CN206607128U - A kind of river sewage processing unit based on water treatment agent and ceramic membrane - Google Patents
A kind of river sewage processing unit based on water treatment agent and ceramic membrane Download PDFInfo
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- CN206607128U CN206607128U CN201720295593.8U CN201720295593U CN206607128U CN 206607128 U CN206607128 U CN 206607128U CN 201720295593 U CN201720295593 U CN 201720295593U CN 206607128 U CN206607128 U CN 206607128U
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 66
- 239000000919 ceramic Substances 0.000 title claims abstract description 49
- 239000012528 membrane Substances 0.000 title claims abstract description 40
- 239000010865 sewage Substances 0.000 title claims abstract description 36
- 239000003795 chemical substances by application Substances 0.000 title claims abstract description 29
- 238000005374 membrane filtration Methods 0.000 claims abstract description 37
- 239000010802 sludge Substances 0.000 claims abstract description 21
- 239000003814 drug Substances 0.000 claims abstract description 19
- 238000002156 mixing Methods 0.000 claims abstract description 19
- 238000001914 filtration Methods 0.000 claims abstract description 13
- 238000005273 aeration Methods 0.000 claims description 14
- 239000004576 sand Substances 0.000 claims description 3
- 239000000725 suspension Substances 0.000 claims description 3
- 239000000463 material Substances 0.000 claims 1
- 230000000694 effects Effects 0.000 abstract description 9
- 239000003337 fertilizer Substances 0.000 abstract description 4
- 239000007789 gas Substances 0.000 description 12
- 238000000034 method Methods 0.000 description 8
- 239000001301 oxygen Substances 0.000 description 5
- 229910052760 oxygen Inorganic materials 0.000 description 5
- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 5
- 239000000969 carrier Substances 0.000 description 4
- 238000004140 cleaning Methods 0.000 description 4
- 238000011109 contamination Methods 0.000 description 4
- 244000005700 microbiome Species 0.000 description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 4
- 241000894006 Bacteria Species 0.000 description 3
- 230000036740 Metabolism Effects 0.000 description 3
- 241000700605 Viruses Species 0.000 description 3
- 239000002253 acid Substances 0.000 description 3
- 238000005276 aerator Methods 0.000 description 3
- 229910001385 heavy metal Inorganic materials 0.000 description 3
- 230000004060 metabolic process Effects 0.000 description 3
- 230000035786 metabolism Effects 0.000 description 3
- 239000011148 porous material Substances 0.000 description 3
- 230000035621 Permeability Rate Effects 0.000 description 2
- 241000589651 Zoogloea Species 0.000 description 2
- 230000001580 bacterial Effects 0.000 description 2
- 238000005842 biochemical reaction Methods 0.000 description 2
- 230000001488 breeding Effects 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 229940079593 drugs Drugs 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000000284 extract Substances 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 238000005189 flocculation Methods 0.000 description 2
- 230000016615 flocculation Effects 0.000 description 2
- 238000011068 load Methods 0.000 description 2
- 230000000813 microbial Effects 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 238000010926 purge Methods 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 239000000377 silicon dioxide Substances 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 230000037250 Clearance Effects 0.000 description 1
- 241000233866 Fungi Species 0.000 description 1
- 241000276438 Gadus morhua Species 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 238000006065 biodegradation reaction Methods 0.000 description 1
- 229960000074 biopharmaceuticals Drugs 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000004061 bleaching Methods 0.000 description 1
- 230000035512 clearance Effects 0.000 description 1
- 230000001112 coagulant Effects 0.000 description 1
- 235000019516 cod Nutrition 0.000 description 1
- 230000000875 corresponding Effects 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 230000035558 fertility Effects 0.000 description 1
- 238000005755 formation reaction Methods 0.000 description 1
- 239000012510 hollow fiber Substances 0.000 description 1
- 229910052738 indium Inorganic materials 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- -1 nitrogen phosphorus Chemical compound 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 229920000620 organic polymer Polymers 0.000 description 1
- 230000000737 periodic Effects 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 238000007781 pre-processing Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000008213 purified water Substances 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 230000000717 retained Effects 0.000 description 1
- 238000007790 scraping Methods 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
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- 238000003756 stirring Methods 0.000 description 1
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Abstract
The utility model is related to the river sewage processing unit based on water treatment agent and ceramic membrane, mainly include pretreatment system, medicine system, film filtering system, canyon, medicine system has water inlet, dosing mouth and mixing chamber, air accumulator, air compressor machine are disposed with canyon, film filtering system has setting ceramic membrane in membrane filtration pond, membrane filtration pond, ceramic membrane bottom connects outlet pipe, water pump is set on outlet pipe pipeline, and membrane filtration bottom of pond portion sets and sets sludge pump on discharge pipeline, discharge pipeline pipeline；Air accumulator connects mixing chamber by tracheae, mixing chamber connects membrane filtration pond by water pipe, the sewage and water treatment agent come out from setting pot is added to mixing chamber, membrane filtration pond is passed through by pipeline after well mixed, sewage is fully handled by water treatment agent, water after being purified in ceramic membrane flows into outlet pipe, and discharge or reuse are extracted out by water pump after collecting.The utility model occupation area of equipment is small, with applied widely, high treating effect, and the sludge that system is produced may be used as farmland fertilizer, environmental protection.
Description
Technical field
The utility model belongs to technical field of sewage treatment equipment, specifically a kind of river sewage processing unit.
Background technology
While industrial boom and people's living standard continuous improvement, serious pollution problem is also brought.River course
As main discharge channel, all kinds of sanitary sewages, industrial wastewater from periphery etc. are receive, pollution problem is increasingly serious.
Now, the pollution control and restoration of the ecosystem in river course have been valued by people.
At present, the sewage treatmentmethod of Drain contamination for river channel mouthful mainly has the engineerings such as desilting, section dirt, aeration, dispensing, biochemistry to arrange
Apply, but be due to cut dirty measure imperfection or cut dirty not thorough, sewage has not just been discharged into river course by effectively processing.Some
Engineering uses direct dosing mode, and not only regulation effect is poor for this mode, and medicament and sludge settling to bottom of river channel, medicament sheet
The heavy metal or organic polymer and the polluter of adsorption precipitation that body contains produce secondary pollution to river bed.General exposure
The technique such as gas, biological prosthetic is applied to Landscape River or the not high waters of pollution level, and treatment effect is also unsatisfactory.Therefore,
Sewage is effectively retained and handled on the spot in Drain contamination for river channel mouth, is the key of river regulation.Green technology is constantly sent out in recent years
Exhibition, various to be developed in succession suitable for the dirty sewage disposal device administered of Drain contamination for river channel mouthful section, these processing equipments are adopted mostly
With modes such as traditional dosing coagulating sedimentation, processing unit structure is various, and floor space is big, and cost of investment is high, and operating cost is high,
Treatment effect is general.
Invention technician devises integrated river sewage processing unit, based on nano biological circulating water treatment agent and
Ceramic membrane filter system, can effectively solve problem above.
Utility model content
The utility model is provided in view of the above-mentioned problems, having invented a kind of integrated river sewage processing unit, and the device is
Based on nano biological circulating water treatment agent+ceramic membrane filter system, floor space is small, operating cost is low, and effluent characteristics are high.
The technical scheme in the invention for solving the above technical problem is：A kind of river based on water treatment agent and ceramic membrane
Road sewage-treatment plant, it is characterised in that：Mainly include pretreatment system, medicine system, film filtering system, canyon, it is described pre-
Processing system includes grid pond and setting pot, and bulky grain suspension and silt in river are removed respectively；The medicine system tool
There are water inlet, dosing mouth and mixing chamber, water inlet is connected with settling pit pipeline；Air accumulator, pneumatics are disposed with the canyon
Machine, the film filtering system has setting ceramic membrane in membrane filtration pond, membrane filtration pond, ceramic membrane bottom connection outlet pipe, outlet pipe pipeline
Upper setting water pump, membrane filtration bottom of pond portion sets and sets sludge pump on discharge pipeline, discharge pipeline pipeline；Air accumulator is connected by tracheae and mixed
Room, mixing chamber connects membrane filtration pond by water pipe, sequentially passes through sewage and water treatment agent after grid pond and settling pit processing and adds
To mixing chamber, it is well mixed, is then passed through by pipeline in membrane filtration pond under being sufficiently stirred for of pressure air-dissolving, it is dirty in membrane filtration pond
Water is fully handled by water treatment agent, is flowed into while ceramic membrane stops the water after being purified in activated sludge and polluter, ceramic membrane
Outlet pipe, discharge or reuse are extracted out after collecting by water pump.
Air accumulator extends gas distribution pipe, and membrane filtration pond bottom of pond sets ceramic aeration tube, and ceramic aeration tube is docked with gas distribution pipe, entered
Row fully aeration, can improve the breeding and metabolism of microorganism, gas is inputted by gas distribution pipe.
Ceramic film component needs fixed time cleaning, and gas-adding pipe is provided between the outlet pipe and air accumulator, from gas-adding pipe to going out
Input forced air, is recoiled by ceramic membrane bottom up in water pipe, and gas is carried out to membrane from inside to outside after being passed through in film
Recoil.
Present apparatus processing river sewage is based primarily upon LS nano biologicals circulating water treatment agent medicine system and film filtering system
United application.
（1）Medicine system
LS nano biological circulating water treatment agent is a new green environment protection water treatment agent of company's research and development, and the product is used
Pure natural formula non-secondary pollution, is different from the ferro-aluminum type medicament and polymerized organics medicament of in the market, can efficiently remove waste water
In all kinds of polluters such as COD, nitrogen phosphorus, heavy metal, and with good adsorption bleaching characteristic.
LS nano biological circulating water treatment agent is added into after medicine system, filled in the presence of pressure air-dissolving with sewage
Divide stirring mixing, the nanoporous structure of water treatment agent makes it have huge specific surface area, countless nanometers are formed in water body
Level bio-carrier, microorganism breed on carrier and forms bacterium ball, while the zoogloea that water treatment agent is formed have powerful flocculation,
Absorption property, surface is enriched to by polluter, polluter is degraded by the metabolism of microorganism.
LS nano biological circulating water treatment agent has the characteristics that and performance：
A. green product non-secondary pollution, reusable edible, energy-saving
B. there is significant Nitrogen/Phosphorus Removal
C. biochemical clearance 20%-30% is lifted
D. bio-carrier is formed, strengthens zoogloea
E. suppress der Pilz, effectively control sludge bulking
F. mud decrement 5%-20% is realized, and sludge dewatering need not add medicament
（2）Film filtering system
Film filtering system organically combines to handle sewage by membrane separation technique with biologic treating technique, in membrane filtration
High activity sludge concentration is kept in pond, biological treatment organic loading is improved, so as to reduce sewage treatment facility floor space, and leads to
Cross and keep low sludge loading to reduce surplus sludge volume.The activated sludge being immersed in the ceramic membrane interception pond in membrane filtration pond divides with big
Sub- organic matter, can extend the growth cycle of microorganism, realize the deep purifying of sewage, and Simultaneous Nitrification bacterium can be fully numerous in system
Grow, with significant nitrification effect, realize advanced nitrogen dephosphorization.
The processing unit of film filtering system most critical is the ceramic membrane and ceramic aeration tube being placed in membrane filtration pond.
Traditional membrane filtration is generally adopted by hollow fiber filter membrane, and this technique uses ceramic super-filtering film, aperture 0.001-
0.05 μm, formed by ceramic post sintering.In running, raw water is on the outside of film in membranous system, and purified water is walked on the inside of film, while built-in
Air pressure backwash technique, by air-flow, to film, back-pressure is washed from inside to outside, can effectively clean membrane, it is ensured that treatment effeciency.Ceramic membrane
Have the characteristics that and performance：
A. all kinds of polluters and bacterial virus are efficiently removed, recycling sewage generated by making can be achieved
B. coordinate micro-pore aeration, MLSS concentration can be improved, improve Microbial denitrogenation dephosphorization efficiency
C. acid and alkali-resistance, high temperature high voltage resistant, extrude water certainly, and energy-saving, cost is less than tunica fibrosa
D. air-flow back purge system is used, permeability rate more than 85% is ensured
E. possess all technological merits of MBR films, be the upgrading substitute of tunica fibrosa
In film filtering system system is efficiently aerated for the MLSS of maintenance high concentration, it is necessary to coordinate to improve biochemical treatment efficiency
System, this technique has the ultra-fine stomata of 0.001-0.05 μm of diameter using ceramic aeration tube, this aerator, and gas passes through ceramics
Guan Shihui produces 50-90 μm of fine gas bubbles, and the bubble slowly risen effectively improves the utilization rate of dissolved oxygen concentration and oxygen.Ceramics
Aeration tube improves the short shortcoming of low traditional aerator oxygen conversion rate, high energy consumption, service life.
The corresponding waste water processes of the present apparatus are as follows
Drain contamination for river channel mouthful sewage introduces present treatment device, and sewage is removed by grid pond, setting pot twice pretreatment process
In bulky grain suspension and silt, then by medicine system water inlet pipeline enter medicine system mixing chamber, while LS
Nano biological circulating water treatment agent enters the mixing chamber of medicine system from dosing mouth, and providing gas-pressurized by air compressor machine is stored in
In gas tank, mixing chamber is entered by tracheae, sewage and LS nano biological circulating water treatment agent under being sufficiently stirred for of pressure air-dissolving
It is sufficiently mixed, is then passed through by pipeline in membrane filtration pond, the water treatment agent being blended in water is covered with rapidly membrane filtration pond, and is formed
Countless nano level biofilm carriers, pollutant is adsorbed, biodegradable, flocculation, the effect such as precipitation, while ceramic membrane hinders
Cut activated sludge and polluter, continuation polluter is effectively degraded, and effectively filter SS, bacterium, virus and
All kinds of polluters.Coordinate membrane filtration system sewage to obtain the water after being purified in deep purifying, film by biochemical reaction and flow into film
The outlet pipe of part bottom extracts discharge or reuse out after collecting by water pump.
Ceramic film component needs fixed time cleaning, and forced air is passed through by tracheae, is recoiled by bottom up, and gas is passed through film
Membrane is recoiled from inside to outside after interior.Ceramic pipe type aeration tube is configured in membrane filtration pond to be fully aerated, and can improve micro- life
The breeding and metabolism of thing, air are inputted by tracheae.Membrane filtration pond needs periodically to discharge minimal amount of aging sludge, in membrane filtration bottom of pond portion
Surrounding cloth one encloses discharge pipeline, periodically extracts mud discharging by sludge pump, as a result of LS nano biological circulating water treatment agent,
This water treatment agent belongs to green product non-secondary pollution, and the sludge of generation does not have the polluters such as heavy metal, polymer not only,
And with good fertility, can be used for farmland as fertilizer.Membrane filtration water face may produce a small amount of scum silica frost, by scraping slag
Scum silica frost is scraped and periodically cleared up after ash pit by machine.
Using ceramic membrane filter system, with advantages below：
（1）All kinds of polluters and bacterial virus are efficiently removed, recycling sewage generated by making can be achieved；
（2）Coordinate micro-pore aeration, MLSS concentration can be improved, improve Microbial denitrogenation dephosphorization efficiency；
（3）Acid and alkali-resistance, high temperature high voltage resistant, energy-saving from water is extruded, cost is less than tunica fibrosa；
（4）Using air-flow back purge system, permeability rate more than 85% is ensured；
（5）Possess all technological merits of MBR films, be the upgrading substitute of tunica fibrosa.
Ceramic pipe type aerator is used, with advantages below：
（1）Dissolved oxygen concentration is effectively improved, promotes biochemical reaction；
（2）Oxygen conversion rate is high, and pore opening is uniform and stable, energy-saving；
（3）Acid and alkali-resistance, high pressure resistant, service life is long.
The river sewage processing unit floor space of the application is small, with applied widely, high treating effect, and dirt can be achieved
Water reuse (treatment reuse, the sludge that system is produced may be used as farmland fertilizer, environmental protection.
Brief description of the drawings
Fig. 1 is the structural representation of river sewage processing unit in the utility model embodiment.
Embodiment
The utility model is described in further detail below in conjunction with accompanying drawing embodiment.
As shown in figure 1, the river sewage processing unit in the present embodiment, mainly including pretreatment system, medicine system, film
Filter system, canyon.Pretreatment system includes grid pond 12 and setting pot 13, and grid pond 12 is tilted to be provided with grid, sand setting
The bottom in pond 13 has sand removing hole.Medicine system has water inlet pipe 1, dosing mouth 2 and mixing chamber, and water inlet pipe 1 connects setting pot 13,
Air accumulator 3, the film filtering system of air compressor machine 4. are disposed with canyon has setting ceramic membrane 6, ceramic membrane in membrane filtration pond 5, membrane filtration pond 5
6 bottoms are connected and water pump 8 are set on outlet pipe 7, the pipeline of outlet pipe 7, and the bottom of membrane filtration pond 5 is set on discharge pipeline 9, the pipeline of discharge pipeline 9
Sludge pump 10 is set, and membrane filtration pond bottom of pond sets ceramic aeration tube 11, and air accumulator 3 extends gas distribution pipe, ceramic aeration tube 11 and cloth
Tracheae is docked.Air accumulator 3 connects mixing chamber by tracheae, and mixing chamber connects membrane filtration pond, the dirt come out from setting pot by water pipe
Water and water treatment agent are added to mixing chamber, are well mixed under being sufficiently stirred for of pressure air-dissolving, are then passed through membrane filtration pond by pipeline
In, in membrane filtration pond, sewage is fully handled by water treatment agent, while ceramic membrane stops activated sludge and polluter, ceramic membrane
Water after interior purification flows into outlet pipe, and discharge or reuse are extracted out by water pump after collecting.
Ceramic membrane needs periodic cleaning, and gas-adding pipe is provided between outlet pipe 7 and air accumulator 3, from gas-adding pipe to outlet pipe 7
Interior input forced air, is recoiled by ceramic membrane bottom up, and gas recoils to membrane from inside to outside after being passed through in film.
The river sewage processing unit of said structure has applied widely, high treating effect, and regeneration effluent can be achieved and returns
With the sludge that system is produced may be used as farmland fertilizer, environmental protection.
In addition to the implementation, the utility model also includes other embodiment, all use equivalents or equivalent
The technical scheme of substitute mode formation, all should fall within the utility model scope of the claims.
Claims (3)
1. a kind of river sewage processing unit based on water treatment agent and ceramic membrane, it is characterised in that：It is main to include pretreatment system
System, medicine system, film filtering system, canyon, the pretreatment system include grid pond and setting pot, remove respectively in river
Bulky grain suspension and silt；The medicine system has water inlet pipe, dosing mouth and mixing chamber, and water inlet pipe connects with settling pit pipeline
Connect；Air accumulator, air compressor machine are disposed with the canyon, the film filtering system has setting ceramic membrane in membrane filtration pond, membrane filtration pond,
Ceramic membrane bottom connects and water pump is set on outlet pipe, outlet pipe pipeline, and membrane filtration bottom of pond portion sets and set on discharge pipeline, discharge pipeline pipeline
Put sludge pump；Air accumulator connects mixing chamber by tracheae, and mixing chamber connects membrane filtration pond by water pipe, sequentially passes through grid pond and heavy
Sewage and water treatment agent after sand basin processing are added to mixing chamber, are well mixed under being sufficiently stirred for of pressure air-dissolving, Ran Houyou
Pipeline is passed through in membrane filtration pond, and in membrane filtration pond, sewage is fully handled by water treatment agent, while ceramic membrane stops activated sludge and dirt
Contaminate the water after being purified in material, ceramic membrane and flow into outlet pipe, discharge or reuse are extracted out by water pump after collecting.
2. the river sewage processing unit according to claim 1 based on water treatment agent and ceramic membrane, it is characterised in that：Institute
State air accumulator and extend gas distribution pipe, membrane filtration pond bottom of pond sets ceramic aeration tube, and ceramic aeration tube is docked with gas distribution pipe.
3. the river sewage processing unit according to claim 1 based on water treatment agent and ceramic membrane, it is characterised in that：Institute
State and gas-adding pipe is provided between outlet pipe and air accumulator, forced air is inputted into outlet pipe from gas-adding pipe, by ceramic membrane bottom
Recoiled upwards, gas recoils to membrane from inside to outside after being passed through in film.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720295593.8U CN206607128U (en) | 2017-03-24 | 2017-03-24 | A kind of river sewage processing unit based on water treatment agent and ceramic membrane |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720295593.8U CN206607128U (en) | 2017-03-24 | 2017-03-24 | A kind of river sewage processing unit based on water treatment agent and ceramic membrane |
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| Publication Number | Publication Date |
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| CN206607128U true CN206607128U (en) | 2017-11-03 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110078175A (en) * | 2019-05-22 | 2019-08-02 | 江苏南大环保科技有限公司 | A kind of ultrafiltration and air-floating integral unit and application |
-
2017
- 2017-03-24 CN CN201720295593.8U patent/CN206607128U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110078175A (en) * | 2019-05-22 | 2019-08-02 | 江苏南大环保科技有限公司 | A kind of ultrafiltration and air-floating integral unit and application |
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