CN207391215U - A kind of microkinetic integrated sewage treating apparatus - Google Patents
A kind of microkinetic integrated sewage treating apparatus Download PDFInfo
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- CN207391215U CN207391215U CN201721303323.3U CN201721303323U CN207391215U CN 207391215 U CN207391215 U CN 207391215U CN 201721303323 U CN201721303323 U CN 201721303323U CN 207391215 U CN207391215 U CN 207391215U
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- dephosphorization
- mbr membrane
- treating apparatus
- filtering
- mbr
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Abstract
The utility model discloses a kind of microkinetic integrated sewage treating apparatus, for technical field of sewage, including biochemical reaction unit, MBR unit and dephosphorization filter element, the MBR unit includes MBR membrane cisternas, the MBR membrane modules being located in MBR membrane cisternas and the production aquaporin being connected with the MBR membrane modules, the dephosphorization filter element includes dephosphorization filtering ponds and the slag filter packing layer being located in the dephosphorization filtering ponds, dephosphorization filtering ponds are divided into filtering proparea and filtering back zone by slag filter packing layer, the production aquaporin is connected with the filtering proparea, the dephosphorization filtering ponds are equipped with the outlet pipe communicated with filtering back zone.The utility model technology is combined using MBR unit and dephosphorization filter element, with the efficient carbon nitrogen phosphor-removing effect of effect, SS and turbidity in water are close to zero, it can be directly as recycle-water, remaining organic sludge amount is few, and floor space is small, can form modularization, management is simplified, it can be achieved that automatically controlling and remote control.
Description
Technical field
The utility model is used for technical field of sewage, is set more particularly to a kind of microkinetic integrated sewage disposal
It is standby.
Background technology
Traditional sewage disposal technology capital construction is high with operating cost, and nitrogen phosphorus ligands efficiency is low, and it is rich can not to solve such as water body
The environmental problems such as nutrient laden.Therefore, it is new to seek low cost, high efficiency, new domestic sewage of villages and small towns microkinetic advanced nitrogen dephosphorization
Method is always the hot spot of China's water treatment field concern.
The technology of existing biological carbon and phosphorous removal is although each advantageous, but is not also generally very ripe, and many sewage are only
It only relies on a kind of technology and is extremely difficult to target, it is necessary to which several technologies are used in combination, such as synchronous nitration and denitrification and life
Object-ecology process integration.Synchronous nitration and denitrification, oxygen demand substantially reduces, the reaction time is short, reaction efficiency is high, energy consumption
Low, efficient characteristic determines that it can become an important directions of future biological denitrogenation technology development.And biology-ecology
Integrated technique because it can realize mutual supplement with each other's advantages, and also can more meet energy-saving and emission-reduction run under the conditions of microkinetic the advantages that
It is required that.Therefore, the new method that exploiting economy is efficient, advanced nitrogen dephosphorization is run, is capable of to microkinetic has wide in villages and small towns area
The market demand and society need.
Utility model content
The purpose of this utility model is to provide a kind of preferable microkinetic integrated sewage treating apparatus of effect.
Technical solution is used by the utility model solves its technical problem：A kind of microkinetic integrated sewage disposal is set
Standby, including biochemical reaction unit, MBR unit and dephosphorization filter element, the MBR unit includes MBR membrane cisternas, is located at MBR membrane cisternas
In MBR membrane modules and the production aquaporin that is connected with the MBR membrane modules, the dephosphorization filter element include dephosphorization filtering ponds
With the slag filter packing layer being located in the dephosphorization filtering ponds, before dephosphorization filtering ponds are divided into filtering by slag filter packing layer
Area and filtering back zone, the production aquaporin are connected with the filtering proparea, and the dephosphorization filtering ponds are equipped with filtering back zone phase
Logical outlet pipe.
The improvement of technical solutions of the utility model is further used as, further includes air blower, the MBR membrane cisternas are interior in MBR films
The lower section of component is equipped with the first aerator being connected with the air blower.
The improvement of technical solutions of the utility model is further used as, the biochemical reaction unit includes being located on MBR membrane cisternas
The aerobic tank of trip is communicated between aerobic tank and MBR membrane cisternas by the first water passage, is equipped with and the air blast in the aerobic tank
The second aerator that machine is connected.
The improvement of technical solutions of the utility model is further used as, the biochemical reaction unit, which further includes, to be located on aerobic tank
The anoxic pond of trip and the anaerobic pond for being located at anoxic pond upstream, anaerobic pond are equipped with water inlet pipe, and the aerobic tank and anoxic pond pass through
Second water passage communicates, and the anaerobic pond and anoxic pond are communicated by the 3rd water passage.
The improvement of technical solutions of the utility model is further used as, floating stuffing is equipped in the anoxic pond and aerobic tank.
The improvement of technical solutions of the utility model is further used as, first water passage communicates and the second water passage
Place is equipped with filter.
The improvement of technical solutions of the utility model is further used as, impeller is equipped in the anoxic pond.
The improvement of technical solutions of the utility model is further used as, is filled out on the upside of slag filter packing layer equipped with quartz sand filtration
The bed of material.
The improvement of technical solutions of the utility model is further used as, is filtered on the dephosphorization filtering ponds in the correspondence slag
Discharge port is equipped at the position of packing layer and quartz sand filtration packing layer.
The beneficial effects of the utility model：The utility model technology substitutes traditional sedimentation basin using MBR films, and treated goes out
Water water quality is good, and SS and turbidity in water outlet possesses removal virus and bacterium close to zero, and water outlet is directly as reuse
Water, it is easy to accomplish the recycling of sewage.
The utility model technology, as efficient filter tank filler constituent, makes full use of it good using discarded object-slag
Absorption property and the characteristic that derives from a wealth of sources, reinforced phosphor-removing effect there is low cost, effect is good, realizes that " treatment of wastes with processes of wastes against one another becomes useless
For treasured ".
The utility model technology is combined using MBR unit and dephosphorization filter element, is had and is imitated efficient carbon nitrogen dephosphorization effect
Fruit, SS and turbidity in water, can be directly as recycle-waters close to zero, and remaining organic sludge amount is few, and floor space is small, can form mould
Block, management are simplified, it can be achieved that automatically controlling and remote control.
Description of the drawings
The utility model is described in further detail below in conjunction with the accompanying drawings：
Fig. 1 is the utility model embodiment structure diagram.
Specific embodiment
With reference to Fig. 1, that show the concrete structures of the preferred embodiment of the utility model.It will be detailed below this reality
It is with shown in FIG. 1 with the design feature of new each component, and during if there is being described to direction (upper and lower, left and right, before and after)
Structure is that reference describes, but the actual use direction of the utility model is not limited thereto.
The utility model provides a kind of microkinetic integrated sewage treating apparatus, including biochemical reaction unit, MBR unit
1 and dephosphorization filter element 2, the MBR unit 1 include MBR membrane cisternas 11, the MBR membrane modules 12 being located in MBR membrane cisternas 11 and with
The production aquaporin that the MBR membrane modules 12 connect, production aquaporin include water producing pipe 13 and the production water pump 14 being located on water producing pipe 13,
The dephosphorization filter element 2 includes dephosphorization filtering ponds 21 and the slag filter packing layer 22 being located in the dephosphorization filtering ponds 21,
Dephosphorization filtering ponds are divided into filtering proparea 23 and filtering back zone 24, the production aquaporin and the mistake by slag filter packing layer 22
It filters proparea 23 to be connected, the dephosphorization filtering ponds 21 are equipped with the outlet pipe 25 communicated with filtering back zone 24.During work, sewage is successively
By biochemical reaction unit biochemical treatment, after MBR unit 1 and the processing of dephosphorization filter element 2, discharged by outlet pipe.
The utility model technology substitutes traditional sedimentation basin using MBR films, and treated, and effluent quality is good, the SS in water outlet
With turbidity close to zero, and possess removal virus and bacterium, water outlet is directly as recycle-water, it is easy to accomplish the recycling of sewage
It utilizes.
The utility model technology, as efficient filter tank filler constituent, makes full use of it good using discarded object-slag
Absorption property and the characteristic that derives from a wealth of sources, reinforced phosphor-removing effect there is low cost, effect is good, realizes that " treatment of wastes with processes of wastes against one another becomes useless
For treasured ".
The utility model technology is combined using MBR unit 1 and dephosphorization filter element 2, is had and is imitated efficient carbon nitrogen dephosphorization
Effect, SS and turbidity in water, can be directly as recycle-waters close to zero, and remaining organic sludge amount is few, and floor space is small, can be formed
Modularization, management are simplified, it can be achieved that automatically controlling and remote control.
Air blower 3 is further included, is equipped in the lower section of MBR membrane modules 12 in the MBR membrane cisternas 11 and is connected with the air blower 3
The first aerator 31.By the castering action of aeration and current floating stuffing is made to be in fluidized state, and then formed and suspended
The activated sludge of growth and the biomembrane of apposition growth.High with volumetric loading, effective ratio area is big, strong shock resistance,
Sludge age is long, and surplus sludge volume is few, does not generate sludge bulking, organics removal and good denitrogenation and dephosphorization effect.
The biochemical reaction unit includes being located at the aerobic tank 41 of 11 upstream of MBR membrane cisternas, aerobic tank 41 and MBR membrane cisternas 11 it
Between communicated by the first water passage 42, the second aerator 32 being connected with the air blower 3 is equipped in the aerobic tank 41.
The biochemical reaction unit further includes the anoxic pond 43 for being located at 41 upstream of aerobic tank and the anaerobic pond 44 for being located at 43 upstream of anoxic pond,
Anaerobic pond 44 is equipped with water inlet pipe 45, and the aerobic tank 41 and anoxic pond 43 are communicated by the second water passage 46, the anaerobism
Pond 44 and anoxic pond 43 are communicated by the 3rd water passage 47.Sewage passes through anaerobic pond 44, anoxic pond 43 and aerobic tank 41 successively,
Enter MBR membrane cisternas 11 after carrying out anaerobic reaction, hypoxia response and aerobic reaction.
In order to improve reaction efficiency, floating stuffing 48 is equipped in the anoxic pond 43 and aerobic tank 41.
In order to avoid floating stuffing 48 drifts about backward with current, first water passage 42 communicates and the second water passage
Filter 40 is equipped at 46.Impeller 49 is equipped in the anoxic pond 43.
In addition, 22 upside of slag filter packing layer is equipped with quartz sand filtration packing layer 26.On the dephosphorization filtering ponds 21
Discharge port 27 is equipped at the position of the corresponding slag filter packing layer 22 and quartz sand filtration packing layer 26, for periodically clear
Manage filter packing.
Certainly, the invention is not limited to the above embodiment, and those skilled in the art are without prejudice to originally
Equivalent variations or replacement can be also made on the premise of utility model spirit, these equivalent modifications or replacement are all contained in the application
In claim limited range.
Claims (9)
1. a kind of microkinetic integrated sewage treating apparatus, it is characterised in that：Including biochemical reaction unit, MBR unit and dephosphorization
Filter element, the MBR unit include MBR membrane cisternas, the MBR membrane modules being located in MBR membrane cisternas and connect with the MBR membrane modules
The production aquaporin connect, the dephosphorization filter element includes dephosphorization filtering ponds and the slag being located in dephosphorization filtering ponds filtering is filled out
Dephosphorization filtering ponds are divided into filtering proparea and filtering back zone, the production aquaporin and the mistake by the bed of material, slag filter packing layer
Filter proparea is connected, and the dephosphorization filtering ponds are equipped with the outlet pipe communicated with filtering back zone.
2. microkinetic integrated sewage treating apparatus according to claim 1, it is characterised in that：Air blower is further included, institute
State the first aerator for being equipped in the lower section of MBR membrane modules in MBR membrane cisternas and being connected with the air blower.
3. microkinetic integrated sewage treating apparatus according to claim 2, it is characterised in that：The biochemical reaction unit
Aerobic tank including being located at MBR membrane cisternas upstream, is communicated between aerobic tank and MBR membrane cisternas by the first water passage, described aerobic
The second aerator being connected with the air blower is equipped in pond.
4. microkinetic integrated sewage treating apparatus according to claim 3, it is characterised in that：The biochemical reaction unit
The anoxic pond for being located at aerobic tank upstream and the anaerobic pond for being located at anoxic pond upstream are further included, anaerobic pond is equipped with water inlet pipe, described
Aerobic tank and anoxic pond are communicated by the second water passage, and the anaerobic pond and anoxic pond are communicated by the 3rd water passage.
5. microkinetic integrated sewage treating apparatus according to claim 4, it is characterised in that：The anoxic pond and aerobic
Floating stuffing is equipped in pond.
6. microkinetic integrated sewage treating apparatus according to claim 5, it is characterised in that：First water passage
It communicates and is equipped with filter at the second water passage.
7. microkinetic integrated sewage treating apparatus according to claim 4, it is characterised in that：It is equipped in the anoxic pond
Impeller.
8. microkinetic integrated sewage treating apparatus according to claim 1, it is characterised in that：On slag filter packing layer
Side is equipped with quartz sand filtration packing layer.
9. microkinetic integrated sewage treating apparatus according to claim 8, it is characterised in that：On the dephosphorization filtering ponds
Discharge port is equipped at the position of the correspondence slag filter packing layer and quartz sand filtration packing layer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721303323.3U CN207391215U (en) | 2017-10-10 | 2017-10-10 | A kind of microkinetic integrated sewage treating apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721303323.3U CN207391215U (en) | 2017-10-10 | 2017-10-10 | A kind of microkinetic integrated sewage treating apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207391215U true CN207391215U (en) | 2018-05-22 |
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ID=62331840
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721303323.3U Active CN207391215U (en) | 2017-10-10 | 2017-10-10 | A kind of microkinetic integrated sewage treating apparatus |
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| Country | Link |
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| CN (1) | CN207391215U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109133514A (en) * | 2018-09-13 | 2019-01-04 | 东华理工大学 | A kind of underground water pollution processing unit |
-
2017
- 2017-10-10 CN CN201721303323.3U patent/CN207391215U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109133514A (en) * | 2018-09-13 | 2019-01-04 | 东华理工大学 | A kind of underground water pollution processing unit |
| CN109133514B (en) * | 2018-09-13 | 2021-07-02 | 东华理工大学 | Groundwater pollution treatment device |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address |
Address after: Room 604, building 25, Tian'an headquarters center, 555 Panyu Avenue North, Donghuan street, Panyu District, Guangzhou, Guangdong 511400 Patentee after: Guangdong Bofang Environmental Protection Technology Group Co.,Ltd. Address before: 511400 No. 919-1, Tian'an Science and Technology Development Building, Panyu Energy Saving Science and Technology Park, No. 555, Panyu Avenue, Panyu District, Guangzhou, Guangdong Patentee before: GUANGZHOU BOFANG ENVIRONMENTAL PROTECTION TECHNOLOGY CO.,LTD. |
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| CP03 | Change of name, title or address |