CN106430605A - Artificial wetland device for deep denitrification of tail water in sewage treatment plant and application - Google Patents

Artificial wetland device for deep denitrification of tail water in sewage treatment plant and application Download PDF

Info

Publication number
CN106430605A
CN106430605A CN201611050608.0A CN201611050608A CN106430605A CN 106430605 A CN106430605 A CN 106430605A CN 201611050608 A CN201611050608 A CN 201611050608A CN 106430605 A CN106430605 A CN 106430605A
Authority
CN
China
Prior art keywords
gravel
hypothalluses
tail water
sewage treatment
treatment plant
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN201611050608.0A
Other languages
Chinese (zh)
Other versions
CN106430605B (en
Inventor
郑晓英
朱星
陈卫
周翔
高雅洁
周橄
卢丹
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hohai University HHU
Original Assignee
Hohai University HHU
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hohai University HHU filed Critical Hohai University HHU
Priority to CN201611050608.0A priority Critical patent/CN106430605B/en
Publication of CN106430605A publication Critical patent/CN106430605A/en
Application granted granted Critical
Publication of CN106430605B publication Critical patent/CN106430605B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/32Biological treatment of water, waste water, or sewage characterised by the animals or plants used, e.g. algae
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/005Combined electrochemical biological processes
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Environmental & Geological Engineering (AREA)
  • Hydrology & Water Resources (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Microbiology (AREA)
  • Molecular Biology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Electrochemistry (AREA)
  • Biotechnology (AREA)
  • Botany (AREA)
  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
  • Biological Treatment Of Waste Water (AREA)

Abstract

The invention discloses an artificial wetland device for deep denitrification of tail water in a sewage treatment plant and application. The artificial wetland device sequentially comprises a vegetation layer, a coarse sand layer, a first gravel matrix layer, a second gravel matrix layer, a supporting layer and a water collecting region from top to bottom, wherein the first gravel matrix layer and the second gravel matrix layer are uniformly doped with iron charcoal; the water collecting region is located below the supporting layer; a perforated organic glass water collecting plate is mounted at the top of the water collecting region. The artificial wetland device provided by the invention is simple in structure and convenient to operate and manage, can effectively purify the tail water of the sewage treatment plant, in particular, improves the denitrification efficiency of artificial wetland, realizes the goal of efficient denitrification and stable operation throughout the year, can further reduce the concentration of pollutants in effluent water of the sewage treatment plant, and is conducive to continuous improvement of water environment.

Description

Constructed wetland device for sewage treatment plant tail water advanced nitrogen and application
Technical field
The present invention relates to sewage treatment area, more particularly to a kind of artificial for sewage treatment plant tail water advanced treating Wetland high-efficiency nitrogen rejection facility.
Background technology
At present, most of sewage treatment plant of China still based on two stage treatment although sewage second-level biological treatment can cut down Most of pollutant, tail Organic substance in water, nitrogen, phosphorus concentration are still higher.2010-2014, south China urban wastewater treatment The main water quality index of factory's secondary effluent is as follows:COD 51.64±22.11mg/L、NH4 +-N 12.63±9.02mg/L、TN 21.54±12.49mg/L、TP 1.94±1.28mg/L.It can be seen that, in tail water, pollutant load is still very high, especially TN concentration Higher, some sewage treatment plants are also often faced with the exceeded risk of water outlet TN.Will even if sewage plant tail water reaches maximum emission Ask《Urban wastewater treatment firm pollutant emission standard》(GB18918-2002) one-level A standard, still falls within bad V class water, right Still important polluter for receiving water body.For the limited receiving water body of self-purification capacity, sewage second-level Process can not fundamentally solve its eutrophication problem, can only delay its development trend.In addition, internationally recognized water body is rich Nutrient laden marginal value is [TN 0.2mg/L, TP 0.2mg/L], and therefore, secondary effluent is still to cause receiving water body eutrophication One of major reason.
Sewage plant tail water is carried out advanced treating, the impact to receiving water body for the tail water can be reduced, improve China's water environment; Tail water water quality through advanced treating reaches after certain standard, also can be back to industrial or agricultural and municipal water use, supplements surface water, carries out Groundwater recharge etc., thus increasing water supply, reduces the impact to environment for the behavior of men.Artificial swamp is to develop in recent years A kind of novel ecological treatment technology getting up, all has good effect in terms of organic pollution, antibacterial, trace organic substance removal Really, have been widely used at purification of water quality and recovery, pollution of area source control, rainwater treatment and the utilization, sewage of polluted-water The fields such as reason, have that pollutant removal is stable, the low remarkable advantage of reduced investment, operating cost, are to cut down in secondary effluent One of effective technique of the pollutant such as nitrogen phosphorus, is that the advanced treating of sewage treatment plant tail water opens a new way.
Vertical current constructed wetland is more and more wider due to being subject to the advantages of floor space is few, high treating effect, sanitary condition are good General concern.Meanwhile, vertical current constructed wetland is formed aerobic, anoxia, anaerobic environment, are conducive to microorganism nitrification, denitrification The carrying out of effect, thus improve the nitric efficiency of device.But, sewage treatment plant tail water is being processed using vertical current constructed wetland When, due to the special water quality of tail water, find to still suffer from following defect:(1) after two stage treatment, the carbon source of tail water is low, can give birth to Poor (the BOD of the property changed5/ COD is 0.1~0.35, BOD5/ TN is about 1), the Organic substance in tail water is mainly fulvic acid, humic acid, table Face activating agent and other trace hardly degraded organic substances, these Organic substances are difficult to be utilized by the microorganism, and wetland device can utilize carbon Source deficiency is that restriction micro-organisms Denitrification leads to the low main cause of nitric efficiency;(2) because winter temperature is low, vegetable layer Withered, plant declines to the removal ability of pollutant, or even can discharge part nitrogen phosphorus in water;On the other hand, temperature drop meeting Reduce electron transport rate in microbial cell, lead to microbial activity and biological denitrificaion ability to decline, finally have impact on whole The denitrification effect of wetland device.
Content of the invention
The technical problem solving:Higher, the current perpendicular flow artificial for nitrogen content in sewage treatment plant's two stage treatment tail water Wetland variation sewage plant tail water has that carbon source is low, biodegradability is poor, the dirt-removing power of winter temperature low impact wetland device, thus Lead to the low problem of its nitric efficiency, the present invention provides a kind of constructed wetland device for sewage treatment plant tail water advanced nitrogen And application.
Technical scheme:The described constructed wetland device for sewage treatment plant tail water advanced nitrogen, including from top to bottom according to The vegetable layer of secondary arrangement, coarse sands layer, the first gravel hypothalluses, the second gravel hypothalluses, supporting layer and gathering ground;
It is provided with the online ORP electrode of the first gravel hypothalluses in the middle part of described first gravel hypothalluses;
It is provided with the online ORP electrode of the second gravel hypothalluses in the middle part of described second gravel hypothalluses;
Described gathering ground top is provided with perforation water collection sheet, and gathering ground bottom is provided with the gradient and is 5% and is in funnelform slope, Described slope center is provided with slag-drip opening, additionally, gathering ground bottom is provided with support column;
The described constructed wetland device top for sewage treatment plant tail water advanced nitrogen is provided with water inlet, and bottom is provided with out The mouth of a river;
Described first gravel hypothalluses Uniform Doped ferrum charcoal I, in described ferrum charcoal I, ferrum charcoal mass ratio is MFe:MC=2:1~6: 1;
Described second gravel hypothalluses Uniform Doped ferrum charcoal II, in described ferrum charcoal II, ferrum charcoal mass ratio is MFe:MC=0.5:1 ~2:1.
Preferably, ferrum charcoal I is the bulk of diameter 10~30mm, in ferrum charcoal, ferrum charcoal mass ratio is MFe:MC=5:1.
Preferably, ferrum charcoal II is the bulk of diameter 10~30mm, in ferrum charcoal, ferrum charcoal mass ratio is MFe:MC=1:1.
Preferably, the coarse sand particle diameter of described coarse sands layer is 2~4mm.
Preferably, the grain size of gravel of described gravel hypothalluses is 4~8mm, the doping of described gravel hypothalluses and ferrum charcoal Ratio is the 0.5%~3% of gravel hypothalluses gross mass.
Preferably, described gravel hypothalluses are the 1% of gravel hypothalluses gross mass with the doping ratio of ferrum charcoal.
Preferably, described supporting layer is made up of gravel, described grain size of gravel is 8~16mm.
Preferably, described perforation water collection sheet open pore size is 5mm, percent opening is 8.25%.
Another kind of technical scheme of the present invention also includes described constructed wetland device in sewage treatment plant tail water advanced nitrogen In application.
Described applying step is:
1) tail water enters vegetable layer (4) from wetland device top, directly absorbs the nitrogen P elements in sewage using plant;
2) after carrying out initial absorption, tail water enters into coarse sands layer (5), removes oarse-grained float;
3) pretreated tail water enters the first gravel hypothalluses (6), will be organic for complicated macromole by Fe-C method Thing is decomposed into small organic molecule;
4) tail water after processing enters the second gravel hypothalluses (7), produces through the Denitrification of denitrifying bacterium and electrolysis Hydrogen Denitrification carries out denitrogenation to tail water, and described denitrifying bacterium is microsphere denitrifying bacterium.
Beneficial effect:1st, the present invention in the substrate of the first gravel hypothalluses Uniform Doped ferrum charcoal I (ferrum charcoal mass ratio is MFe:MC=2:1~6:1), the block ferrum charcoal of diameter 10~30mm, ferrum charcoal forms former electricity in the sewage with certain electrical conductivity , there is Inner electrolysis reaction in pond, compared with existing vertical current constructed wetland, can divide complicated larger molecular organicses in sewage Solve as small organic molecule, consuming the Denitrification for microorganism while oxygen provides more available carbon sources.
2nd, the present invention in the substrate of the second gravel hypothalluses Uniform Doped ferrum charcoal II (ferrum charcoal mass ratio is MFe:MC= 0.5:1~2:1), the block ferrum charcoal of diameter 10~30mm, under anaerobic, this gravel hypothalluses are traditional different except occurring Foster Denitrification outer it also occur that electrolytic hydrogen production autotrophic denitrification, the H that autotrophic denitrification bacterium is produced with electrode2Supply for electronics Body, nitrogen oxides are reduced into N as electron acceptor2.Compared with existing vertical current constructed wetland, tradition can not only be realized Heterotrophic denitrification denitrogenation, may additionally facilitate the autotrophic denitrification denitrogenation of microorganism, thus improve the nitric efficiency of wetland device.
3rd, compared with existing vertical current constructed wetland, the present invention pass through from top to bottom set gradually vegetable layer, coarse sands layer, First gravel hypothalluses, the second gravel hypothalluses and supporting layer, absorption of going forward one by one processes nitrogen, improves the denitrogenation of wetland device Efficiency.
4th, compared with existing vertical current constructed wetland, the present invention is in the first gravel hypothalluses and the second gravel hypothalluses There is galvanic interaction in the ferrum charcoal of doping, the nascent state iron ion of generation can participate in and pass through Fe in cell2+And Fe3+Between Redox reaction is come the electron transmission to carry out, thus improve the speed of biochemical reaction, and is effectively improved carbon source biodegradability; Being respectively provided with of two-layer ferrum charcoal can promote the synchronization of heterotrophic denitrification and autotrophic denitrification to be smoothed out, and improves wetland dress further Put nitric efficiency, the denitrification effect of wetland when particularly improving winter low temperature.
Brief description
Fig. 1 is apparatus of the present invention schematic diagram;
Fig. 2 is the structural representation of perforation water collection sheet.
In figure:1. enter bucket;2. peristaltic pump;3. water inlet pipe;4. vegetable layer;5. coarse sands layer;6. the first gravel hypothalluses;7. Second gravel hypothalluses;8. supporting layer;9. perforation water collection sheet;10. gathering ground;11. slag-drip openings;12. outlet pipes;13. second gravels Stone hypothalluses online ORP electrode;The online ORP electrode of 14. first gravel hypothalluses;15. ferrum charcoal I (MFe:MC=2:1~6:1); 16. ferrum charcoal II (MFe:MC=0.5:1~2:1);17. bottom support columns.
Specific embodiment
With reference to embodiment and accompanying drawing, the present invention is described in further detail.
Embodiment 1
Referring to Fig. 1, there is shown with a kind of constructed wetland device for sewage treatment plant tail water advanced nitrogen of the present invention Preferred embodiment, described constructed wetland device includes vegetable layer 4, coarse sands layer 5, the first gravel hypothalluses 6, the second gravel hypothalluses 7 and supporting layer 8, supporting layer 8 lower section is gathering ground 10.Sewage treatment plant tail water squeezes into wetland device by peristaltic pump 2, flows successively Through vegetable layer 4, the first gravel hypothalluses 6, the second gravel hypothalluses 7, supporting layer 8, worn by the lucite of supporting layer 8 lower section Hole water collection sheet 9 enters gathering ground 10, from bottom water outlet.
Vegetable layer 4 can have the emergent aquactic plant of flourishing root system from perennial phragmites communiss, Herba Typhae, Herba Lythri Salicariae etc., permissible Single or collocation miscegenation.Plant can directly absorb the nitrogen P elements in sewage, and complicated root system can be microorganism Absorption Growth provides bigger surface area moreover it is possible to convey oxygen, the penetration to substrate for the root system to wetland device, can strengthen The sedimentation of substrate, thus strengthen and maintain the hydraulic conductivity of substrate.
Coarse sands layer 5 medium coarse sand particle diameter is 2~4mm, is that microorganism provides stable attaching surface, also normal for plant Growth provides carrier.Coarse sands layer 5 can also float in effectively catching sewage, to delay the blocking of wetland device.Additionally, it is thick Layer of sand 5 itself can remove the nutrient substance such as nitrogen phosphorus in sewage by the materializing procedure such as absorption, filtration, ion exchange.
First gravel hypothalluses 6 are one of main removal units of pollutant, Uniform Doped ferrum charcoal I 15 (ferrum in substrate Charcoal mass ratio is MFe:MC=2:1~6:1), ferrum charcoal is immersed in the sewage with certain electrical conductivity and can form the former electricity of ferrum charcoal Pond, there is electrode reaction Fe-2e=Fe in anode2+(E0=-0.44V), in, under alkalescence condition negative electrode occur electrode reaction O2+ 2H2O+4e=4OH-(E0=+0.40V).Fe-C method process produces [H] and the Fe of activity in a large number2+, make the complexity in sewage There is the effect such as open loop, chain rupture in Organic substance, in addition, in Fe2+It is oxidized to Fe3+During, can produce with strong oxidizing property OH, O, can destroy-CN and C=O key.A series of redox reaction being caused by electrochemical action, can be by dirt Complicated larger molecular organicses in water are decomposed into small organic molecule, thus improving tail water biodegradability, are microorganism denitrification Effect provides and carbon source more can be utilized, and improves the nitric efficiency of wetland device.
Second gravel hypothalluses 7 are the formants of denitrogenation, and sewage biodegradability after the first gravel hypothalluses 6 obtains Improve, the heterotrophic denitrification effect for this unit provides carbon source more can be utilized, it is possible to increase denitrification denitrogenation efficiency. Second gravel hypothalluses 7 are also doped with ferrum charcoal II 16, and (ferrum charcoal mass ratio is MFe:MC=0.5:1~2:1), this gravel hypothalluses remove Occur outside traditional Denitrification, it also occur that electrolytic hydrogen production autotrophic denitrification.Electrolytic hydrogen production autotrophic denitrification is microorganism The autotrophic denitrification being reduced nitrogen oxides for electron donor with hydrogen, this kind of denitrifying bacterium is mainly microsphere denitrifying bacterium, needs Carry out under anoxia or anaerobic condition.Through coarse sands layer and the first gravel hypothalluses to O2Consumption after, the second gravel substrate Layer is substantially at scarce/anaerobic state, and anode can occur electrode reaction C+2H2O=CO2+4H++4e(E0=-0.207V), negative electrode There is electrode reaction 2H2O+2e=H2+2OH-(E0=0V), electrode reaction provides electron donor and inorganic carbon source respectively as certainly The denitrifying foster source of foster microorganism.Second gravel hypothalluses mainly occur to produce H2, produce CO2Autotrophic denitrification react realizing taking off Nitrogen, Fe2+Dissolution is secondary reaction, can accelerate electron transmission in microbial cell, therefore this hypothallus MFe:MCSuitably reduce (ferrum Charcoal mass ratio is MFe:MC=0.5:1~2:1).
The grain size of gravel of described gravel hypothalluses is 4~8mm, and the doping ratio of described ferrum charcoal is gravel hypothalluses gross mass 0.5%~3%.
Fe2+And Fe3+It is important electron transport system in microbial life activity, produce during Fe-C method Fe2+And Fe3+This electron transmission being participated in, thus accelerating the electron transmission efficiency in cell, improving microbial activity.
It is respectively equipped with 13,/14 two online ORP electrodes, difficult fall in the middle part of first gravel hypothalluses 6 and the second gravel hypothalluses 7 Solution Organic substance needs to be degraded to small organic molecule under preferable oxidizing condition, and Denitrification needs in anaerobic condition Lower could occur, ORP be directly reflection environmental oxidation reduce situation index.The present invention arranges online ORP and is intended to research interpolation The improvement situation to wet land system redox environment for the ferrum charcoal.
Described gathering ground 10 top is provided with perforation water collection sheet 9, and described perforation water collection sheet 9 open pore size is 5mm, and percent opening is 8.25%, gathering ground 10 bottom is provided with the gradient and is 5% and is in funnelform slope, described slope center is provided with slag-drip opening 11, this Outward, gathering ground 10 bottom is provided with support column.
Fe-C method, autotrophic denitrification are introduced artificial swamp by the present invention, by wetland device plant absorption, microorganism The materializations such as degraded, the absorption and precipitation and bio combined effect realization efficient denitrification to tail water, the depth jointly completing tail water is net Change.
Present configuration is simple, process stabilizing, with low cost, can bear certain pollutional load and hydraulic load punching Hit, can effectively purify sewage treatment plant tail water, particularly improve denitrification efficiency of constructed wetland, ensureing that sewage treatment plant goes out On the basis of water is up to standard, reduces sewage disposal plant effluent pollutant levels further, be conducive to the lasting improvement of water environment.
Embodiment 2
Most sewage treatment plant tail water B/C values are about 0.02~0.10, B/C=0.05 in the present embodiment, using embodiment 1 Device, through different proportion ferrum charcoal effect after, tail water biodegradability improve situation as shown in table 1:
The biodegradability of tail water after the effect of table 1 different proportion ferrum charcoal
Experimental example sequence number 1 2 3 4 5 6
MFe/MC 0.5:1 2:1 4:1 5:1 6:1 8:1
B/C 0.08 0.17 0.23 0.27 0.20 0.14
Table 1 shows, after the effect of ferrum charcoal, tail water B/C value significantly improves, and biodegradability is obviously improved.Ferrum charcoal mass ratio is MFe: MC=4:1~6:When 1, after effect, B/C value, up to more than 0.2, is preferably M from improving tail water angle iron carbon ratio exampleFe:MC=5:1.
Second gravel hypothalluses Fe-C micro electrolysis are secondary reactions, and iron carbon ratio example is too high, can be competing with autotrophic denitrification generation Strive (C+2H2O=CO2+4H++4e(E0=-0.207V), Fe-2e=Fe2+(E0=-0.44V)), should be using relatively low ferrum charcoal Mass ratio, ferrum charcoal mass ratio is MFe:MC=0.5:1~2:1 is more suitable, and 1:1 is should in finished iron Carbon composites on market With most widely low iron carbon ratio product, therefore preferably ferrum charcoal II ferrum charcoal mass ratio is MFe:MC=1:1.
Embodiment 3
Artificial swamp adopts cylindrical structure, internal diameter 20cm, high 65cm;Device is sequentially provided with vegetable layer 4, thick from top to bottom Layer of sand 5, the first gravel hypothalluses 6, the second gravel hypothalluses 7, supporting layer 8 and gathering ground 10.Set in the middle part of first gravel hypothalluses There is the online ORP electrode 14 of the first gravel hypothalluses, in the middle part of the second gravel hypothalluses 7, be provided with the second gravel hypothalluses online ORP electricity Pole 13, described gathering ground 10 top is provided with perforation water collection sheet 9, and it is 5% and in funnelform oblique that gathering ground 10 bottom is provided with the gradient Slope, described slope center is provided with slag-drip opening 11, and bottom is provided with support column 17.Additionally, described constructed wetland device top be provided with into The mouth of a river, bottom is provided with outlet.In first gravel hypothalluses 6, Uniform Doped ferrum charcoal mass ratio is MFe:MC=5:1 ferrum charcoal I 15, In second gravel hypothalluses 7, Uniform Doped mass ratio is 1:1 ferrum charcoal II 16, wherein, described ferrum charcoal I, II be diameter 10~ The bulk of 30mm.
In order to draw the preferred proportion of the doping of ferrum charcoal in gravel hypothalluses, the present invention is doped with that to account for gravel hypothalluses total respectively The ferrum charcoal of the different proportion of quality is to obtain preference data.It is doped with gravel substrate respectively in each gravel hypothallus of experimental example 9 The ferrum charcoal I, II of layer gross mass 0.5%, is doped with gravel hypothalluses gross mass 1% in each gravel hypothallus of experimental example 10 respectively Ferrum charcoal I, II, be doped with the ferrum charcoal I, II of gravel hypothalluses gross mass 3% in each gravel hypothallus in experimental example 11 respectively.
As a comparison, also added experimental example 7 and experimental example 8 in the present embodiment, each gravel substrate in described experimental example 7 Equal undoped p ferrum charcoal in layer, distinguishes Uniform Doped gravel hypothalluses gross mass 1% in each gravel hypothallus in experimental example 8 Ferrum, other experiment parameters are identical with experimental example 9-11.
Additionally, Performance of Constructed Wetlands Substrates coarse sands layer coarse sand particle diameter is 2~4mm, thickness is 5cm;First, second gravel hypothalluses Grain size of gravel be 4~8mm, thickness is 20cm;The grain size of gravel of supporting layer is 8~16mm, and thickness is 5cm;Vegetable layer From phragmites communiss, the planting density of phragmites communiss is 20 plants/m2.During test, hydraulic detention time is 2d, and artificial swamp is intake as sewage Process plant tail water, in tail water, pollutant levels are respectively COD 52.16~62.43mg/L, TN 14.77~19.83mg/L.? Obtain following experimental data eventually.
Experimental example 7-11 ferrum charcoal doping situation is as shown in table 2, pollutants removal rate efficiency, microbial activity and wet land system ORP is as shown in table 3.
Table 2 wetland ferrum charcoal doping situation
Experimental example sequence number 7 8 9 10 11
First gravel hypothalluses No 1% ferrum 0.5% ferrum charcoal I 1% ferrum charcoal I 3% ferrum charcoal I
Second gravel hypothalluses No 1% ferrum 0.5% ferrum charcoal II 1% ferrum charcoal II 3% ferrum charcoal II
Table 3 wetland COD, TN average removal rate and microbial activity comparison
* note:Microbial activity adopts fluorescence developing method to characterize.
According to table 3, experimental example 8-11 whole year COD average removal rate exceeds 0.92% respectively than experimental example 7, 5.09%th, 10.16%, 11.64%, winter (- 2 months December) exceeds 1.14% than experimental example 7 respectively, 6.15%, 11.22%, 14.16%, show to add the removal that ferrum charcoal contributes to COD in tail water, but individually add ferrum and almost there is no effect.Experimental example 8-11 Annual TN average removal rate exceeds 4.74%, 8.36%, 13.72%, 14.34% respectively than experimental example 7, winter (- 2 months December) Exceed 5.52%, 6.71%, 16.17%, 17.75% than experimental example 7 respectively, show that individually adding ferrum can improve artificial swamp pair The clearance of TN, and add ferrum Carbon composites formation galvanic element lifting effect and become apparent from, and winter effect is more significantly.Pass through It is located at the ORP on-line computing model in the middle part of the first gravel hypothalluses and in the middle part of the second gravel hypothalluses respectively to find, experimental example 7-11 First gravel hypothalluses, the second gravel hypothalluses all can be in good aerobic, anaerobic environment.Sampled by substrate, using glimmering Light development process detects Wetland Substrate microbial activity, finds that experimental example 8-11 microbial activity is far above experimental example 7, shows to add Ferrum charcoal and ferrum, all can improve microbial activity of artificial wetland, and after interpolation ferrum charcoal or ferrum, winter microbial activity reaches as high as not 2.3 times adding.With the raising of ferrum charcoal doping ratio, COD, TN clearance and microbial activity are all in rising trend, but mix Miscellaneous ratio, to after 1%, continues to improve doping ratio, and lifting amplitude less, simultaneously takes account of Cost Problems, doping ratio is preferably 1%.
Embodiment 4
Because tail water electrical conductivity is not very high, and tail water pH is usually closer to 7, and chemical dissolution is less, so ferrum in substrate Charcoal consumes relatively slowly, continuously available.During plant running 18 months, in ferrum charcoal, iron ion stably continues dissolution, and does not have Find obvious clogging, the ferrum charcoal of 0.5%-1% can be supplemented after plant running 2-3.
The above be only the preferred embodiment of the present invention it should be pointed out that:Embodiments of the present invention are not subject to above-mentioned The restriction of embodiment, under the premise without departing from the principles of the invention, the modification made under any present principles, replacement, combination, all should For equivalent substitute mode, it is included within protection scope of the present invention.

Claims (10)

1. a kind of constructed wetland device for sewage treatment plant tail water advanced nitrogen it is characterised in that:Described at sewage The constructed wetland device of reason plant tail water advanced nitrogen is followed successively by vegetable layer (4), coarse sands layer (5), the first gravel substrate from top to bottom Layer (6), the second gravel hypothalluses (7), supporting layer (8) and gathering ground (10);
It is provided with the online ORP electrode of the first gravel hypothalluses (14) in the middle part of described first gravel hypothalluses (6);
It is provided with the online ORP electrode of the second gravel hypothalluses (13) in the middle part of described second gravel hypothalluses (7);
Described gathering ground (10) top is provided with perforation water collection sheet (9), and gathering ground (10) bottom is provided with the gradient and is 5% and is in funnel-form Slope, described slope center is provided with slag-drip opening (11), additionally, gathering ground (10) bottom is provided with support column (17);
The described constructed wetland device top for sewage treatment plant tail water advanced nitrogen is provided with water inlet, and bottom is provided with water outlet Mouthful;
Described first gravel hypothalluses (6) Uniform Doped ferrum charcoal I (15), ferrum charcoal mass ratio M in described ferrum charcoal I (15)Fe:MC=2: 1~6:1;
Described second gravel hypothalluses (7) Uniform Doped ferrum charcoal II (16), ferrum charcoal mass ratio M in described ferrum charcoal II (16)Fe:MC= 0.5:1~2:1.
2. the constructed wetland device for sewage treatment plant tail water advanced nitrogen according to claim 1 it is characterised in that: Described ferrum charcoal I (15) is the bulk of diameter 10~30mm, and in ferrum charcoal, ferrum charcoal mass ratio is preferably MFe:MC=5:1.
3. the constructed wetland device for sewage treatment plant tail water advanced nitrogen according to claim 1 it is characterised in that: Described ferrum charcoal II (16) is the bulk of diameter 10~30mm, and in ferrum charcoal, ferrum charcoal mass ratio is preferably MFe:MC=1:1.
4. the constructed wetland device for sewage treatment plant tail water advanced nitrogen according to claim 1 it is characterised in that: The coarse sand particle diameter of described coarse sands layer (5) is 2~4mm.
5. the constructed wetland device for sewage treatment plant tail water advanced nitrogen according to claim 1,2 or 3, its feature It is:The grain size of gravel of described gravel hypothalluses is 4~8mm, and the doping ratio of described ferrum charcoal is gravel hypothalluses gross mass 0.5%~3%.
6. the constructed wetland device for sewage treatment plant tail water advanced nitrogen according to claim 5 it is characterised in that: The doping ratio of described ferrum charcoal is preferably the 1% of gravel hypothalluses gross mass.
7. the constructed wetland device for sewage treatment plant tail water advanced nitrogen according to claim 1 it is characterised in that: Described supporting layer (8) is made up of gravel, and described grain size of gravel is 8~16mm.
8. the constructed wetland device for sewage treatment plant tail water advanced nitrogen according to claim 1 it is characterised in that: Described perforation water collection sheet (9) open pore size is 5mm, and percent opening is 8.25%.
9. application in sewage treatment plant tail water advanced nitrogen for the constructed wetland device according to claim 1.
10. according to claim 9 application it is characterised in that:
1) tail water enters vegetable layer (4) from wetland device top, directly absorbs the nitrogen P elements in sewage using plant;
2) after carrying out initial absorption, tail water enters into coarse sands layer (5), removes oarse-grained float;
3) pretreated tail water enters the first gravel hypothalluses (6), is divided complicated larger molecular organicses by ferrum charcoal galvanic element Solve as small organic molecule;
4) tail water after processing enters the second gravel hypothalluses (7), through denitrifying bacterium heterotrophic denitrification and the anti-nitre of electrolytic hydrogen production Change effect carries out denitrogenation to tail water, and described denitrifying bacterium is microsphere denitrifying bacterium.
CN201611050608.0A 2016-11-24 2016-11-24 Constructed wetland device and application for sewage treatment plant tail water advanced nitrogen Active CN106430605B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201611050608.0A CN106430605B (en) 2016-11-24 2016-11-24 Constructed wetland device and application for sewage treatment plant tail water advanced nitrogen

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201611050608.0A CN106430605B (en) 2016-11-24 2016-11-24 Constructed wetland device and application for sewage treatment plant tail water advanced nitrogen

Publications (2)

Publication Number Publication Date
CN106430605A true CN106430605A (en) 2017-02-22
CN106430605B CN106430605B (en) 2019-08-06

Family

ID=58218875

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201611050608.0A Active CN106430605B (en) 2016-11-24 2016-11-24 Constructed wetland device and application for sewage treatment plant tail water advanced nitrogen

Country Status (1)

Country Link
CN (1) CN106430605B (en)

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107010728A (en) * 2017-06-05 2017-08-04 济南大学 A kind of gradual change type whole process autotrophic denitrification system and its processing method
CN107792946A (en) * 2017-12-05 2018-03-13 郑州大学 Solid shore spats component of vegetation type for micro- polluted river strengthened denitrification and preparation method thereof
CN107879477A (en) * 2017-10-31 2018-04-06 河海大学 Collapsible multistage Inner electrolysis drowned flow artificial wet land
CN107986567A (en) * 2017-12-12 2018-05-04 河海大学 A kind of Inner electrolysis denitrification Compound filter pool and its application
CN111039509A (en) * 2019-12-30 2020-04-21 河海大学 Subsurface flow constructed wetland system for sewage treatment and use method thereof
CN111792782A (en) * 2020-07-13 2020-10-20 中国科学院海洋研究所 Constructed wetland composite treatment system for intensively eliminating nitrogen in seawater culture tail water and use method thereof
CN113149233A (en) * 2021-04-16 2021-07-23 中国市政工程华北设计研究总院有限公司 Sewage treatment plant tail water wetland strengthening system and construction method thereof
CN114988638A (en) * 2022-05-30 2022-09-02 广州市环境保护工程设计院有限公司 Black and odorous water body treatment system
CN116715343A (en) * 2023-04-28 2023-09-08 中国科学院合肥物质科学研究院 Iron-carbon reinforced microbial fuel cell type wetland and application thereof
CN117509966A (en) * 2023-12-05 2024-02-06 西安工程大学 Ternary micro-electrolysis reinforced aeration vertical flow constructed wetland and construction method thereof
CN113149233B (en) * 2021-04-16 2024-05-31 中国市政工程华北设计研究总院有限公司 Sewage treatment plant tail water wetland strengthening system and construction method thereof

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1562823A (en) * 2004-04-08 2005-01-12 上海交通大学 Device of treating depth of sewage for processing layered objective pollutant
CN103183402A (en) * 2013-04-21 2013-07-03 北京工业大学 Reinforced nitrogen and phosphorus removal method suitable for reclaimed water with low carbon nitrogen ratio
CN203768122U (en) * 2014-01-22 2014-08-13 同济大学 Vertical flow-horizontal flow compound artificial wetland high-efficiency denitrification system
CN204752327U (en) * 2015-04-23 2015-11-11 复旦大学 A constructed wetland device for getting rid of oestradio in sewage treatment plant tail water
CN105217796A (en) * 2015-11-04 2016-01-06 中国科学院水生生物研究所 A kind of method of downward vertical artificial wetland coupling microorganism electrolysis cell strengthened denitrification and device
CN105859054A (en) * 2016-06-15 2016-08-17 句容苏米特环保科技有限公司 Device and method for electrochemically treating sewage with microorganisms and microbial film culture method

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1562823A (en) * 2004-04-08 2005-01-12 上海交通大学 Device of treating depth of sewage for processing layered objective pollutant
CN103183402A (en) * 2013-04-21 2013-07-03 北京工业大学 Reinforced nitrogen and phosphorus removal method suitable for reclaimed water with low carbon nitrogen ratio
CN203768122U (en) * 2014-01-22 2014-08-13 同济大学 Vertical flow-horizontal flow compound artificial wetland high-efficiency denitrification system
CN204752327U (en) * 2015-04-23 2015-11-11 复旦大学 A constructed wetland device for getting rid of oestradio in sewage treatment plant tail water
CN105217796A (en) * 2015-11-04 2016-01-06 中国科学院水生生物研究所 A kind of method of downward vertical artificial wetland coupling microorganism electrolysis cell strengthened denitrification and device
CN105859054A (en) * 2016-06-15 2016-08-17 句容苏米特环保科技有限公司 Device and method for electrochemically treating sewage with microorganisms and microbial film culture method

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
E. ASUMAN KORKUSUZ ET AL.: "Comparison of the treatment performances of blast furnace slag-based and gravel-based vertical flow wetlands operated identically for domestic wastewater treatment in Turkey", 《ECOLOGICAL ENGINEERING》 *
M. MARTÍN ET AL.: "Phosphorus and nitrogen removal from tertiary treated urban wastewater s by a vertical flow constructed wetland", 《ECOLOGICAL ENGINEERING》 *

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107010728B (en) * 2017-06-05 2022-08-23 济南大学 Gradual change type completely autotrophic nitrogen removal system and treatment method thereof
CN107010728A (en) * 2017-06-05 2017-08-04 济南大学 A kind of gradual change type whole process autotrophic denitrification system and its processing method
CN107879477A (en) * 2017-10-31 2018-04-06 河海大学 Collapsible multistage Inner electrolysis drowned flow artificial wet land
CN107792946A (en) * 2017-12-05 2018-03-13 郑州大学 Solid shore spats component of vegetation type for micro- polluted river strengthened denitrification and preparation method thereof
CN107986567A (en) * 2017-12-12 2018-05-04 河海大学 A kind of Inner electrolysis denitrification Compound filter pool and its application
CN111039509A (en) * 2019-12-30 2020-04-21 河海大学 Subsurface flow constructed wetland system for sewage treatment and use method thereof
CN111792782A (en) * 2020-07-13 2020-10-20 中国科学院海洋研究所 Constructed wetland composite treatment system for intensively eliminating nitrogen in seawater culture tail water and use method thereof
CN113149233A (en) * 2021-04-16 2021-07-23 中国市政工程华北设计研究总院有限公司 Sewage treatment plant tail water wetland strengthening system and construction method thereof
CN113149233B (en) * 2021-04-16 2024-05-31 中国市政工程华北设计研究总院有限公司 Sewage treatment plant tail water wetland strengthening system and construction method thereof
CN114988638A (en) * 2022-05-30 2022-09-02 广州市环境保护工程设计院有限公司 Black and odorous water body treatment system
CN116715343A (en) * 2023-04-28 2023-09-08 中国科学院合肥物质科学研究院 Iron-carbon reinforced microbial fuel cell type wetland and application thereof
CN117509966A (en) * 2023-12-05 2024-02-06 西安工程大学 Ternary micro-electrolysis reinforced aeration vertical flow constructed wetland and construction method thereof
CN117509966B (en) * 2023-12-05 2024-06-04 西安工程大学 Ternary micro-electrolysis reinforced aeration vertical flow constructed wetland and construction method thereof

Also Published As

Publication number Publication date
CN106430605B (en) 2019-08-06

Similar Documents

Publication Publication Date Title
CN106430605B (en) Constructed wetland device and application for sewage treatment plant tail water advanced nitrogen
Ren et al. Two-stage hybrid constructed wetland-microbial fuel cells for swine wastewater treatment and bioenergy generation
Liu et al. High degree of contaminant removal and evolution of microbial community in different electrolysis-integrated constructed wetland systems
CN103086508B (en) Microbial fuel cell wastewater treatment system for improving nitrogen removal effect
CN105152351A (en) Photoelectric artificial wetland and application thereof
CN101428938A (en) Treatment process for garbage leachate
CN105859054A (en) Device and method for electrochemically treating sewage with microorganisms and microbial film culture method
CN104787977A (en) Continuous flow integrated electrode bio-membrane reactor and nitrate removal technology
CN108658372A (en) Anammox couples the method that electro-oxidation processes processing landfill leachate realizes depth carbon and nitrogen removal
CN110395851B (en) High-altitude town sewage treatment method based on nitrogen and phosphorus capture and completely autotrophic nitrogen removal
CN105836894A (en) System and method for treating wastewater by coupling of tidal flow constructed wetlands and microbial fuel cells
CN206553350U (en) A kind of two-stage manual controlled infusion of intensified denitrification and dephosphorization
CN111825203A (en) Artificial wetland sewage treatment device integrating ammoniation, nitrification, denitrification and application thereof
CN110606626B (en) Synchronous nitrogen and phosphorus removal sewage treatment process
Lu Advanced treatment of aged landfill leachate through the combination of aged-refuse bioreactor and three-dimensional electrode electro-Fenton process
CN112174293A (en) Electric-enhanced bioretention system for removing low-concentration antibiotics
CN109626563A (en) A kind of domestic sewage in rural areas deep denitrification method
CN109502751A (en) A kind of green top partitioning type multistage AO integrated sewage disposal technique
CN115893655B (en) Method for performing microbial anaerobic ammonia oxidation denitrification by taking biochar as filler
Gao et al. High performance of nitrogen and phosphorus removal in an electrolysis-integrated biofilter
CN106430590A (en) Two-stage AO (Anoxic Oxic) device based treatment method for high-conductivity wastewater
Xie et al. An iron-carbon-activated carbon and zeolite composite filter, anaerobic-aerobic integrated denitrification device for nitrogen removal in low C/N ratio sewage
CN112093994B (en) CW-MFC device and method for reducing methane and ammonia nitrogen pollution
CN101973661B (en) Treatment method of processing wastewater of Chinese galls
CN213388232U (en) Electric-enhanced bioretention system for removing low-concentration antibiotics

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant