CN208532384U - A kind of multistage multistage integrated sewage processor - Google Patents
A kind of multistage multistage integrated sewage processor Download PDFInfo
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- CN208532384U CN208532384U CN201820614123.8U CN201820614123U CN208532384U CN 208532384 U CN208532384 U CN 208532384U CN 201820614123 U CN201820614123 U CN 201820614123U CN 208532384 U CN208532384 U CN 208532384U
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- multistage
- zone
- integrated sewage
- sewage processor
- cabinet
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- 239000010865 sewage Substances 0.000 title claims abstract description 40
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 37
- 238000001914 filtration Methods 0.000 claims abstract description 22
- 239000010802 sludge Substances 0.000 claims abstract description 12
- 238000012856 packing Methods 0.000 claims abstract description 9
- 238000005192 partition Methods 0.000 claims abstract description 8
- 238000005273 aeration Methods 0.000 claims description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 5
- 229910052760 oxygen Inorganic materials 0.000 claims description 5
- 239000001301 oxygen Substances 0.000 claims description 5
- 230000005484 gravity Effects 0.000 claims description 4
- 230000013011 mating Effects 0.000 claims description 4
- 238000011001 backwashing Methods 0.000 claims description 3
- 239000004698 Polyethylene Substances 0.000 claims description 2
- 238000001816 cooling Methods 0.000 claims description 2
- 238000013461 design Methods 0.000 claims description 2
- 239000000945 filler Substances 0.000 claims description 2
- 239000000463 material Substances 0.000 claims description 2
- 238000012544 monitoring process Methods 0.000 claims description 2
- -1 polyethylene Polymers 0.000 claims description 2
- 229920000573 polyethylene Polymers 0.000 claims description 2
- 238000011010 flushing procedure Methods 0.000 claims 1
- 238000005086 pumping Methods 0.000 claims 1
- 239000000725 suspension Substances 0.000 claims 1
- 238000012423 maintenance Methods 0.000 abstract description 4
- 230000000694 effects Effects 0.000 description 6
- 238000010992 reflux Methods 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 230000010354 integration Effects 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- 241000196324 Embryophyta Species 0.000 description 2
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 229910052698 phosphorus Inorganic materials 0.000 description 2
- 239000011574 phosphorus Substances 0.000 description 2
- 229910000975 Carbon steel Inorganic materials 0.000 description 1
- 235000006508 Nelumbo nucifera Nutrition 0.000 description 1
- 240000002853 Nelumbo nucifera Species 0.000 description 1
- 235000006510 Nelumbo pentapetala Nutrition 0.000 description 1
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000003851 biochemical process Effects 0.000 description 1
- 238000005842 biochemical reaction Methods 0.000 description 1
- 239000010962 carbon steel Substances 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 230000001932 seasonal effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Landscapes
- Biological Treatment Of Waste Water (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
The utility model discloses a kind of multistage multistage integrated sewage processor, the device stable water outlet, efficient, maintenance convenience.The multistage multistage integrated sewage processor of the utility model, main structure include cabinet, aerating system and equipment room, and the cabinet is successively separated into anaerobic zone, anoxic zone, aerobic zone, settling zone, filtering area, gathering ground and clear water zone by partition；The equipment room is integrated in above cabinet, includes elevator pump, sludge pump, blower and various instrument valves, wherein pump and instrument valve are external, equipment room pipeline is all drawn from partition, is located at below cabinet upper baffle plate；Biological suspended packing is filled in the aerobic zone；The filtering area is complete set of equipments filtration system；The water intake mode of multistage multistage integrated sewage processor is using multistage water inlet.
Description
Technical field
The utility model relates to a kind of sewage-treatment plants, and in particular to a kind of multistage multistage integrated form sewage treatment dress
It sets.
Background technique
Decentralized type sewage processing technique, using traditional A2Integration apparatus based on/O biochemical process can play denitrogenation and remove
The effect of phosphorus, but itself there is also certain limitation, denitrogenation can not reach good effect with dephosphorization simultaneously, so as to cause
The problems such as effluent quality fluctuation is bigger, regular not up to standard occurs.Traditional integral process does not consider water outlet excessively
SS, it is general after extended meeting connect the treatment facilities such as artificial swamp, occupied area is larger, vulnerable to seasonal effect and treatment effect it is unstable
Deng.
The buried integrated sewage treating apparatus of tradition, equipment room are normally at equipment rear end, are placed in underground, operation inspection
Repair inconvenience.
With the development of the social economy, the requirement for environmental protection is also increasingly stringenter, in view of traditional integrated sewage disposal
The treatment effect that equipment occurs is unstable, overhauls the disadvantages of constant, needs to improve the integrated of integrated sewage treating apparatus, by force
While changing technological effect, accomplish the Highgrade integration of equipment, therefore, multistage multistage integrated form is obtained except TN sewage-treatment plant
Extensive research and application.
Summary of the invention
The utility model in view of the above-mentioned problems, providing a kind of multistage multistage integrated sewage processor, which goes out
Water is stable, efficient, and maintenance is convenient.
The technical scheme adopted by the utility model is
The multistage multistage integrated sewage processor of the utility model, main structure include cabinet, aerating system and
Equipment room, the cabinet be successively separated by partition anaerobic zone, anoxic zone, aerobic zone, settling zone, filtering area, gathering ground and
Clear water zone；The equipment room is integrated in above cabinet, includes elevator pump, sludge pump, blower and various instrument valves, wherein
Pump and instrument valve are external, and equipment room pipeline is all drawn from partition, are located at below cabinet upper baffle plate；In the aerobic zone
Fill biological suspended packing；The filtering area is complete set of equipments filtration system；Multistage multistage integrated sewage processor into
Water mode is using multistage water inlet.
The multistage multistage integrated sewage processor of the utility model, further technical solution are the cabinets
Multiple access holes are arranged in top.
The multistage multistage integrated sewage processor of the utility model, further technical solution can also be described
Anaerobic zone, anoxic zone, aerobic zone effective volume ratio be 1~2:1~2:3~8.
The multistage multistage integrated sewage processor of the utility model, further technical solution can also be described
Anoxic zone or it is aerobic divide into three-level, every grade of effective volume division scale is 1~2:1~2:1~2.Further technology
Scheme is that the biological suspended packing material is polyethylene, specific surface area 600m2/m3~1500m2/m3, specific gravity 0.98~
1.02g/cm3, whole dosing rate 10%~40%.
The multistage multistage integrated sewage processor of the utility model, further technical solution can also be described
Anoxic zone, aerobic zone bottom be arranged inclined plate, height 100~350mm, 45 °~60 ° of tilt angle, be provided with and wear between inclined plate
Hole aeration tube.
The multistage multistage integrated sewage processor of the utility model, further technical solution can also be described
Settling zone 1~4 sludge bucket is set, the another effluent weir that is arranged collects water outlet, overflow weir Design cooling load 0.5L/s.m~1.5L/
s.m。
The multistage multistage integrated sewage processor of the utility model, further technical solution can also be described
Aerating system use boring aeration, anoxic zone and aerobic zone share a set of aerating system, be aerated opening diameter 1mm~10mm,
10~50:1 of gas-water ratio is rationally controlled each section dissolved oxygen concentration by valve.
The multistage multistage integrated sewage processor of the utility model, further technical solution can also be described
Complete set of equipments filtration system include intake pump, backwashing pump and filtering tank；It intakes mating collecting-tank, the collecting-tank residence time
1h~3h, backwashes mating clear water reserviors, clear water reserviors residence time 0.3h~1h, and complete set of equipments filtration system takes independent automatic control
System is rationally controlled, 5~15min of recoil time, time interval 5h~48h.
The multistage multistage integrated sewage processor of the utility model, further technical solution can also be described
2~4:1 of water inlet ratio~2:1, guarantee the supply of subsequent carbon source and cancel in reflux；At the multistage multistage integrated form sewage
It manages device and all realizes automatic control, realized and monitored in real time using APP.
The beneficial effects of the utility model are as follows:
The utility model takes multi-section water-inlet, the mode of multistage operation, it is ensured that the carbon source supply of subsequent nitrification denitrogenation,
Strengthened denitrification effect solves the disadvantage that conventional integration apparatus goes out water unstable, can guarantee that stable water outlet is up to standard.Aerobic zone
Biological suspended packing is added, the sludge loading of biochemical reaction is improved, optimizes pond body volume, reduces occupied area.Filtering area uses
Set of filter plant, maintenance control are rationally simple.Equipment room is integrated in cabinet top, the matched valve of Pumps & Fans, metering
Equipment all unified setting and integrated controls, all realize precisely metering.Matched with devices APP realizes real time monitoring, understands at any time
Equipment operation condition.The utility model flows back in cancelling, and saves energy consumption, reduces operating cost, is not necessarily to personal management, only need to be part-time
Personnel's periodic maintenance.Integration degree is high for integral device, and size is small, and management service is convenient.
Detailed description of the invention
Fig. 1 is utility model structural facades figure；
Fig. 2 is utility model structural plan figure.
In figure: 1, cabinet, 2, equipment room, 3, partition, 4, access hole, 5, anaerobic zone, 6, anoxic zone, 7, aerobic zone, 8, heavy
Shallow lake area, 9, filtering area, 10, gathering ground, 11, clear water zone, 12, overcurrent mouth, 13, biological suspended packing, 14, elevator pump, 15, sludge
Pump, 16, blower, 17, aerating system, 18, inclined plate, 19, sludge bucket, 20, effluent weir.
Specific embodiment
The utility model is further described with reference to the accompanying drawings and examples, device scheme is as follows in embodiment:
As shown, the multistage multistage integrated sewage processor of the utility model, main structure include cabinet 1,
Equipment room 2, several reaction zones that the cabinet is separated by partition 3；Several access holes 4 are arranged in 1 top of cabinet, having a size of
600mm*600mm；The reaction zone is by anaerobic zone 5, anoxic zone 6, aerobic zone 7, settling zone 8, filtering area 9, gathering ground 10, clear water
Area 11 is constituted, anaerobic zone 5: anoxic zone 6: aerobic zone 7=1:1:3 (volume ratio)；The anoxic zone 6 is respectively divided into three with aerobic zone 7
Part, volume ratio 1:1:1；Reaction zone enters subsequent processing units by the gravity flow of overcurrent mouth 12 having a size of DN25；It is described aerobic
Biological suspended packing 13, specific surface area 800m2/m3, specific gravity 0.98g/cm3 packing ratio 30% are filled in area 7；The filtering area 9
It is made of complete set of equipments；The equipment room 2 is made of elevator pump 14, reflux pump 15, blower 16 and various instrument valves.At sewage
It manages device and uses carbon steel anticorrosion structure.
Wherein, the equipment room 2 is integrated in 1 top of cabinet, and equipment room size is 2000mm*1300*950mm；The exposure
Gas system 17 uses boring aeration, and anoxic zone 6 and aerobic zone 7 share a set of aerating system, is aerated opening diameter 5mm, passes through gas
The reasonable setting of water ratio 10:1 is regulated and controled with valve, so that whole system maintains optimal dissolved oxygen concentration.In the aerobic zone 7
Biological suspended packing 13 is filled, the carrier that filler adheres to as microorganism effectively increases sludge concentration, has higher processing negative
Lotus reduces occupied area.The anoxic zone 6,7 bottom of aerobic zone setting inclined plate 18, height 300mm, 60 ° of tilt angle.Aeration
Pipe is placed between inclined plate 18.2 sludge buckets 19 are arranged in the settling zone 8, and the another effluent weir 20 that is arranged collects water outlet, and effluent weir is set
Count load 1.0L/s.m, configuration reflux pump 15 realizes exteenal reflux and regular spoil disposal, especially for the equipment of small water, have compared with
High utility value.The filtering area 9 uses complete set of equipments, includes intake pump, backwashing pump and filtering tank.Water inlet made-up set
Pond 10, residence time 1h backwash mating clear water reserviors 11, and residence time 30min, recoil time interval 10h are rinsed every time
10min, a whole set of filtration system take independent robot control system(RCS) rationally to be controlled, and pass through water outlet qualified discharge.
In the present embodiment, sewage realize multi-section water-inlet, 2/5 enter anaerobic zone 5, later by flowmeter control, respectively into
Enter subsequent anoxic zone 6；Carbon source needed for subsequent water inlet mainly supplement denitrification reaction, specific water inlet ratio can be according to reality
Water inlet index be rationally arranged, realize the stable operation of whole system.The water outlet of afterbody aerobic zone 7 enters settling zone
8 carry out mud-water separation, and sludge sinks and sludge bucket 19, pass through the reflux pump 15 configured and realize exteenal reflux and regular spoil disposal.Settling zone 8
Supernatant enters collecting-tank 10 by effluent weir 20, enters filter plant by elevator pump, passes through the row up to standard of clear water reserviors 11 later
It puts.
The present embodiment in application, influent COD in 300mg/L, ammonia nitrogen 35mg/L, total phosphorus 10mg/L, it is more using above-mentioned multistage
Section integrated form removes TN sewage-treatment plant, and effluent quality reaches " urban wastewater treatment firm pollutant emission standard " level-one A mark
It is quasi-.
Claims (10)
1. a kind of multistage multistage integrated sewage processor, main structure includes cabinet, aerating system and equipment room, spy
Sign is that the cabinet is successively separated into anaerobic zone, anoxic zone, aerobic zone, settling zone, filtering area, gathering ground and clear by partition
Pool；The equipment room is integrated in above cabinet, includes elevator pump, sludge pump, blower and various instrument valves, wherein pumping
And instrument valve is external, equipment room pipeline is all drawn from partition, is located at below cabinet upper baffle plate；It is filled out in the aerobic zone
Fill biological suspended packing；The filtering area is complete set of equipments filtration system；The water inlet of multistage multistage integrated sewage processor
Mode is using multistage water inlet.
2. multistage multistage integrated sewage processor according to claim 1, it is characterised in that the cabinet top
Multiple access holes are set.
3. multistage multistage integrated sewage processor according to claim 1, it is characterised in that the anaerobic zone lacks
Oxygen area, aerobic zone effective volume ratio are 1~2:1~2:3~8.
4. multistage multistage integrated sewage processor according to claim 1 or 3, it is characterised in that the anoxic zone
Or it is aerobic divide into three-level, every grade of effective volume division scale is 1~2:1~2:1~2.
5. multistage multistage integrated sewage processor according to claim 4, it is characterised in that the biological suspension
Filler material is polyethylene, specific surface area 600m2/m3~1500m2/m3, 0.98~1.02g/cm3 of specific gravity, whole dosing rate
10%~40%.
6. multistage multistage integrated sewage processor according to claim 1, it is characterised in that the anoxic zone, good
Inclined plate is arranged in oxygen area bottom, and 100~350mm of height, is provided with boring aeration pipe by 45 °~60 ° of tilt angle between inclined plate.
7. multistage multistage integrated sewage processor according to claim 1, it is characterised in that the settling zone is set
1~4 sludge bucket is set, the another effluent weir that is arranged collects water outlet, overflow weir Design cooling load 0.5L/s.m~1.5L/s.m.
8. multistage multistage integrated sewage processor according to claim 1, it is characterised in that the aerating system
Using boring aeration, anoxic zone and aerobic zone share a set of aerating system, are aerated opening diameter 1mm~10mm, and gas-water ratio 10~
50:1 is rationally controlled each section dissolved oxygen concentration by valve.
9. multistage multistage integrated sewage processor according to claim 1, it is characterised in that the complete set of equipments
Filtration system includes intake pump, backwashing pump and filtering tank；It intakes mating collecting-tank, collecting-tank residence time 1h~3h, instead
Flushing clear water reserviors, clear water reserviors residence time 0.3h~1h, complete set of equipments filtration system take independent robot control system(RCS) to carry out
Rationally control, 5~15min of recoil time, time interval 5h~48h.
10. multistage multistage integrated sewage processor according to claim 1, it is characterised in that the water inlet ratio
2~4:1~2:1, the multistage multistage integrated sewage processor are all realized and are automatically controlled, and are realized using APP real-time
Monitoring.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820614123.8U CN208532384U (en) | 2018-04-27 | 2018-04-27 | A kind of multistage multistage integrated sewage processor |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820614123.8U CN208532384U (en) | 2018-04-27 | 2018-04-27 | A kind of multistage multistage integrated sewage processor |
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| Publication Number | Publication Date |
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| CN208532384U true CN208532384U (en) | 2019-02-22 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110104900A (en) * | 2019-06-03 | 2019-08-09 | 西安西热水务环保有限公司 | A kind of environmentally friendly high efficiency composition thermal power plant domestic sewage processing system and method |
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2018
- 2018-04-27 CN CN201820614123.8U patent/CN208532384U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110104900A (en) * | 2019-06-03 | 2019-08-09 | 西安西热水务环保有限公司 | A kind of environmentally friendly high efficiency composition thermal power plant domestic sewage processing system and method |
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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 |
Denomination of utility model: A multi-level and multi-stage integrated sewage treatment device Effective date of registration: 20230822 Granted publication date: 20190222 Pledgee: Chengdong Branch of Nanjing Bank Co.,Ltd. Pledgor: JIANGSU AONISI ENVIRONMENTAL PROTECTION TECHNOLOGY Co.,Ltd. Registration number: Y2023980053248 |
|
| PE01 | Entry into force 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: 20190222 Pledgee: Chengdong Branch of Nanjing Bank Co.,Ltd. Pledgor: JIANGSU AONISI ENVIRONMENTAL PROTECTION TECHNOLOGY Co.,Ltd. Registration number: Y2023980053248 |
|
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: A multi-level and multi-stage integrated sewage treatment device Granted publication date: 20190222 Pledgee: Chengdong Branch of Nanjing Bank Co.,Ltd. Pledgor: JIANGSU AONISI ENVIRONMENTAL PROTECTION TECHNOLOGY Co.,Ltd. Registration number: Y2024980037782 |