 filtrate Substances 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 230000000903 blocking effect Effects 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 244000144977 poultry Species 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 238000005276 aerator Methods 0.000 description 1
- 241001148470 aerobic bacillus Species 0.000 description 1
- 230000001112 coagulating effect Effects 0.000 description 1
- 230000029087 digestion Effects 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000005189 flocculation Methods 0.000 description 1
- 230000016615 flocculation Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- RUTXIHLAWFEWGM-UHFFFAOYSA-H iron(3+) sulfate Chemical compound [Fe+3].[Fe+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O RUTXIHLAWFEWGM-UHFFFAOYSA-H 0.000 description 1
- 229910000360 iron(III) sulfate Inorganic materials 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 230000032258 transport Effects 0.000 description 1
- 238000009280 upflow anaerobic sludge blanket technology Methods 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
- 239000010457 zeolite Substances 0.000 description 1
Landscapes
- Biological Treatment Of Waste Water (AREA)
Abstract
The utility model relates to a portable aquaculture wastewater treatment integration equipment, including the casing, be equipped with the ABR pond, contact oxidation tank, sedimentation tank and the equipment room that communicate in proper order in the casing, separate through the baffle in the ABR pond has at least three check room, and wherein, dirty district and upper reaches district are all separated into through the folded plate in the intake check room of the check room of head end for being equipped with the inlet tube, all the other check rooms, and are equipped with the filler at least in the upper reaches district of terminal check room, and the upper reaches district is 5 with the volume ratio in dirty district: 1~3: 1, the folded plate is bent near the next check room of tip orientation of ABR pond bottom of the pool and just and between the bottom of the pool of ABR pond is had the clearance, and the top of folded plate is higher than the top of baffle. The utility model provides a check room that intakes in ABR pond does not set up dirty district, prevents into that the too high emergence of water load stops up, and the indoor increase of two last check is packed, holds back with the anaerobic microorganisms who adheres to wherein anaerobism mud, carries top grafting and touches the oxidation pond quality of water of intaking, has increased the interior microbial biomass of unit volume simultaneously, has improved the treatment effect.
Description
Technical field
The utility model is related to sewage treatment area, more particularly to a kind of portable cultivating wastewater purification integration apparatus.
Background technology
Distributing and small-scale plant are difficult to its scale at this stage as rural area pillar of the local economy industry
And standardization, breeding way is lack of standardization, cultivation amount fluctuation larger, pollutant emission point dispersion, economic level are limited etc. all becomes
The key factor of restricting rural distributing cultivating wastewater purification.The direct discharge of rural area distributing breeding wastewater will be to its ecological ring
Border damages.
Application No. CN201210201431.5 Chinese patent application discloses integrated livestock and poultry cultivating wastewater purification method.
The method is realized by following technology path：1. after breeding wastewater unification is collected, to add and use solid-liquid after bodied ferric sulfate flocculation
Seperator carries out initial gross separation；2. the waste water after separating carries out anaerobic digestion by UASB anaerobic techniques；3. waste water enters after decomposing
Entering carries out a series of senior physical reactions in the closed circuit generating means of ultrasonic wave；4. waste water Jing ozone after physical filtering after reacting
Reaction tower carries out fully oxidized reaction；5. filtered finally by filtrates such as activated carbon and zeolites.The method processes livestock and poultry and supports
Grow waster water process route more complicated, need special messenger to operate and operating personnel's specialty is required higher；By the way of coagulating sedimentation
Separation of solid and liquid is carried out, increases operating cost and operation difficulty, therefore the method is more suitable for industrialized production.
Application No. CN201420263050.4 Chinese patent application discloses a kind of livestock breeding wastewater integrated treatment
Equipment.The equipment includes the housing in settling zone, anaerobic zone, aerobic zone, Disengagement zone and Zhong Chen areas.Anaerobism is provided with anaerobic zone
Bacterium, is provided with aerobic bacteria in aerobic zone, three phase separator is provided with Disengagement zone, also includes：Air blast, air blast goes out
Mouth is connected with multiple aeration heads, and aeration head is partially toward anaerobic zone and is partially toward aerobic zone.The equipment processes small-sized plant and gives up
Water substantially reduces the completion time of project than traditional civil engineering mode, but the equipment subregion is more, increases equipment effective volume；Each function
Section treatment effeciency is not high, similar to traditional AO techniques.
Application No. CN201320784239.3 Chinese patent application discloses a kind of processing system of livestock breeding wastewater.
The system includes ABR ponds, aerobic biofilter and denitrification pond, is connected by sewage conduct between ABR ponds and aerobic biofilter
Connect, sewage conduct stretches into a section of aerobic biofilter and is provided with atomizer, elevator pump, aerobic life are provided with sewage conduct
Water outlet is sent into denitrification pond by thing filter tank by pipeline, and filtrate is provided with denitrification pond, and filtrate lower section is provided with aerator,
The bottom in denitrification pond is provided with delivery port.The system anaerobic unit employs the ABR of efficient zero energy consumption, improves pollutant
Removal efficiency, but do not consider before and after ABR that compartment pollutional load is different, and sludge and growth of microorganism speed is not into before caused
Level blocking and the below not enough problem of microbial biomass.
Accordingly, the utility model is intended on the basis of above research, is opened for rural economy technical merit and cultivation characteristic
Send a set of technology for being adapted to its livestock breeding wastewater process.
Utility model content
To solve above-mentioned technical problem, the purpose of this utility model is to provide a kind of process to improve breeding wastewater and imitates
Rate, while reduce equipment operation difficulty, reduce occupation area of equipment portable cultivating wastewater purification integration apparatus.
Portable cultivating wastewater purification integration apparatus of the present utility model, including housing, are provided with successively in the housing
The ABR ponds of connection, contact-oxidation pool, sedimentation basin and equipment room, the ABR ponds are separated by dividing plate at least three compartments, its
In, the compartment of head end is the water inlet compartment for being provided with water inlet pipe, and remaining compartment is separated into lower current area and ascending zone by flap, and
Filler is at least provided with the ascending zone of end compartment, the ascending zone is 5 with the volume ratio of lower current area：1～3：1；The folding
Plate has gap, the flap towards next compartment bending and between the bottom of pond of ABR ponds near the end of ABR ponds bottom of pond
Top higher than the dividing plate top.
Further, the sedimentation basin is vertical sedimentation basin, and between the contact-oxidation pool and sedimentation basin top is provided with
Higher than contact-oxidation pool and the baffle plate on sedimentation basin top.
Further, described filler is floating stuffing, preferred particle column floating stuffing.
Further, aerating pipelines, carrier filler and liquid level gauge are provided with the contact-oxidation pool.
Further, the aerating pipelines are boring aeration pipe or microporous aeration disc.
Further, the carrier filler is suspension type filler, floats hanging filler or floating stuffing.
Further, the liquid level is calculated as static-pressure type liquid level transmitter.
Further, be provided with the equipment room connect with the aerating pipelines Aeration fan, for controlling aeration wind
Machine and liquid level gauge and switch board, the ultra violet sterilizer of intake pump.
Further, the ultra violet sterilizer is pipeline overflow-type ultraviolet sterilizer.
Further, the housing is made up of carbon steel, and is equipped with anticorrosive coat in inner walls and outer wall.
By such scheme, the utility model at least has advantages below：
1st, water inlet compartment in ABR ponds is not provided with lower current area, reduces the failure that blocking occurs into water, due to ABR ponds water inlet lattice
The organic loading that room undertakes is higher, and the sludge speed of growth is very fast, therefore water inlet end and easy generation sludge blockage phenomenon, cancels dirty
Area can effectively reduce this failure；
2nd, last two compartments of ABR increase filler and are conducive to retaining microorganism and sludge, prevent sludge loss, improve next ring
The influent quality of section, increases the microbial biomass in reactor unit volume, improves treatment effeciency；
3rd, by increasing baffle plate between contact-oxidation pool and sedimentation basin, change the direction of a stream of water, sedimentation basin is put down by original
Streaming is changed into vertical-flow, and sedimentation effect is more preferable, more compact structure；
4th, whole device is as in integral housing, one-touch startup, simple to operate, conveniently moving.
Described above is only the general introduction of technical solutions of the utility model, in order to better understand skill of the present utility model
Art means, and being practiced according to the content of specification, with preferred embodiment of the present utility model and coordinate accompanying drawing detailed below
Describe in detail bright as after.
Description of the drawings
Fig. 1 is structural representation of the present utility model；
Fig. 2 is the structural representation in ABR ponds in the utility model.
Specific embodiment
With reference to the accompanying drawings and examples, specific embodiment of the present utility model is described in further detail.Below
Embodiment is used to illustrate the utility model, but is not limited to scope of the present utility model.
Referring to Fig. 1 and Fig. 2, a kind of portable cultivating wastewater purification integration described in the preferred embodiment of the utility model one
ABR ponds 2, contact-oxidation pool 3, sedimentation basin 4 and the equipment room 5 being sequentially communicated is provided with equipment, including housing 1, housing 1.ABR ponds
2 are separated into five equal compartments of volume by dividing plate 18, and the first compartment is water inlet compartment, water inlet pipe 6 at the top of the first compartment,
Sewage is flow automatically successively into next compartment by the first compartment Jing dividing plate 18；Four compartments are separated into upstream by flap 16 behind ABR ponds 2
The volume ratio of area 15 and lower current area 14, ascending zone 15 and lower current area 14 is 5：1～3：1；Add in the compartment of ABR ponds 2 the four, the 5th
Floating stuffing 17, in the implementation case, floating stuffing be particle column filler, filler chi Packing ratio 20%
～30%.To make sewage that the lower current area 14 and ascending zone 15 of compartment below are sequentially entered from after the entrance of the first compartment, this practicality is new
Flap 16 has gap towards next compartment bending and between the bottom of pond of ABR ponds 2 near the end of the bottom of pond of ABR ponds 2 in type, and
The top of flap 16 is made higher than the top of dividing plate 18.The water inlet compartment in the ABR ponds 2 in the utility model is not provided with lower current area, prevents
Only influent load is too high blocks, and filler is increased in last two compartment, to anaerobic sludge and attachment anaerobe therein
Retained, improved contact-oxidation pool influent quality, while increased the microbial biomass in unit volume, improve process effect
Really.
The compartment water outlet of ABR ponds 2 the 5th by top gravity flow enter contact-oxidation pool 3, contact-oxidation pool 3 comprising aerating pipelines 8,
Place packing area 7 and the liquid level gauge 9 of carrier filler.In the implementation case, aerating pipelines 8 are located at the bottom of contact-oxidation pool 3, to wear
Hole aeration tube, aeration bore dia 4mm；Packing area 7 is located at the top 200mm of aerating pipelines 8, and carrier filler is Pall ring fillerPacking ratio 40%～50%；Liquid level gauge 9 is static-pressure type liquid level transmitter, and linkage controls aeration and enters
Water, two position can be reported to the police.
By top water outlet, the baffle plate 10 that water outlet Jing is located between contact-oxidation pool 3 and sedimentation basin 4 stops contact-oxidation pool 3,
The top of baffle plate 10 can change the direction of a stream of water higher than contact-oxidation pool and sedimentation basin top, make water outlet enter sedimentation basin by bottom
4, in the implementation case, sedimentation basin 4 is vertical sedimentation basin, and water outlet is flowed out by the top of sedimentation basin 4, and gravity flow enters the equipment of being located at
Between 5 ultra violet sterilizer 12.
Equipment room 5 connects with sedimentation basin 4, and Aeration fan 11, switch board 13 and chlorination equipment 12 etc. are placed in it.In this reality
In applying case, Aeration fan 11 be preferably Roots blower, ultra violet sterilizer 12 be overflow-type ultraviolet sterilizer, switch board
13 are connected with intake pump, Aeration fan 11 and liquid level gauge 9, and by switch board 13 the one-touch startup and control of equipment can be realized
System.
ABR ponds 2, contact-oxidation pool 3, sedimentation basin 4 and equipment room 5 are placed in integrated shell 1, and housing 1 is by carbon steel system
Into thickness >=8mm, internal and external anti-corrosive, anticorrosive coat thickness >=200 μm, profile is moved easily and transports similar to packaging box mode.
The above is only preferred embodiment of the present utility model, is not limited to the utility model, it is noted that
For those skilled in the art, on the premise of without departing from the utility model know-why, can also do
Go out some improvement and modification, these are improved and modification also should be regarded as protection domain of the present utility model.
Claims (10)
1. a kind of portable cultivating wastewater purification integration apparatus, it is characterised in that：Including housing, it is provided with successively in the housing
The ABR ponds of connection, contact-oxidation pool, sedimentation basin and equipment room, the ABR ponds are separated by dividing plate at least three compartments, its
In, the compartment of head end is the water inlet compartment for being provided with water inlet pipe, and remaining compartment is separated into lower current area and ascending zone by flap, and
Filler is at least provided with the ascending zone of end compartment, the ascending zone is 5 with the volume ratio of lower current area：1～3：1；The folding
Plate has gap, the flap towards next compartment bending and between the bottom of pond of ABR ponds near the end of ABR ponds bottom of pond
Top higher than the dividing plate top.
2. portable cultivating wastewater purification integration apparatus according to claim 1, it is characterised in that：The sedimentation basin is
Vertical sedimentation basin, is provided with top higher than contact-oxidation pool and the gear on sedimentation basin top between the contact-oxidation pool and sedimentation basin
Plate.
3. portable cultivating wastewater purification integration apparatus according to claim 1, it is characterised in that：Described filler for
Grain column floating stuffing.
4. portable cultivating wastewater purification integration apparatus according to claim 2, it is characterised in that：The catalytic oxidation
Aerating pipelines, carrier filler and liquid level gauge are provided with pond.
5. portable cultivating wastewater purification integration apparatus according to claim 4, it is characterised in that：The aerating pipelines
For boring aeration pipe or microporous aeration disc.
6. portable cultivating wastewater purification integration apparatus according to claim 4, it is characterised in that：The carrier filler
For suspension type filler, float hanging filler or floating stuffing.
7. portable cultivating wastewater purification integration apparatus according to claim 4, it is characterised in that：The liquid level is calculated as
Static-pressure type liquid level transmitter.
8. portable cultivating wastewater purification integration apparatus according to claim 5, it is characterised in that：In the equipment room
It is provided with Aeration fan, the switch board for controlling Aeration fan and liquid level gauge and intake pump, the purple connected with the aerating pipelines
Outer chlorination equipment.
9. portable cultivating wastewater purification integration apparatus according to claim 8, it is characterised in that：The ultraviolet disinfection
Device is pipeline overflow-type ultraviolet sterilizer.
10. portable cultivating wastewater purification integration apparatus according to any one of claim 1-9, it is characterised in that：Institute
State housing to be made up of carbon steel, and anticorrosive coat is equipped with inner walls and outer wall.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621053840.5U CN206109148U (en) | 2016-09-13 | 2016-09-13 | Portable aquaculture wastewater treatment integration equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621053840.5U CN206109148U (en) | 2016-09-13 | 2016-09-13 | Portable aquaculture wastewater treatment integration equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206109148U true CN206109148U (en) | 2017-04-19 |
Family
ID=58518991
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621053840.5U Active CN206109148U (en) | 2016-09-13 | 2016-09-13 | Portable aquaculture wastewater treatment integration equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206109148U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113104972A (en) * | 2021-04-15 | 2021-07-13 | 桂林理工大学 | Composite two-phase integrated anaerobic reaction system |
| CN114014513A (en) * | 2021-03-26 | 2022-02-08 | 深圳市自由度环保科技有限公司 | Wastewater treatment mechanism and process in livestock and poultry breeding process |
-
2016
- 2016-09-13 CN CN201621053840.5U patent/CN206109148U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114014513A (en) * | 2021-03-26 | 2022-02-08 | 深圳市自由度环保科技有限公司 | Wastewater treatment mechanism and process in livestock and poultry breeding process |
| CN113104972A (en) * | 2021-04-15 | 2021-07-13 | 桂林理工大学 | Composite two-phase integrated anaerobic reaction system |
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| GR01 | Patent grant |