CN209161799U - Unpowered full-buried type rural domestic waste processing unit - Google Patents
Unpowered full-buried type rural domestic waste processing unit Download PDFInfo
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- CN209161799U CN209161799U CN201821980577.3U CN201821980577U CN209161799U CN 209161799 U CN209161799 U CN 209161799U CN 201821980577 U CN201821980577 U CN 201821980577U CN 209161799 U CN209161799 U CN 209161799U
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- aerobic
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- 238000012545 processing Methods 0.000 title claims abstract description 13
- 239000010791 domestic waste Substances 0.000 title claims abstract description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 62
- 239000000835 fiber Substances 0.000 claims abstract description 37
- 239000010802 sludge Substances 0.000 claims abstract description 17
- 238000012423 maintenance Methods 0.000 claims abstract description 8
- 239000012528 membrane Substances 0.000 claims description 39
- 239000010865 sewage Substances 0.000 claims description 37
- 239000007789 gas Substances 0.000 claims description 25
- 238000004891 communication Methods 0.000 claims description 13
- 230000002906 microbiologic effect Effects 0.000 claims description 7
- 239000011148 porous material Substances 0.000 claims description 7
- 239000001301 oxygen Substances 0.000 claims description 5
- 229910052760 oxygen Inorganic materials 0.000 claims description 5
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 3
- 239000002351 wastewater Substances 0.000 abstract description 4
- 238000005273 aeration Methods 0.000 abstract description 3
- 238000005265 energy consumption Methods 0.000 abstract description 3
- 230000006641 stabilisation Effects 0.000 abstract 1
- 238000011105 stabilization Methods 0.000 abstract 1
- 239000005416 organic matter Substances 0.000 description 5
- 238000001914 filtration Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 239000011499 joint compound Substances 0.000 description 2
- 230000000717 retained effect Effects 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 238000005276 aerator Methods 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 238000003287 bathing Methods 0.000 description 1
- 238000002306 biochemical method Methods 0.000 description 1
- 239000000969 carrier Substances 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 230000000593 degrading effect Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000002957 persistent organic pollutant Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 239000008213 purified water Substances 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
- 241001148471 unidentified anaerobic bacterium Species 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
- 229940088594 vitamin Drugs 0.000 description 1
- 229930003231 vitamin Natural products 0.000 description 1
- 235000013343 vitamin Nutrition 0.000 description 1
- 239000011782 vitamin Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Landscapes
- Biological Treatment Of Waste Water (AREA)
Abstract
The utility model relates to domestic living waste water treaters, specially unpowered full-buried type rural domestic waste processing unit, solving existing rural domestic waste processing unit needs power repeatedly to be promoted, additional blast aeration equipment, energy consumption is high, the big problem of noise, scheme: including anaerobic jar and aerobic tank, anaerobic sludge filter layer, fibre bundle separator for mud and water are equipped in anaerobic jar；Biological bed, fibre bed are equipped in aerobic tank；It is connected with water route, gas circuit communicating pipe between tank, is connected with vortex ventilator respectively.Advantage: it is not necessarily to power Multi-stage lifting；Without being aerated blast apparatus, not power consumption, energy-saving and noise-reducing；Automatic running, it is unattended；There is relatively strong anti-load-bearing capacity, water stabilization is up to standard；Occupied area is small, and investment is low, consumes energy low, and equipment fault is few, and maintenance is simple.
Description
Technical field
The utility model relates to domestic living waste water treater, specially unpowered full-buried type rural domestic waste processing dress
It sets.
Background technique
Domestic sewage in rural areas discharges approach mainly from kitchen drainage, lavatory draining and bathing wastewater, domestic sewage in rural areas
Mainly have: directly spilling and be discharged into river to the ground, nearby, enter river by sewer etc., causes river, pool pollution, influence resident
Living environment seriously threatens resident's health.Domestic sewage in rural areas be noteworthy characterized by intermittent discharge, displacement it is small and disperse,
Far from blowdown pipe network and big water body, wastewater treatment rate is low, and management level is low.The source of sanitary sewage is simultaneously uncomplicated, only resident
Extensively, after discharge sewage belongs to pollution of area source to life range, it is difficult to focus on.The country is for the universal of domestic sewage in rural areas at present
Processing mode is biochemical method, mainly activated sludge and MBR etc..
Existing small water spread source sewage disposal technology and equipment are different degrees of, and there are following some defects: 1, using
Traditional handicraft is taken up an area larger；2, pollution of area source is dispersed for villages and small towns, using traditional handicraft, high investment；3, process flow is superfluous
It is long, it needs repeatedly to be promoted；4, additional blast aeration equipment, energy consumption is higher, and noise is larger；5, special operational management people is needed
Member, and related personnel must have certain Specialized Quality；6, uneven water is easy to cause effluent quality to fluctuate, and causes exceeded outer
Row.Therefore, design a kind of full-buried type domestic living waste water treater suitable for rural area be very it is necessary to.
Summary of the invention
The utility model solves existing rural domestic waste processing unit and power is needed repeatedly to be promoted, additional blast aeration
Equipment, energy consumption is high, and the big problem of noise provides a kind of unpowered full-buried type rural domestic waste processing unit.
The utility model is achieved through the following technical solutions: unpowered full-buried type rural domestic waste processing dress
Set, including anaerobic jar, middle part is provided with anaerobic sludge filter layer in the anaerobic jar, the anaerobic jar top be provided with sewage into
Water pipe, the sewage water inlet pipe pass through anaerobic sludge filter layer after protruding into anaerobic jar, and the sewage water inlet pipe lower end, which is connected with, to be set
It is placed in the first water distributor of anaerobism pot bottom；It is provided with maintenance pore at the top of the anaerobic jar, is provided in the maintenance pore
Fibre bundle separator for mud and water, fibre bundle separator for mud and water lower end are higher than anaerobic sludge filter layer upper surface；It further include aerobic
Biomembrane tank is connected with water route communicating pipe, the water route communicating pipe between aerobic biologic membrane tank top and anaerobic jar top
One end and the connectivity port of anaerobic jar are higher than fibre bundle separator for mud and water upper end, and the water route communicating pipe other end protrudes into aerobic life
In object film tank and it is connected with the second water distributor；Bottom biology modules are disposed with upwards by bottom in the aerobic biologic membrane tank
Bed, fiber biological bed, top biology modules bed, the top biology modules bed use hollow out carrier, and load has aerobic microbiological
Film, the fiber biological bed use fibre bundle carrier, and load has aerobic microbiological, and the bottom biology modules bed is carried using hollow out
Body, load have aerobic biologic membrane；Be vertically arranged with gas distribution pipe outside the aerobic biologic membrane tank, the gas distribution pipe top be connected with into
Tracheae, the gas distribution pipe top are connected with the upper layer air communication pipe with the perforation of aerobic biologic membrane tank, the upper layer air communication
The connection end of pipe and aerobic biologic membrane tank is higher than top biology modules bed upper surface, is separately connected in the middle part of the gas distribution pipe with lower part
Have and the perforation of aerobic biologic membrane tank, and lower air communicating pipe corresponding with fiber biological bed, bottom biology modules bed respectively
And drainpipe, the gas distribution pipe lower end are also connected with outlet pipe, the outlet pipe height is lower than drainpipe height；The aerobic life
Be also connected with air communication pipe between at the top of object film tank top and anaerobic jar, at the top of the anaerobic jar with fiber biological bed pair
The vortex ventilator basseted is also respectively connected in side wall.Anaerobic sludge filter layer is set in anaerobic jar, and sewage is through water inlet pipe
Import anaerobism pot bottom, anaerobism pot bottom be distributed in by the first water distributor, anaerobic sludge filter layer be immersed in the water surface for a long time hereinafter,
The biomembrane using anaerobic bacteria as dominant bacteria is filtered out, the organic matter in sewage is retained, is degraded.Sewage is through anaerobic sludge
After filter layer processing, by fibre bundle separator for mud and water, water route communicating pipe flowing into aerobic biologic membrane tank, fibre bundle separator for mud and water
In fibre bundle filtration core separating and filtering sewage in solid waste.Upper layer biology modules bed, fiber in aerobic biologic membrane tank
Biological bed, bottom biology modules bed are successively reacted with sewage, are retained, are degraded respectively, the organic matter in filter sewage, then by arranging
Water pipe is discharged after flowing into gas distribution pipe through outlet pipe.Upper layer air communication pipe, lower layer are connected between gas distribution pipe and aerobic biologic membrane tank
Air communication pipe, respectively upper layer biology modules bed provide the oxygen-enriched environment of high load capacity, are fiber biological bed and bottom biology mould
Block bed provides micro- oxygen environment of underload, to retain, to degrade between each layer, organic matter different in filter sewage.Anaerobic jar
It has been respectively communicated with vortex ventilator with aerobic biologic membrane tank top, has been rotated under extraneous subtle wind-force effect, anaerobic jar is become reconciled
Gas extraction in oxygen biomembrane tank, forms negative pressure in tank, and fresh air is promoted to enter aerobic life through gas distribution pipe by air inlet pipe
In object film tank, guarantee the living environment for supporting microorganism.
The utility model has the advantage that 1, sewage flows automatically entirely from inlet water to outlet water, is not necessarily to Multi-stage lifting；2, sufficiently sharp
The molten gas of negative pressure is formed with water flow and natural wind convection current, special aerator is not necessarily to, does not need power consumption；3, air blower is saved to set
It is standby, energy-saving and noise-reducing；4, package unit fully automatic operation is not necessarily to staff on duty；5, equipment uses biofilm, there is relatively strong anti-load
Ability, effectively solve the problems, such as water quality and quantity it is unstable cause out water unstable it is up to standard；6, compared with traditional equipment, occupied area
Small, investment is low, consumes energy low, and equipment fault is few, and maintenance is simple.
Detailed description of the invention
FIG. 1 is a schematic structural view of the utility model；
Fig. 2 is Fig. 1 top view；
Fig. 3 is vortex ventilator schematic diagram；
In figure: 1- anaerobic jar, 2- anaerobic sludge filter layer, 3- sewage water inlet pipe, the first water distributor of 4-, 5- overhaul pore,
6- fibre bundle separator for mud and water, 7- aerobic biologic membrane tank, the water route 8- communicating pipe, the second water distributor of 9-, the bottom 10- biology modules
Bed, 11- fiber biological bed, the top 12- biology modules bed, 13- gas distribution pipe, 14- air inlet pipe, the upper layer 15- air communication pipe, 16-
Lower air communicating pipe, 17- drainpipe, 18- outlet pipe, 19- air communication pipe, 20- are vortexed ventilator.
Specific embodiment
Unpowered full-buried type rural domestic waste processing unit, including anaerobic jar 1, the interior middle part setting of the anaerobic jar 1
There is anaerobic sludge filter layer 2,1 top of anaerobic jar is provided with sewage water inlet pipe 3, and the sewage water inlet pipe 3 protrudes into anaerobic jar 1
Anaerobic sludge filter layer 2 is passed through afterwards, and 3 lower end of sewage water inlet pipe is connected with the first water distributor for being set to 1 bottom of anaerobic jar
4；It is provided with maintenance pore 5 at the top of the anaerobic jar 1, is provided with fibre bundle separator for mud and water 6 in the maintenance pore 5, it is described
6 lower end of fibre bundle separator for mud and water is higher than 2 upper surface of anaerobic sludge filter layer；It further include aerobic biologic membrane tank 7, the aerobic life
Water route communicating pipe 8, described 8 one end of water route communicating pipe and anaerobic jar 1 are connected between 7 top of object film tank and 1 top of anaerobic jar
Connectivity port is higher than 6 upper end of fibre bundle separator for mud and water, and 8 other end of water route communicating pipe protrudes into aerobic biologic membrane tank 7 simultaneously
It is connected with the second water distributor 9；It is disposed with bottom biology modules bed 10, fibre in the aerobic biologic membrane tank 7 upwards by bottom
Vitamins bed 11, top biology modules bed 12, the top biology modules bed 12 use hollow out carrier, and load has aerobic microbiological
Film, the fiber biological bed 11 use fibre bundle carrier, and load has aerobic microbiological, and the bottom biology modules bed 10 is used and engraved
Empty carrier, load have aerobic biologic membrane；Gas distribution pipe 13 is vertically arranged with outside the aerobic biologic membrane tank 7, the gas distribution pipe 13 pushes up
End is connected with air inlet pipe 14, and 13 top of gas distribution pipe is connected with the upper layer air communication pipe 15 penetrated through with aerobic biologic membrane tank 7,
The connection end of the upper layer air communication pipe 15 and aerobic biologic membrane tank 7 is higher than 12 upper surface of top biology modules bed, the cloth
The middle part of tracheae 13 and lower part are connected separately with to be penetrated through with aerobic biologic membrane tank 7, and biological with fiber biological bed 11, bottom respectively
The corresponding lower air communicating pipe 16 of module bed 10 and drainpipe 17,13 lower end of gas distribution pipe are also connected with outlet pipe 18, institute
18 height of outlet pipe is stated lower than 17 height of drainpipe；It is also connected between 7 top of aerobic biologic membrane tank and 1 top of anaerobic jar
Air communication pipe 19,1 top of the anaerobic jar and fiber biological bed 11 pair side wall the whirlpool basseted is also respectively connected
Flow ventilator 20.
When installing and using, anaerobic jar 1, aerobic biologic membrane tank 7, gas distribution pipe 13 are embedded in underground, air inlet pipe 14, vortex ventilation
Device 20 bassets above.Sanitary sewage flows into 1 bottom of anaerobic jar by sewage water inlet pipe 3, during sewage rises from bottom to top,
It is acted on by anaerobic sludge filter layer 2, the organic matter in sewage is trapped, degrades, while upper layer sludge and sewage are formed and mixed completely
Conjunction state removes the majority of organic pollutants in sewage, while can also improve sewage in the case where being thoroughly mixed anaerobic state
Biodegradability, so that subsequent processing is more easier；Sewage after reaction is through entering fibre bundle separator for mud and water 6, water route communicating pipe 8
The filtration core of aerobic biologic membrane tank 7, fibre bundle separator for mud and water 6 retains anaerobic sludge, avoids enter into aerobic biologic membrane tank 7；It is dirty
After water enters aerobic biologic membrane tank 7, top biology modules bed 12 is first flowed through, hollow out carrier is used, it can be abundant with air
Contact, supported on carriers aerobic microbiological film form first layer high load capacity aerobic stage；Middle layer uses fibre bundle carrier, thoroughly
Gas is good, has both crown_interception, while aerobic microbiological degrades retain pollutant by cellulose carrier again；Sewage passes through
After fiber biological bed 11, into bottom biology modules bed 10, organic matter in sewage of further degrading under micro- oxygen environment is formed
Underload aerobic environment.For sewage after layer-by-layer biological membrane degradation, filtering, purified water flows into 13 bottom of gas distribution pipe through drainpipe 17,
Then by 18 discharger of outlet pipe.In sewage disposal process, anaerobic jar 1 is communicated with respectively with 7 top of aerobic biologic membrane tank
It is vortexed ventilator 20, is rotated under extraneous subtle wind-force effect, the gas in anaerobic jar 1 and aerobic biologic membrane tank 7 is extracted out,
Negative pressure is formed in tank, is promoted fresh air to be entered in aerobic biologic membrane tank 7 by air inlet pipe 14 through gas distribution pipe 13, is guaranteed to support micro- life
The living environment of object.
Claims (1)
1. a kind of unpowered full-buried type rural domestic waste processing unit, it is characterised in that: described to detest including anaerobic jar (1)
Middle part is provided with anaerobic sludge filter layer (2) in oxygen tank (1), and anaerobic jar (1) top is provided with sewage water inlet pipe (3), institute
It states sewage water inlet pipe (3) and protrudes into anaerobic jar (1) afterwards across anaerobic sludge filter layer (2), sewage water inlet pipe (3) the lower end connection
There is the first water distributor (4) for being set to anaerobic jar (1) bottom；Maintenance pore (5) is provided at the top of the anaerobic jar (1), it is described
It is provided with fibre bundle separator for mud and water (6) in maintenance pore (5), it is dirty that fibre bundle separator for mud and water (6) lower end is higher than anaerobism
Mud filter layer (2) upper surface；It further include aerobic biologic membrane tank (7), on aerobic biologic membrane tank (7) top and anaerobic jar (1)
It is connected between portion water route communicating pipe (8), the connectivity port of described water route communicating pipe (8) one end and anaerobic jar (1) is higher than fiber
Beam separator for mud and water (6) upper end, water route communicating pipe (8) other end protrude into aerobic biologic membrane tank (7) and are connected with second
Water distributor (9)；It is raw to be disposed with bottom biology modules bed (10), fiber in the aerobic biologic membrane tank (7) upwards by bottom
Object bed (11), top biology modules bed (12), the top biology modules bed (12) use hollow out carrier, and load has aerobic micro- life
Object film, the fiber biological bed (11) use fibre bundle carrier, and load has aerobic microbiological, the bottom biology modules bed (10)
Using hollow out carrier, load has aerobic biologic membrane；It is vertically arranged with gas distribution pipe (13) outside the aerobic biologic membrane tank (7), it is described
Gas distribution pipe (13) top is connected with air inlet pipe (14), and gas distribution pipe (13) top is connected with to be penetrated through with aerobic biologic membrane tank (7)
Upper layer air communication pipe (15), the connection end of the upper layer air communication pipe (15) and aerobic biologic membrane tank (7) is higher than top
Biology modules bed (12) upper surface, in the middle part of the gas distribution pipe (13) and lower part is connected separately with and aerobic biologic membrane tank (7) perforation
, and lower air communicating pipe (16) corresponding with fiber biological bed (11), bottom biology modules bed (10) and drainpipe respectively
(17), gas distribution pipe (13) lower end is also connected with outlet pipe (18), and the outlet pipe (18) is highly high lower than drainpipe (17)
Degree；Air communication pipe (19), the anaerobism are also connected between at the top of the aerobic biologic membrane tank (7) and at the top of anaerobic jar (1)
At the top of tank (1) with fiber biological bed (11) pair side wall the vortex ventilator (20) basseted is also respectively connected.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821980577.3U CN209161799U (en) | 2018-11-29 | 2018-11-29 | Unpowered full-buried type rural domestic waste processing unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821980577.3U CN209161799U (en) | 2018-11-29 | 2018-11-29 | Unpowered full-buried type rural domestic waste processing unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209161799U true CN209161799U (en) | 2019-07-26 |
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ID=67340895
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821980577.3U Active CN209161799U (en) | 2018-11-29 | 2018-11-29 | Unpowered full-buried type rural domestic waste processing unit |
Country Status (1)
| Country | Link |
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| CN (1) | CN209161799U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111592198A (en) * | 2020-06-11 | 2020-08-28 | 安徽蓝鼎环保能源科技有限公司 | Biochemical treatment method and device for landfill leachate |
-
2018
- 2018-11-29 CN CN201821980577.3U patent/CN209161799U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111592198A (en) * | 2020-06-11 | 2020-08-28 | 安徽蓝鼎环保能源科技有限公司 | Biochemical treatment method and device for landfill leachate |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Non-power fully buried rural domestic wastewater treatment device Effective date of registration: 20230208 Granted publication date: 20190726 Pledgee: China CITIC Bank Co.,Ltd. Taiyuan Branch Pledgor: TAIYUAN RUNMIN ENVIRONMENTAL PROTECTION ENERGY SAVING Co.,Ltd. Registration number: Y2023140000007 |
|
| PC01 | Cancellation of the registration of the contract for pledge of patent right | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Granted publication date: 20190726 Pledgee: China CITIC Bank Co.,Ltd. Taiyuan Branch Pledgor: TAIYUAN RUNMIN ENVIRONMENTAL PROTECTION ENERGY SAVING Co.,Ltd. Registration number: Y2023140000007 |
|
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Non powered fully buried rural domestic wastewater treatment device Granted publication date: 20190726 Pledgee: China CITIC Bank Co.,Ltd. Taiyuan Branch Pledgor: TAIYUAN RUNMIN ENVIRONMENTAL PROTECTION ENERGY SAVING Co.,Ltd. Registration number: Y2024140000010 |