CN110240350A - It is a kind of to enhance sewerage integrated equipment and impact resistance method using nitrification liquid reflux - Google Patents
It is a kind of to enhance sewerage integrated equipment and impact resistance method using nitrification liquid reflux Download PDFInfo
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- CN110240350A CN110240350A CN201910210166.9A CN201910210166A CN110240350A CN 110240350 A CN110240350 A CN 110240350A CN 201910210166 A CN201910210166 A CN 201910210166A CN 110240350 A CN110240350 A CN 110240350A
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- 239000007788 liquid Substances 0.000 title claims abstract description 47
- 238000000034 method Methods 0.000 title claims abstract description 43
- 238000010992 reflux Methods 0.000 title claims abstract description 25
- 239000010865 sewage Substances 0.000 claims abstract description 65
- 230000003750 conditioning effect Effects 0.000 claims abstract description 48
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 41
- 239000010802 sludge Substances 0.000 claims abstract description 22
- 238000011282 treatment Methods 0.000 claims abstract description 19
- 239000007787 solid Substances 0.000 claims abstract description 15
- 230000005484 gravity Effects 0.000 claims abstract description 10
- 238000011221 initial treatment Methods 0.000 claims abstract description 7
- 238000000926 separation method Methods 0.000 claims abstract description 6
- 238000012545 processing Methods 0.000 claims abstract description 5
- 230000029087 digestion Effects 0.000 claims abstract description 4
- 239000006228 supernatant Substances 0.000 claims abstract description 4
- 238000005273 aeration Methods 0.000 claims description 11
- 230000002708 enhancing effect Effects 0.000 claims description 10
- 238000013461 design Methods 0.000 claims description 4
- 230000000717 retained effect Effects 0.000 claims description 2
- 230000014759 maintenance of location Effects 0.000 abstract 1
- 230000008569 process Effects 0.000 description 21
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 11
- 239000002351 wastewater Substances 0.000 description 9
- 238000005516 engineering process Methods 0.000 description 8
- 208000028659 discharge Diseases 0.000 description 7
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 229910052757 nitrogen Inorganic materials 0.000 description 5
- 239000001301 oxygen Substances 0.000 description 5
- 229910052760 oxygen Inorganic materials 0.000 description 5
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 4
- 241000894006 Bacteria Species 0.000 description 4
- 230000003647 oxidation Effects 0.000 description 4
- 238000007254 oxidation reaction Methods 0.000 description 4
- 230000008859 change Effects 0.000 description 3
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 2
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 2
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 229910021529 ammonia Inorganic materials 0.000 description 2
- 238000013459 approach Methods 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 238000011953 bioanalysis Methods 0.000 description 2
- 230000003851 biochemical process Effects 0.000 description 2
- 238000011109 contamination Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000010790 dilution Methods 0.000 description 2
- 239000012895 dilution Substances 0.000 description 2
- 238000012851 eutrophication Methods 0.000 description 2
- 238000007667 floating Methods 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 229910017604 nitric acid Inorganic materials 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 229910052698 phosphorus Inorganic materials 0.000 description 2
- 239000011574 phosphorus Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 229910002651 NO3 Inorganic materials 0.000 description 1
- IOVCWXUNBOPUCH-UHFFFAOYSA-M Nitrite anion Chemical compound [O-]N=O IOVCWXUNBOPUCH-UHFFFAOYSA-M 0.000 description 1
- CKUAXEQHGKSLHN-UHFFFAOYSA-N [C].[N] Chemical compound [C].[N] CKUAXEQHGKSLHN-UHFFFAOYSA-N 0.000 description 1
- 150000001413 amino acids Chemical class 0.000 description 1
- 238000007630 basic procedure Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 239000003864 humus Substances 0.000 description 1
- BHEPBYXIRTUNPN-UHFFFAOYSA-N hydridophosphorus(.) (triplet) Chemical compound [PH] BHEPBYXIRTUNPN-UHFFFAOYSA-N 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 239000013067 intermediate product Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 230000002906 microbiologic effect Effects 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000006396 nitration reaction Methods 0.000 description 1
- 238000006902 nitrogenation reaction Methods 0.000 description 1
- 230000020477 pH reduction Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 238000012163 sequencing technique Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000008223 sterile water Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/30—Aerobic and anaerobic processes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Biodiversity & Conservation Biology (AREA)
- Microbiology (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
Enhance sewerage integrated equipment and impact resistance method using nitrification liquid reflux the invention discloses a kind of, it is related to technical field of sewage.Sewage enters grille well and carries out primary treatment, conditioning tank will be entered after the solid of larger size in sewage and hair retention, sewage carries out anaerobic digestion and separation of solid and liquid here, and most of lesser suspended matter of density floats to form dross, and most of biggish solid of density is deposited in the bottom of conditioning tank；Elevator pump in conditioning tank is by conditioning tank sewage lifting to anoxic pond, carry out biochemical treatment, after sewage passes sequentially through the processing of anoxic and aerobic tank, sludge settling is carried out in secondary settling tank, the supernatant gravity flow of secondary settling tank enters clear water reserviors, clear water is formed, clear water is by gravity flow or promotes the water body near being discharged into.The present invention saves equipment investment expense, reduces the biochemical treatment impact to sewage disposal device, practical reliable, has a extensive future.
Description
Technical field
The present invention relates to technical field of sewage, and in particular to a kind of to utilize nitrification liquid reflux enhancing sewage one
The equipment and impact resistance method of change.
Background technique
Country sewage feature has: the total amount that 1. country sewage generates is very big, but individually peasant household's sewage effluent amount is smaller, individually
Treating stations treatment scale is smaller.
2. sewage discharge diurnal variation is big.The discharge of country sewage has uneven Drainage feature, and early, late discharge amount is big,
His period discharge amount is smaller, night few sewage discharge, and diurnal variation is larger.
3. discharge dispersion.Rural residence population is not concentrated, and distribution density is small, the Sewage outlet that do not fix, and lacks row
Water collection system；Collecting sewage by extensive sewage collecting pipe network, there are Difficulties, and the investment of sewage collecting pipe network is very
Greatly, collection rate is also very low.
4. influent quality is relatively stable, biodegradability is generally preferable.
Wherein, sewage variation coefficient height is the significant difficulty of rural domestic sewage treatment, and sewage ash machine focuses in the morning, afternoon and evening three
A period generates, at this point, the common approach is that increase the residence time of conditioning tank, and increase occupation area of equipment, while
Increase investment cost.
Currently, the technology of sewage treatment has:
(1) activated sludge technology: activated sludge technology is a kind of bioanalysis, and air is passed through into waste water, keeps aerobic microbiological numerous
It grows culture and forms the activated sludge for having very strong adsorption capacity, bioanalysis is increasingly becoming the main stream approach of sewage disposal technology.Activity
The basic procedure of sludge technology: it is made of aeration tank, secondary sedimentation tank, aerating system and sludge recirculation system.By sinking for the first time
The waste water of shallow lake pond outflow enters aeration tank with the activated sludge to flow back from secondary precipitation bottom of pond portion simultaneously, becomes mixed liquor.It is exposing
Under the action of gas pond, mixed liquor is sufficiently aerated, and comes into full contact with activated sludge and waste water, the soluble organic contamination in waste water
Object is adsorbed by activated sludge, and is decomposed by micropopulation, and waste water is purified.
Activated sludge technology specifically further includes many kinds, wherein having general expression activated sludge process, oxidation ditch process, AB two-part
Activated sludge process, sequencing batch activated sludge (SBR) method, being thoroughly mixed property sludge etc..
(2) A/O Process: also it is anaerobic-aerobic Process.It, can also be same in addition to can remove the organic contamination beyond the region of objective existence in waste water
When go to denitrogenate, hydrolysis acidification section is arranged before aerobic section, can significantly mention for high concentrated organic wastewater and used water difficult to degradate for phosphorus
High wastewater biodegradability.
(3) A2/O method: biological denitrification phosphorous removal technique is conventional activated sludge process, biological nitration and denitrification process and life
The synthesis of object dephosphorization process.The process efficiency can generally reach: BOD5 and SS is 90%-95%, and total nitrogen is 70% or more, phosphorus
It is 90% or so, applies in general to the large- and-medium size cities sewage plant for requiring denitrogenation dephosphorizing, but the capital cost and running cost of A2/O technique
It is above conventional activated sludge process, operational management requires height, so sewage is discharged into when treated for current China's national situation
Closure water body or slow flow water bodies cause eutrophication, to just use the technique when influencing water supply source.
(4) biological aerated filter: abbreviation BAF is the third for integrating both biofilm and activated sludge process advantage
For biofilter, BAF has the function of removing organic matter, harmful substance, denitrogenation, dephosphorization;Occupied area is small, capital expenditure is few,
Energy consumption and operating cost are low.
(5) contact oxidation method: biological contact oxidation process is a kind of biological effluent treatment derived from from biofilm.
Sewage is in contact with biomembrane in the process, under the action of microorganism on biomembrane, can make to purify the sewage, therefore again
Claim " submerged bacteria filter ".This method provides the oxygen amount that Institute of Micro-biology needs using aeration method identical with aeration tank, and rises
Stirring and mixed effect, while adding filler in aeration tank.
(6) integration MBR technique: a kind of tradition combining activated sludge process and Integral immersion film separation system changes
It is outstanding effectively to remove solid instead of traditional infall process for good figure technique, the separation of solid and liquid process carried out using membrane module
Floating particles and organic granular, prepare sterile water.System water outlet can be directly used for producing or living reuse.Waste water passes through present treatment system
The indices of system processing discharge water outlet can achieve the specified value of " urban sewage reutilization urban reclaimed water water quality ".
The common sewage disposal technology of the above is required to be aerated, and in order to solve the requirement of removal denitrogenation, is all provided with
Anoxic (denitrification) and aerobic (nitrification) two kinds of environment are counted, to reduce the polluted by nitrogen and eutrophication problem that are discharged into river,
It is the common recognition of environmentalist.Aerobic Process for Treatment refers in the presence of microorganism, in conditions such as suitable carbon-nitrogen ratio, moisture content and oxygen
Under, by organic matter degradation, it is converted to the biochemical process of humus sample substance.The ammonia that nitrification amino acid is taken off, aerobic
Under the conditions of, the effect through nitrite bacteria and nitrate bacteria is converted into the process of nitric acid.The oxidation that ammonia is converted into nitric acid must have
O2It participates in.Anoxic pond is with respect to the department of biochemistry for for anaerobic and aerobic, generally referring to dissolved oxygen control between 0.2-0.5mg/l
System.Denitrification, also referred to as denitrification refer to bacterium by nitrate (NO3) in nitrogen (N) pass through series of intermediate products (NO2−、
NO、N2O) it is reduced to nitrogen (N2) Biochemical processes, that is, denitrification process.Therefore in order to reach in sewage treatment project
To the effect of azo, it can all be designed as AN/O technique, that is, anoxic+aerobic, such as Fig. 1, still, this nitrification liquid reflux type
It needs using nitrification liquid reflux pump 10, equipment investment is costly, simultaneously as when the generation of sanitary sewage usually has very big
Between variation coefficient especially in field of rural sewage water treatment lead to a large amount of water inlets of integrated equipment for sewage treatment interval, to dirt
The biochemical treatment of water treatment facilities causes very big impact.Based on this, if a kind of utilize nitrification liquid reflux enhancing sewage one
The equipment and impact resistance method of change are particularly necessary.
Summary of the invention
In view of the shortcomings of the prior art, a kind of dirty using nitrification liquid reflux enhancing object of the present invention is to be to provide
Water integrated equipment and impact resistance method, it is reasonable in design, equipment investment expense is saved, is reduced to sewage disposal device
Biochemical treatment impact, practical, high reliablity, use easy to spread.
To achieve the goals above, the present invention is to realize by the following technical solutions: a kind of to be flowed back using nitrification liquid
Enhance sewerage integrated equipment, including conditioning tank, anoxic pond, aerobic tank, Aeration fan, secondary settling tank, storage basin and clear water reserviors,
Conditioning tank is connected to anoxic pond by elevator pump, and anoxic pond, aerobic tank, secondary settling tank, clear water reserviors are set gradually, anoxic pond, aerobic
Aeration fan is installed above pond, secondary settling tank is connected to storage basin, and the aerobic tank is connected to conditioning tank by return pipe.
Preferably, the conditioning tank front end is provided with thickness twice grid, to sewage primary treatment, by sewage compared with
Large-sized solid and hair are retained.
Preferably, the liquid level of the aerobic tank is higher than conditioning tank, the refluxing opening being arranged on aerobic tank and return pipe phase
Connection, allows the water of aerobic tank to be back to conditioning tank, the end of return pipe is goed deep into conditioning tank, and the end of return pipe is equipped with
Ball-cock assembly, when the liquid level of conditioning tank is lower than this liquid level, backflow functionality is opened；If the liquid level in conditioning tank is not less than ball-cock assembly
Liquid level is designed, backflow functionality stops.
A kind of impact resistance method enhancing sewerage integrated equipment using nitrification liquid reflux, the steps include: sewage into
Enter grille well and carry out primary treatment, is cut the solid of larger size in sewage and hair etc. by the artificial grid of thickness twice
After staying, into conditioning tank, sewage carries out anaerobic digestion and separation of solid and liquid, most of lesser suspended matter floating shape of density here
At dross, most of biggish solid of density, such as sandstone are deposited in the bottom of conditioning tank, convenient for drawing clearly；Mentioning in conditioning tank
Pump is risen by conditioning tank sewage lifting to anoxic pond, starts to carry out biochemical treatment, sewage passes sequentially through the place of anoxic pond and aerobic tank
After reason, sludge settling is carried out in secondary settling tank, the supernatant gravity flow of secondary settling tank enters clear water reserviors, forms clear water, clear water passes through gravity flow
Or it is promoted and is discharged into neighbouring water body.
Beneficial effects of the present invention: the present apparatus makes nitrification liquid be back to conditioning tank by the way of gravity stream, greatlys save
Equipment investment expense, while a degree of dilution is carried out to sewage, reduce biochemical treatment of the sewage to anoxic pond and aerobic tank
Impact.
Detailed description of the invention
The following describes the present invention in detail with reference to the accompanying drawings and specific embodiments；
Fig. 1 is the structural schematic diagram of background technique；
Fig. 2 is structural schematic diagram of the invention；
Fig. 3 is process flow chart of the invention.
Specific embodiment
To be easy to understand the technical means, the creative features, the aims and the efficiencies achieved by the present invention, below with reference to
Specific embodiment, the present invention is further explained.
Referring to Fig. 2-3, present embodiment uses following technical scheme: a kind of to utilize nitrification liquid reflux enhancing sewage one
The equipment of body, including conditioning tank 1, anoxic pond 2, aerobic tank 3, Aeration fan 4, secondary settling tank 5, storage basin 6 and clear water reserviors 7 are adjusted
Section 1 front end of pond is provided with the thickness twice grid to sewage primary treatment, and conditioning tank 1 is connected to anoxic pond 2 by elevator pump 8,
Anoxic pond 2, aerobic tank 3, secondary settling tank 5, clear water reserviors 7 are set gradually, and Aeration fan 4 is equipped with above anoxic pond 2, aerobic tank 3, good
The liquid level in oxygen pond 3 is higher than conditioning tank 1, and the refluxing opening being arranged on aerobic tank 3 is connected with return pipe, and the end of return pipe is deeply adjusted
It saves in pond 1, the end of return pipe is equipped with ball-cock assembly, and secondary settling tank 5 is connected to storage basin 6, and the aerobic tank 3 passes through return pipe
It is connected to conditioning tank 1.
A kind of impact resistance method enhancing sewerage integrated equipment using nitrification liquid reflux, the steps include: sewage into
Enter grille well and carry out primary treatment, is cut the solid of larger size in sewage and hair etc. by the artificial grid of thickness twice
After staying, into conditioning tank 1, sewage carries out anaerobic digestion and separation of solid and liquid here, and most of lesser suspended matter of density floats
It forms dross, most of biggish solid of density, such as sandstone and is deposited in the bottom of conditioning tank 1, convenient for drawing clearly；In conditioning tank 1
Elevator pump 8 by conditioning tank sewage lifting to anoxic pond 2, start to carry out biochemical treatment, sewage passes sequentially through anoxic pond 2 and aerobic
After the processing in pond 3, sludge settling is carried out in secondary settling tank 5, the supernatant gravity flow of secondary settling tank 5 enters clear water reserviors 7, forms clear water, clearly
Water is by gravity flow or promotes the water body near being discharged into.
Present embodiment is higher than 1 liquid level of conditioning tank by the way of nitrification liquid reflux, using 3 liquid level of aerobic tank
Feature designs a refluxing opening in 3 water outlet of aerobic tank, so that the water of aerobic tank 3 is back to conditioning tank 1, nitrification liquid is returned
It is flow to conditioning tank, increases a pre- denitrogenation unit, has positive effect for reducing CODCr and total nitrogen in sewage disposal process,
Sewage because containing higher dissolved oxygen in nitrification liquid, and is substantially at anaerobism in conditioning tank 1 after the processing of aerobic tank 3
State contributes to form anaerobic condition after mixing, to achieve the effect that pre- denitrogenation, and then reduces total in sewage
Nitrogen；Meanwhile the reflux pipe end of nitrification liquid is equipped with ball-cock assembly, when the liquid level of conditioning tank 1 is lower than this liquid level, backflow functionality is opened
It opens, if the liquid level in conditioning tank 1 designs liquid level not less than ball-cock assembly, backflow functionality stops.
Present embodiment makes nitrification liquid be back to conditioning tank by the way of gravity stream, is not necessarily to nitrification liquid reflux pump,
Equipment investment expense is saved, sewage water is increased by reflux type, the sewage water in conditioning tank is made to keep abundant substantially
State, stabilizes sewage water, and elevator pump can reduce the failure rate of elevator pump, nitrification liquid is back to avoid frequent start-stop
Conditioning tank can carry out a degree of dilution to sewage, reduce a large amount of water inlets of interval to anoxic pond and aerobic tank using reflux
Biochemical treatment caused by impact, have a vast market application prospect.
The above shows and describes the basic principles and main features of the present invention and the advantages of the present invention.The technology of the industry
Personnel are it should be appreciated that the present invention is not limited to the above embodiments, and the above embodiments and description only describe this
The principle of invention, without departing from the spirit and scope of the present invention, various changes and improvements may be made to the invention, these changes
Change and improvement all fall within the protetion scope of the claimed invention.The claimed scope of the invention by appended claims and its
Equivalent thereof.
Claims (5)
1. a kind of enhance sewerage integrated equipment using nitrification liquid reflux, which is characterized in that including conditioning tank (1), anoxic pond
(2), aerobic tank (3), Aeration fan (4), secondary settling tank (5), storage basin (6) and clear water reserviors (7), conditioning tank (1) pass through elevator pump
(8) it being connected to anoxic pond (2), anoxic pond (2), aerobic tank (3), secondary settling tank (5), clear water reserviors (7) are set gradually, anoxic pond (2),
It is equipped with Aeration fan (4) above aerobic tank (3), secondary settling tank (5) is connected to storage basin (6), and the aerobic tank (3) passes through back
Flow tube is connected to conditioning tank (1).
2. a kind of equipment sewerage integrated using nitrification liquid reflux enhancing according to claim 1, which is characterized in that institute
Conditioning tank (1) front end stated is provided with the thickness twice grid to sewage primary treatment.
3. a kind of equipment sewerage integrated using nitrification liquid reflux enhancing according to claim 1, which is characterized in that institute
The liquid level for the aerobic tank (3) stated is higher than conditioning tank (1), and the refluxing opening being arranged on aerobic tank (3) is connected with return pipe, return pipe
End go deep into conditioning tank (1).
4. a kind of equipment sewerage integrated using nitrification liquid reflux enhancing according to claim 3, which is characterized in that institute
The end for the return pipe stated is equipped with ball-cock assembly (9), and when the liquid level of conditioning tank (1) is lower than this liquid level, backflow functionality is opened；When
Liquid level in conditioning tank (1) designs liquid level not less than ball-cock assembly, and backflow functionality stops.
5. a kind of impact resistance method for enhancing sewerage integrated equipment using nitrification liquid reflux, which is characterized in that its step
Are as follows: sewage enters grille well and carries out primary treatment, by the artificial grid of thickness twice by the solid and hair of larger size in sewage
After hair etc. is retained, into conditioning tank (1), sewage carries out anaerobic digestion and separation of solid and liquid here, and most of density is smaller
Suspended matter float to form dross, most of biggish solid of density, as sandstone is deposited in the bottom of conditioning tank (1)；Conditioning tank
(1) conditioning tank sewage lifting to anoxic pond (2) are started to carry out biochemical treatment, sewage passes sequentially through anoxic by the elevator pump (8) in
After the processing of pond (2) and aerobic tank (3), sludge settling is carried out in secondary settling tank (5), sludge is discharged into storage basin (6), secondary settling tank (5)
Supernatant gravity flow enter clear water reserviors (7), form clear water, clear water is by gravity flow or is promoted and is discharged into neighbouring water body.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201910210166.9A CN110240350A (en) | 2019-03-19 | 2019-03-19 | It is a kind of to enhance sewerage integrated equipment and impact resistance method using nitrification liquid reflux |
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| CN201910210166.9A CN110240350A (en) | 2019-03-19 | 2019-03-19 | It is a kind of to enhance sewerage integrated equipment and impact resistance method using nitrification liquid reflux |
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| CN110510830A (en) * | 2019-09-23 | 2019-11-29 | 苏州首创嘉净环保科技股份有限公司 | A kind of sewage disposal device promoting anoxic pond aeration stirring effect |
| CN113480111A (en) * | 2021-08-20 | 2021-10-08 | 北京海华云拓能源研发中心有限公司 | Organic sewage cyclic degradation system |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN110510830A (en) * | 2019-09-23 | 2019-11-29 | 苏州首创嘉净环保科技股份有限公司 | A kind of sewage disposal device promoting anoxic pond aeration stirring effect |
| CN113480111A (en) * | 2021-08-20 | 2021-10-08 | 北京海华云拓能源研发中心有限公司 | Organic sewage cyclic degradation system |
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Application publication date: 20190917 |