CN206616122U - A kind of decentralized type sewage processing unit - Google Patents
A kind of decentralized type sewage processing unit Download PDFInfo
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- CN206616122U CN206616122U CN201720334682.9U CN201720334682U CN206616122U CN 206616122 U CN206616122 U CN 206616122U CN 201720334682 U CN201720334682 U CN 201720334682U CN 206616122 U CN206616122 U CN 206616122U
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- filter element
- processing unit
- pond body
- sewage processing
- type sewage
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Abstract
The utility model is related to decentralized type sewage processing unit, part old town and rural area can effectively be solved and there is the in line phenomenon of sewage, subregion quality of water environment is caused constantly to deteriorate, and multiplied with foul smelling and mosquitos and flies, the problem of having had a strong impact on resident's daily life, its solve technical scheme be, closure is provided with the top of pond body, center water inlet pipe is through the center of closure and stretches into pond body bottom, deflection plate is fixed with the water inlet pipe of center, pond body top is provided with overflow delivery port, bottom side is provided with mud discharging mouth, first filter element, second filter element bottom is connected, from top to bottom provided with the first grit layer in first filter element, zeolite filler layer, the utility model reasonable in design, operation maintenance is convenient, the COD and BOD that can be largely gone in water removal by anaerobic digestion, removal organic polluter can be further removed in filter process, while the addition intensified denitrification and dephosphorization effect of specific filler, it is the innovation in sewage disposal system.
Description
Technical field
The utility model is related to environmental protecting device, particularly a kind of decentralized type sewage processing unit.
Background technology
Due to the missing of sewage disposal pipe network, there is the in line phenomenon of sewage in part old town and rural area, cause part area
Domain quality of water environment constantly deteriorates, and is multiplied with foul smelling and mosquitos and flies, has had a strong impact on resident's daily life, how to have reduced dirt
Water it is in line, be current Xiao Mie smelly water body, protection and lifting quality of water environment in the urgent need to.Therefore, sewage-treatment plant
Improvement the problem of be current urgent need to resolve.
The content of the invention
For above-mentioned situation, to solve the defect of prior art, the purpose of the utility model is just to provide a kind of distributing
Sewage-treatment plant, can effectively solve part old town and rural area and there is the in line phenomenon of sewage, cause subregion water environment
Quality constantly deteriorates, and is multiplied with foul smelling and mosquitos and flies, the problem of having had a strong impact on resident's daily life.
The technical scheme that the utility model is solved is, including modified form anaerobic digester and filtration system, modified form anaerobism
Digester is made up of pond body, closure and center water inlet pipe, and closure is provided with the top of pond body, and center water inlet pipe passes through closure
Pond body bottom is simultaneously stretched into center, and deflection plate is fixed with the water inlet pipe of center, and pond body top is provided with overflow delivery port, and bottom side is set
There is mud discharging mouth, filtration system is divided into two units, and the first filter element, the second filter element bottom are connected, the first filtering is single
From top to bottom provided with the first grit layer, zeolite filler layer in first, water (flow) direction from top to bottom, in the second filter element from bottom to top
Provided with blast furnace slag packing layer, tire debris packing layer, the second grit layer, water (flow) direction from bottom to up, is set on the second filter element
There is discharge outlet.
The utility model reasonable in design, operation maintenance is convenient, the COD that can largely be gone in water removal by anaerobic digestion and
Removal organic polluter can be further removed in BOD, filter process, while the addition intensified denitrification and dephosphorization effect of specific filler, goes out
Water water quality is more secure, is the innovation in sewage disposal system.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
In figure, water inlet pipe centered on 1,2 be closure, and 3 be pond body, and 4 be deflection plate, and 5 be mud discharging mouth, and 6 be collecting methane
Valve, 7 be overflow delivery port, and 8 be the first filter element, and 9 be the second filter element, and 10 be the first grit layer, and 11 be zeolite filler
Layer, 12 be blast furnace slag packing layer, and 13 be tire debris packing layer, and 14 be delivery port, and 15 be the second grit layer.
Embodiment
Embodiment of the present utility model is described in further detail below in conjunction with accompanying drawing.
Provided by Fig. 1, the utility model include modified form anaerobic digester and filtration system, modified form anaerobic digester by
Pond body, closure and center water inlet pipe are constituted, and the top of pond body 3 is provided with closure 2, and center water inlet pipe 1 passes through the center of closure 2
And stretch into deflection plate 4 is fixed with the bottom of pond body 3, center water inlet pipe 1, the top of pond body 3 is provided with overflow delivery port 7, bottom side
Provided with mud discharging mouth 5, filtration system is divided into two units, and the first filter element 8, the bottom of the second filter element 9 are connected, the first mistake
Filter unit 8 in from top to bottom provided with the first grit layer 10, zeolite filler layer 11, water (flow) direction from top to bottom, the second filter element 9
Inside from bottom to top provided with blast furnace slag packing layer 12, tire debris packing layer 13, the second grit layer 15, water (flow) direction from bottom to up,
Second filter element 9 is provided with discharge outlet 14.
Described deflection plate 4 has 3, is equidistantly fixed on center water inlet pipe 1, and the discrepancy in elevation is in 0.3- between the plate of deflection plate 4
Between 0.5m, diameter is suitable with the internal diameter of pond body 3, and deflection plate 4, which is provided with sewage in some perforation, normal course of operation, to be passed through
Perforate and rise on plate, sewage flows downward via perforation on plate during spoil disposal.
Punch position between described deflection plate 4 is differed, it is ensured that current are not straight line in uphill process
Motion, adds the residence time of sewage, while in sewage uphill process, current and the frequent impact of deflection plate 4, sewage mixing effect
It is really good, it is easier to be settled down to bottom after being collided in particulate matter uphill process, not only increases the treatment effect to organic matter,
The suspension content in sewage can also effectively be reduced.
Collecting methane valve 6, external corresponding gas collection cleaning system are housed at the top of described pond body on closure 2.
The described aperture position of overflow delivery port 7 is higher than deflection plate 4, and maintains the discrepancy in elevation between closure 2.
Described the first grit 10 composition of layer are grit, highly in 20-30cm, and zeolite filler 11 composition of layer are boiling
Stone, highly in 70-80cm, the effect of the first grit layer 10 is, can be intercepted by the filtering crop of grit from anaerobic digestion
The suspension that pond comes out, the effect of zeolite filler layer 11 is, ammonia nitrogen that can largely in absorption effluent and adsorbs small part phosphorus,
Improve wet land system Microbial denitrogenation dephosphorization efficiency.
Described the first filter element 8, the bottom of the second filter element 9 are provided with the through hole being connected, through hole and add sieve
Net, to keep current insertion.
The described composition of blast furnace slag packing layer 12 is blast furnace slag, and highly in 40-50cm, the composition of tire debris packing layer 13 is
Tire debris, highly in 30-40cm, the composition of the second sandy gravel stratum 15 is grit, highly in 10-20cm；Blast furnace slag packing layer 12
Effect is, phosphorus that can largely in absorption effluent, improves treatment effeciency of the artificial swamp to phosphorus, tire debris packing layer 13
Effect is, can a large amount of nitrate in absorption effluent, reduce water outlet nitrate content, the effect of the second sandy gravel stratum 15 is to prevent
Only tire debris are lost in.
Described discharge outlet 14 is located at the top of the second filter element 9, highly less than overflow delivery port 7, it is ensured that current exist
It can be discharged under not acted on by external force from discharge outlet.
Service condition of the present utility model is, including modified form anaerobic digester and filtration system two parts, in sewage warp
Heart water inlet pipe 1 enters the bottom of pond body 3 from the closure 2 at the top of modified form anaerobic digester, then slowly rises through deflection plate 4,
Flowed out from the overflow delivery port 7 of the top of pond body 3, the biogas that anaerobic fermentation is produced is collected through the top collecting methane valve 6 of pond body 3, mistake
Filter system is divided into two units, and first module is connected with second unit bottom, and first module filler is grit, zeolite, current
From top to bottom, second unit filler is blast furnace slag, tire debris and grit in direction, water (flow) direction from bottom to up, from modified form
The sewage that anaerobic digester is overflowed, by the water distribution pipe of overflow delivery port even into filtration system, the second filtering is single
First water outlet uses downflow weir mode, and height of weir plate is less than the water distribution pipe of overflow delivery port, when the first filter element water level is high
When the second filter element height of weir plate, the water after processing is flowed out from the discharge outlet 14 of downflow weir, and sludge is passed through through mud discharging mouth 5
Pump periodically extracts pool bottom sludge.
Case study on implementation 1, treating capacity is 10 ton days, BOD of intaking5Average value in 254mg/L, COD average values in 448mg/L,
Total phosphorus is 6mg/L, and ammonia nitrogen is 51mg/L, 25 DEG C of temperature, under the conditions of hydraulic detention time 24h, water outlet BOD5Average removal rate
79.4%, COD average removal rate 86.2%, ammonia nitrogen removal frank 80%, total tp removal rate 70%.
Case study on implementation 2, treating capacity is 10 ton days, BOD of intaking5Average value in 254mg/L, COD average values in 448mg/L,
Total phosphorus is 6mg/L, the micro- 51mg/L of ammonia nitrogen, 15 DEG C of temperature, under the conditions of hydraulic detention time 24h, modified form anaerobic digester water outlet
BOD5Average removal rate 48.2%, COD average removal rates 42.6%, ammonia nitrogen removal frank 50%, total tp removal rate 48%.
Calculated according to water consumption 200L for each person every day, 10 tons of water consumptions equivalent to 50 people, currently without drainage pipeline networks
Old every building of cell at most 2-14 families, an average family 3-4 people calculates, and sum should be 50 or so.
From the foregoing, the utility model can effectively realize the processing to cell domestic water, application of the present utility model
The discharge of water pollutant can be greatly decreased, water environment pollution problem is contained from source, can also be in dirty drainage pipeline networks
Residential area and rural area are used, and sanitary sewage can be effectively treated, and effectively alleviate water environment pressure, simple to operate,
Easy to use, operating cost is low, is the innovation on sewage-treatment plant, with good social and economic benefit.
Claims (8)
1. a kind of decentralized type sewage processing unit, including modified form anaerobic digester and filtration system, it is characterised in that modified form
Anaerobic digester is made up of pond body, closure and center water inlet pipe, and closure (2), center water inlet pipe are provided with the top of pond body (3)
(1) pass through the center of closure (2) and stretch on pond body (3) bottom, center water inlet pipe (1) and be fixed with deflection plate (4), pond body
(3) top is provided with overflow delivery port (7), and bottom side is provided with mud discharging mouth (5), and filtration system is divided into two units, the first filtering
Unit (8), the second filter element (9) bottom are connected, from top to bottom provided with the first grit layer in the first filter element (8)
(10) filled out from bottom to top provided with blast furnace slag packing layer (12), tire debris in, zeolite filler layer (11), the second filter element (9)
The bed of material (13), the second grit layer (15), the second filter element (9) are provided with discharge outlet (14).
2. decentralized type sewage processing unit according to claim 1, it is characterised in that described deflection plate (4) has 3,
Equidistantly it is fixed on center water inlet pipe (1), the discrepancy in elevation is between 0.3-0.5m between deflection plate (4) plate, diameter and pond body (3) internal diameter
Quite, deflection plate (4) is provided with the perforation that some positions are differed.
3. decentralized type sewage processing unit according to claim 1, it is characterised in that closure at the top of described pond body
(2) collecting methane valve (6) is housed on.
4. decentralized type sewage processing unit according to claim 1, it is characterised in that described overflow delivery port (7) is opened
Mouth position is higher than deflection plate (4), and maintains the discrepancy in elevation between closure (2).
5. decentralized type sewage processing unit according to claim 1, it is characterised in that described the first grit layer (10) into
It is divided into grit, highly in 20-30cm, described zeolite filler layer (11) composition is zeolite, highly in 70-80cm.
6. decentralized type sewage processing unit according to claim 1, it is characterised in that described the first filter element (8),
Second filter element (9) bottom is provided with the through hole being connected, through hole and adds screen cloth.
7. decentralized type sewage processing unit according to claim 1, it is characterised in that described blast furnace slag packing layer (12)
Composition is blast furnace slag, highly in 40-50cm, and tire debris packing layer (13) composition is tire debris, highly in 30-40cm, the
Two grit layer (15) composition is grit, highly in 10-20cm.
8. decentralized type sewage processing unit according to claim 1, it is characterised in that described discharge outlet (14) is located at the
The top of two filter elements (9), highly less than overflow delivery port (7).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720334682.9U CN206616122U (en) | 2017-03-31 | 2017-03-31 | A kind of decentralized type sewage processing unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720334682.9U CN206616122U (en) | 2017-03-31 | 2017-03-31 | A kind of decentralized type sewage processing unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206616122U true CN206616122U (en) | 2017-11-07 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720334682.9U Expired - Fee Related CN206616122U (en) | 2017-03-31 | 2017-03-31 | A kind of decentralized type sewage processing unit |
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| Country | Link |
|---|---|
| CN (1) | CN206616122U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110981008A (en) * | 2019-12-06 | 2020-04-10 | 广东水利电力职业技术学院（广东省水利电力技工学校） | Industrial chemicals device is got rid of to high-efficient BOD |
-
2017
- 2017-03-31 CN CN201720334682.9U patent/CN206616122U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110981008A (en) * | 2019-12-06 | 2020-04-10 | 广东水利电力职业技术学院（广东省水利电力技工学校） | Industrial chemicals device is got rid of to high-efficient BOD |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20171107 Termination date: 20200331 |
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| CF01 | Termination of patent right due to non-payment of annual fee |