CN201999827U - High-efficiency stable sewage treatment device with bio-doubling process - Google Patents
High-efficiency stable sewage treatment device with bio-doubling process Download PDFInfo
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- CN201999827U CN201999827U CN2010202363844U CN201020236384U CN201999827U CN 201999827 U CN201999827 U CN 201999827U CN 2010202363844 U CN2010202363844 U CN 2010202363844U CN 201020236384 U CN201020236384 U CN 201020236384U CN 201999827 U CN201999827 U CN 201999827U
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Abstract
The utility model relates to an improvement for a water treatment device with bio-doubling process. The high-efficiency stable sewage treatment device with the bio-doubling process is characterized in that an aeration oxic zone is an annular trench, a water flow propelling device is arranged in the annular trench, a water inlet mixing reaction area, a water lifting area and a settling area are arranged on the inner side of the annular trench, and the annular trench is respectively communicated with the settling area and the water inlet mixing reaction area. The trench structure more effectively solves the contradiction of low dissolved oxygen and high sludge content required by the bio-doubling process and is capable of ensuring low dissolved oxygen and high sludge content required by the bio-doubling process, so that practical effect and advantages of the bio-doubling process are ensured. Two or more circulation flows are formed by treatment, so that overhaul for equipment is facilitated without stopping running and reflux ratio is adjustable and high, and a controllable gate or valve is additionally arranged between the lifting area and the annular trench so that adjustability of practical running is enhanced, an aerating device can be flexibly added, turned on or off according to the condition of treated water quality in construction or after construction, application expandability is fine and the device is high in process adaptability.
Description
Technical field
Utility model is the improvement to biological multiplication process water treatment device, relate in particular to a kind of change treating pond layout, can form the biological multiplication process waste disposal plant of efficient stable (the biological multiplication of the built-in Round Sump of annular ditch treatment unit) of two and above cycle of treatment.
Background technology
Biological multiplication process (Bio-dopp) is a kind of novel sewage treatment process of Germany's invention, it is with all single technology (biological nitration, denitrification, release phosphorus, inhale phosphorus, a plurality of unit such as oxidation operation, precipitation) being combined in an adjacent branch is separated with in the rectangle form pool of several different processing units, and (common 0.3～0.5mg/l) realizes vertical short distance nitration/denitrification denitrogenation, and (common 5～8g/l) guarantee highly-efficient treatment continual and steady (low dissolved oxygen and high sludge concentration are its technology two big characteristics) to high sludge concentration to adopt low dissolved axygen.Existing water technology has: simple to operate, high-efficiency biological denitrification and good phosphor-removing effect under the low dissolved oxygen, realize synchronously and short distance nitration/denitrification denitrogenation with the pond, operation is efficient, lasting, stable water outlet, low mud output, the few 40-60% of the comparable traditional technology of excess sludge, maintenance workload is little, and floor space is little, uses the rectangle pond to save a large amount of soils, sewage work only needs half area of common process sewage work, and reduced the pipeline reduced investment greatly, and investment is low with running cost, and investment, running cost roughly can reduce about half.Thereby in sewage disposal, obtain paying attention to and promoting.
Existing biological multiplication process, treating pond floor plan basic structure such as Fig. 1, in a rectangle form pool, adjacently be separated out aeration aerobic zone 3, air-lift unit district 2, water inlet mixing anaerobic reaction zone 1 (releasing the phosphorus district), the settling region 4 of built-in mud-water separation filler 8 and scraping/suction dredger 9.Treating water enters into water mixing anaerobic reaction zone 1, with the former mud mixture diluted mixture that obtains preliminary treatment, and carry out anaerobic phosphorus release within it and handle, enter gas by the bottom connection then and carry district 2, enter the aeration aerobic zone 3 that is provided with aeration flexible pipe by the air-lift device lifting, carry out aerobic treatment at the aeration aerobic zone, 4 enter into water mixing anaerobic reaction zone through the settling region again, form single cycle of treatment.The settling tank sludge part is communicated with water inlet mixing anaerobic reaction zone by the bottom and replenishes, and all the other are by scraping/the suction dredger discharge.Yet in actual engineering operation, because the defective on the layout of art breading pond, make actual motion be difficult to meet the requirements of low dissolved oxygen (for example 0.3～0.5mg/l), high reactivity mud (perfect conditions of 5～8g/l) operations for example, thereby actual engineering operation is difficult to reach design effect, reason:
In handling single circulation, muddy water mixes and the main water power that relies on bottom aeration flexible pipe and gas to propose generation that flows, low dissolved axygen aeration and high sludge concentration contradiction are difficult to coordinate, for example satisfy low dissolved axygen, aeration generation power is low, and sludge settling very easily takes place high-content mud, not only causes the operation sludge concentration to reduce, influence treatment effect, and sludge settling also influence the bottom aerator normally move; For preventing sludge settling, strengthen aeration rate, not only excessive but also be difficult to realize the short distance nitration/denitrification of highly-efficient treatment because of dissolved oxygen, dissolved oxygen reaches about 2mg/l usually in the actual engineering, cause short distance nitration/denitrification effect not reach design requirements, cause nitric efficiency not high, it is not up to standard to occur water outlet nitrogen easily.Secondly, muddy water mixed cycle mobilization force mainly relies on gas to put forward the liquid level difference of formation, and the relatively low treating water in addition of flow velocity cycling stream distance is longer, has also limited the sludge concentration raising, is difficult to the high sludge concentration that realizes that biological multiplication requires.Sludge concentration reduces influences short distance nitration/denitrification again conversely; only depend on gas to carry simultaneously and produce the circulation power that liquid level difference provides; and circulation fluid passes through settling tank; cause the mixed solution internal circulating load little; the reflux ratio adjustability is poor; the anti-load impact and the rain impact capacity of exposing to the sun are poor, for example during unusual or heavy rain, can not keep stable sludge activity and concentration at influent quality.Besides, the settling region is adjacent with the aeration aerobic zone to be arranged in juxtaposition, and the circulation overcurrent is born in the settling region, not only be difficult to guarantee the clarification current static state that requires, influence clarifying effect, and occur sludge settling in the mobile muddy water of circulation dead angle generation easily, also cause sludge concentration reduction in the circular current sewage water; Increase at chance heavy rain flooding quantity suddenly, cause big flow water inlet to cause sludge loss again easily, the circulation sludge concentration reduces after causing rain equally, carries if close to hold one's breath, though can reduce sludge loss, mud upgrades circulation but can cause for want of, make that to keep the microbial metabolism desired nutritional not enough, cause microbial metabolism under-nutrition and produce microorganism and do not have nutrition source " hungry dead ", cause rain after system recovery time longer, influence normal water outlet, therefore uprising rain impact capacity is poor.In addition, this pond type processing unit layout, the treating processes mud mixture has only a kind of circulation, and each pond is series operation, forms the single circulation of sealing, and the maintenance of any like this pond all influences the operation in other ponds.The defective that aforementioned because treating pond structure is brought has a strong impact on biological multiplication process and should have superiority and treatment effect, causes actual engineering operation to be difficult to reach design effect, has limited the performance of biological multiplication process advantage.
Besides, low dissolved oxygen in the biological multiplication process for the lower waste water of ammonia-nitrogen content, can be handled up to standard and saves energy consumption, but when disposing of sewage ammonia nitrogen (NH
3-N) concentration is higher, (NH such as leather-making waste water, alcohol waste water for example
3-N 〉=100mg/l), low dissolved axygen can cause the not enough complete oxidation that is difficult to realize nitrogen nitrogen of aerobic zone oxygen supply, influences the removal effect of ammonia nitrogen, has therefore limited its application in high ammonia-nitrogen wastewater, causes the limitation of technology.
Still with typical biological multiplication, its above-mentioned shortcoming of being brought by pool-type structure is not still overcome for Chinese patent CN101602541 bio sewage treating process and device, its treating pond type.
Above-mentioned deficiency still has is worth improved place.
The utility model content
The utility model purpose is to overcome above-mentioned the deficiencies in the prior art, provide a kind of and can guarantee that not only short distance nitration/denitrification requirement hangs down dissolved oxygen, and not sedimentation of high sludge concentration, and treating processes can form two and above circulation, can give full play to the biological multiplication process waste disposal plant of efficient stable of biological multiplication process advantage.
Another purpose of utility model is to provide a kind of technology adjustability good, can be applied to the biological multiplication process waste disposal plant of efficient stable of various wastewater.
The utility model purpose realizes, the main improvement is that aeration aerobic zone in the protista multiplication process is designed to annular ditch, the plug-flow device that forms circulation is set in the annular ditch, lifting zone, water inlet hybrid reaction district and the settling region of adjacent setting are moved to the annular ditch inboard, and the corresponding function district is communicated with, form at least two circulation by annular ditch, thereby overcome the deficiency that existing biological multiplication process treating pond layout is brought, realize the utility model purpose.Specifically, the biological multiplication process waste disposal plant of utility model efficient stable, comprise the water inlet hybrid reaction district, water lifting zone, aeration aerobic zone and the settling region that are communicated with by biology multiplication treatment scheme water, it is characterized in that the aeration aerobic zone is an annular ditch, the current puopulsion unit is arranged in the annular ditch, water inlet hybrid reaction district, water lifting zone, built-in annular ditch inboard, settling region, annular ditch are communicated with settling region and water inlet hybrid reaction district respectively.
The utility model device is handled basic procedure, and is roughly the same with the biological multiplication of prior art sewage treatment process:
Handle water inlet, at first enter into water hybrid reaction district, the water quality treatment situation is looked in water inlet hybrid reaction district, can be set at anoxic condition or anaerobic state respectively by the quantity of reflux that adjusting enters, and carries out biological denitrificaion or biological phosphate-eliminating respectively; Dispose of sewage through biological denitrificaion or biological phosphate-eliminating and to enter lifting zone by connected entrance or pipe, enter aerobic annular ditch by the lifting gear lifting, under promoting, the current puopulsion unit in annular ditch, forms circulation, and by annular ditch to other processing unit water distribution: for example a part is mixed muddy water and is entered the settling region by pool wall perforate or communicating pipe in the annular ditch, carry out mud-water separation, clarification and effluent is collected by the top effluent weir and is discharged; A part is mixed muddy water and is flowed through pool wall perforate etc. according to annular ditch and enter into water hybrid reaction district circulation (abbreviation partial circulating), a part is mixed muddy water circulation (abbreviation systemic circulation) in annular ditch, form at least two cycle of treatment thereby making disposes of sewage, internal circulating load is looked sewage quality and is regulated.The settling tank precipitating sludge, part is back to into water hybrid reaction district with high sludge concentration in keeping handling by pool wall perforate etc., and rest part is discharged as unnecessary mud.Owing in annular ditch, increase the plug-flow device, thereby strengthened mixing muddy water flow velocity in annular ditch, can guarantee the little aeration rate under the low dissolved oxygen of biological multiplication process requirement, not sedimentation of high sludge content (mixed soil water flows and mainly relies on plug-flow device plug-flow), both can guarantee short distance nitration/denitrifying carrying out, keep high sludge content again, can guarantee biological multiplication process advantage performance.Each pool volume calculates by water quality and art breading requirement to be determined.
In the utility model:
The aerobic annular ditch of aeration, the one, as aerobic reactor zone, under low dissolved oxygen, realize vertical short distance nitration/denitrification denitrogenation as existing biological doubling technology, and the biological removal organism, the 2nd, form processing mixing muddy water different rings stream the water distribution passage is provided, form at least two and handle circulation.By this function, annular ditch, ditch shape for example can be the rectangle ditch, it also can be the two ends arc ditch of similar oxidation ditch, mix for prolonging muddy water circulation time in aerobic ditch, and can satisfy the requirement of the circulation residence time in short plot, annular ditch can also be designed to fit two ditches or more than.Oxygenate apparatus in the annular ditch, substantially roughly the same biological multiplication process, mainly based on end aeration apparatus of oxygen supply oxygen supply, for example can be water treatment with various micro-hole aerators, efflux aerator, stream aerating apparatus etc. looses, be good with micro-hole aerator especially wherein, it produces, and bubble is tiny, specific surface area is big, and upflow velocity is slow, the easier oxygen that obtains of microorganism, and can improve the oxygen transfer efficiency.In addition, according to treating water water quality situation, for example too high or too low wastewater treatment of ammonia nitrogen also can form based on surface aeration equipment or two kinds of oxygenation patterns of bottom aeration+surface aeration by increasing surface aeration equipment, improves dissolved oxygen in water.
Mixing muddy water mobile fast power that provides in annular ditch is provided current puopulsion unit in the annular ditch, guarantees long circulation circulation realization on the one hand, provides on the other hand and mixes the enough flow velocitys of muddy water, prevents that high concentration sludge from producing sludge settling because of hanging down flow velocity.Make and realize vertical short distance nitration/denitrification aeration oxygen supply, with mix muddy water plug-flow power and separate, thereby can guarantee for realizing the required low dissolved oxygen of short distance nitration/denitrification, and can keep the high sludge concentration of circulation fluid, thereby better coordinated high sludge concentration of biological multiplication process and low dissolved oxygen contradiction, it is unified to make both reach processing requirement.The current puopulsion unit, because its major function provides the mobile plug-flow power of mixed soil water, in theory thruster can not limited, it for example can be the vane type thruster, also can be oxidation ditch with rotating disk or change brush, and ejector, suction penetrate device etc., all can be employed as long as can promote the power of flow, transition oxygenation destroys low dissolved oxygen, a kind of employing underwater propeller that is preferably in the plug-flow in order to avoid.From forming the plug-flow function, puopulsion unit can design the optional position at annular ditch, and wherein a kind of better being arranged on is lifted out near the pool, can utilize simultaneously to promote waterhead increase plug-flow, to reduce plug-flow power.Look treating water design annular ditch circulation length, the current puopulsion unit can be a place, also can be two or more on flow path.In systemic circulation, do not hold because of flow velocity reduces for preventing circulation, cause sludge settling, current puopulsion unit plug-flow, can be designed to the gap way traffic, for example adopt the positive and negative running of turntable clearance, circulation alternately can effectively prevent from not hold end to end because of flow velocity reduces and cause sludge settling like this.
Lifting gear, major function will promote from water inlet hybrid reaction district's mixing muddy water and enter the exterior annular ditch with biological multiplication process, form and upgrade circulation.Lifting gear can be a pump, also can be air-lift device, and perhaps other have the water lift functional device, and for example perforate on lifting zone and annular ditch pool wall is provided with thruster, and wherein a kind of employing air-lift unit that is preferably, gas carry that to have energy consumption low, energy-conservation.Lifting zone can be arranged in parallel with water inlet hybrid reaction district, also can be to be arranged vertically.
Water inlet hybrid reaction district, be that into water is handled the first step, except that bearing into the water mixing functions, according to the influent quality situation, can enter inhalant region quantity of reflux size by adjusting respectively, be set to anoxic condition or anaerobic state, realize that respectively biological denitrificaion is that main operational mode or biological phosphate-eliminating are main operational mode, realization is based on biological denitrificaion, or is main two kinds of processing capacities with the biological phosphate-eliminating, thereby can be described as anaerobic zone or oxygen-starved area again.
In addition:
In order to improve streamflow regime in the water inlet hybrid reaction district, prevent that high sludge concentration from producing sludge settling, and accelerate water inlet and mix, better be provided with in the inhalant region and quicken to mix the wake turbulence device, for example waterpower such as vane wheel propeller, agitator is mixed, thruster, mixes ability and velocity of flow to improve sewage.
The settling region for realizing clarification fast and improving clarifying effect, can be provided with in settling tank and quicken mud-water separation precipitation filling, for example swash plate or inclined tube mud-water separation filler with biological multiplication process.Swash plate or inclined tube can adopt the tilting mode of tilting for example 60 degree of straight channel, also can adopt the vertical mounting means of vertical crooked ripple swash plate; Bottom settlings mud, a part are by bottom opening or connection, and the district replenishes active sludge to the water inlet hybrid reaction, keeps the sludge content requirement, and a part is discharged from settling tank.Discharging settling tank can be by being arranged on scraping/the mud-sucking device discharge of settling region, perhaps by being fixedly mounted on the settling region or discharging near the suction pump of settling region.According to settling tank shape structure, it is scraped and/or mud-sucking device, can adopt reciprocating typely, or rotary, only needs in accelerate precipitation mud-water separation filler both sides or the center is reserved and driven the space.
In order to strengthen the technology controllability in the pond of finalizing the design, improve adaptability, and further save operation energy consumption disposing of sewage, be provided with on a kind of lifting zone more fortunately and the annular ditch common wall and be communicated with the controlled gate of flow or valve or plug-flow device.In service: it is lower for example to work as the water inlet Pollutant levels, in the time of can reaching processing requirements by less circular flow, can stop or reducing lifting gear promotes, the plug-flow device of starting gate or valve or pool wall face, replenish water inlet to annular ditch, can save the lifting energy consumption like this, in more energy-conservation operation down.Enter annular ditch " ultromotivity " for improving gravity flow, advance the current puopulsion unit of circulation in the annular ditch, better be arranged on the mobile direction front end of controllable gate or valve or plug-flow device water,, strengthen gravity flow " power " and reach from flow by " suction function " that the plug-flow device forms.
In order to improve to high NH
3-N (NH for example
3The leather of-N 〉=100mg/l, alcohol) nitrogen of waste water removes ability, can for example make dissolved oxygen to 2 mg/l by increasing the dissolved oxygen content that aeration improve aerobic ditch.Improving the dissolved oxygen mode, can be to strengthen the end air demand of exposing to the sun, the perhaps increase table device that exposes to the sun again, for example rotating disk, change oxygenate apparatus such as brush, the employing table oxygen supply of exposing to the sun separately.
The biological multiplication process waste disposal plant of utility model efficient stable, with respect to existing biological multiplication process pond type, owing to changed pond type arrangement, change the aeration aerobic zone into annular ditch, and the current puopulsion unit that advances circulation is set in annular ditch, other processing capacity districts are built in the inboard adjacent setting of annular ditch circle.Thereby brought following variation:
At first, changed processing mixed solution circulation form and improved circulation velocity, made processing mix muddy water and formed water inlet hybrid reaction district-lifting zone-aerobic annular ditch-water inlet hybrid reaction district partial circulating; With systemic circulation in the aerobic annular ditch; And also has aerobic annular ditch-settling region water exit (precipitated outlet water is separated with cycle of treatment), when make needing the wherein a certain unit equipment of maintenance like this, can be not out of service because of not realizing that cycle of treatment causes, the while partial circulating, obtained the lower concentration circulation mixed solution handled to water inlet carry out greatly than doubly dilution (circular flow can be as required for flooding quantity tens in addition thousands of times), making into, the water Pollutant levels are reduced rapidly, making into, water significantly reduces in water inlet hybrid reaction district pond internal contamination substrate concentration difference, more effective water inlet high concentration of COD of having avoided causes impact to active sludge, stablize the microorganism growth environment, thereby improved capacity of resisting impact load; Systemic circulation in the aerobic ditch has increased sewage waterpower flow process and residence time (good oxygen is lengthened out) in aerobic annular ditch, has not only strengthened COD, BOD, NH
3-N, the particularly removal of total nitrogen, and since circulation fluid in pollutent along with water circulation, by microorganism pollution degradation substrate concentration reduction gradually, having formed oxyty at the circulation end improves relatively, nitrate nitrogen content increases, thereby strengthened denitrification functions, and the waste water of organic wastewater with difficult degradation thereby and biochemical difference there is treatment effect preferably, particularly annular ditch is designed to fit two ditches or more than, prolong the mixed soil water circulation time especially, and do not held the high section of dissolved oxygen flow process, improved sewage treatment capacity, can guarantee water outlet total nitrogen stably reaching standard, this design has simultaneously also improved the adaptability to short and small plot.High circulation flow velocity has been guaranteed under low aeration dissolved oxygen (dissolved oxygen minimum can at 0.1mg/l), and high sludge content (for example sludge concentration 8g/l) sludge settling can not take place yet, and has better solved low dissolved oxygen of biological multiplication process requirement and high sludge content contradiction; In addition, thruster produces high flow velocity also makes the muddy water mixing reach and the quickening of oxygen contact mass transfer, can guarantee biological multiplication process advantage performance; Strengthen plug-flow and can also further improve sludge concentration.In addition, this ditch shape design and increase plug-flow device have also improved reflux ratio, and the adjustability of reflux ratio, can be according to the situation of disposing of sewage, and the flexible reflux ratio; Big reflux ratio has kept high sludge concentration again, and high sludge concentration can be guaranteed the low dissolved oxygen of vertical short distance nitration/denitrification, and short distance nitration/denitrification is effective, and both fine coordinations are that this patent is different from the maximum difference that existing biological multiplication pond type is arranged.
Secondly, the settling region places in the annular ditch, only playing the mud-water separation clarification uses, and there is not original circulation overcurrent function, not only can guarantee to clarify desired current static state, help fast clarification and high clarifying effect, even acceleration mud-water separation precipitation filling is not set, also can fine realization precipitate and separate; And overcome prior art settling region overcurrent and produce the dead angle and cause sludge settling, reduce circulation sludge concentration phenomenon.
Besides, set up controllable gate or valve between lifting zone and annular ditch, make in the low Pollutant levels of rain or water inlet of exposing to the sun, can close lifting gear, rely on the connection of gate or valve to provide fresh mix liquid for circulation, keep certain replenishment cycles amount, thereby guarantee to keep the microbial metabolism desired nutritional, can avoid because of closing lifting, causing nothing to augment the mixed solution circulation causes microbial metabolism under-nutrition and causes microorganism not have nutrition source " hungry dead ", also save aeration energy consumption, realized more energy-saving run.Can make into when exposing to the sun rain simultaneously that water directly enters the settling region, directly discharge after clarifying, avoid causing the sludge loss phenomenon because of heavy rain causes big flow, improve the uprising rain impact capacity of technology, the system that is easy to replys and uses.Simultaneously, set up controllable gate or valve between lifting zone and annular ditch, also improved treatment unit according to the handiness of disposing of sewage and regulating.
The biological multiplication process waste disposal plant of utility model efficient stable, kept biological multiplication process operational conditions, and don't be same as existing biological multiplication pond type, the biological multiplication of the built-in Round Sump of its annular ditch treating pond type, guarantee biological multiplication process requirement---low dissolved oxygen, high sludge concentration, can realize more that in actual engineering this patent pond type dissolved oxygen can be controlled at 0.1～0.5mg/l, sludge concentration is actual can be brought up to 5～8g/l or higher (looking plug-flow) and sludge settling can not occur.Overcome the shortcoming that existing biological multiplication process processing unit layout is difficult to overcome, can more give full play to biological multiplication process treatment effect and advantage, and device technique adaptability is strong, can regulate total reflux ratio according to different treatment sewage and processing requirements, reach two and loop back flow, can realize biological multiplication process by efficient stable, and improve anti-shock loading and the anti-rain impact capacity of exposing to the sun, this is the maximum characteristics of utility model device.
On aerobic ditch, set up or substitute oxygenate apparatus such as aeration turn plate, commentaries on classics brush are set,, for example dissolved oxygen is increased to 2mg/l or higher, can improve high NH by strengthening the dissolved oxygen content of aerobic ditch
3-N (NH for example
3Waste water nitrogen such as the leather of-N 〉=100mg/l, alcohol are removed ability, have enlarged biological multiplication process range of application.And this device can be after building or building up, according to the water quality treatment situation, increasing aerating apparatus flexibly realizes, improved the handiness of Patent equipment especially, it is good to use expandability, has overcome the limitation that is difficult to extended functionality after existing biological multiplication process pond type layout is built up.
Below in conjunction with some specific embodiments; utility model essence is further understood in exemplary illustration and help; but the embodiment detail only is for utility model is described; do not represent utility model design whole technical schemes down; therefore should not be construed as the total technical scheme of utility model is limited; some are In the view of the technician; the unsubstantiality that does not depart from the utility model design increases and/or change; for example change or replace, all truely use novel protected scope so that technical characterictic with same or similar technique effect is simple.
Description of drawings
Fig. 1 is that the biological multiplication process base pool of prior art type is arranged synoptic diagram.
Fig. 2 is that the biological multiplication process waste disposal plant of utility model efficient stable base pool type is arranged synoptic diagram.
Fig. 3 is that the second embodiment pond type is arranged synoptic diagram.
Fig. 4 is that the 3rd embodiment pond type is arranged synoptic diagram.
Fig. 5 is that the 4th embodiment pond type is arranged synoptic diagram.
Fig. 6 is that the 5th embodiment pond type is arranged synoptic diagram.
Fig. 7 is that the 6th embodiment pond type is arranged synoptic diagram.
Fig. 8 is that a kind of pond of the 7th embodiment type is arranged synoptic diagram.
Fig. 9 is that the another kind of pond of the 7th embodiment type is arranged synoptic diagram.
Figure 10 is that another pond type of the 7th embodiment is arranged synoptic diagram.
Figure 11 is that a kind of pond of the 8th embodiment type is arranged synoptic diagram.
Figure 12 is that the another kind of pond of the 8th embodiment type is arranged synoptic diagram.
Wherein Fig. 3-12 all omits interior arrangement.
Embodiment
Dispose of sewage and at first enter into water hybrid reaction district 1, under thruster 6 effects, realize short mix with former mud mixture, finish into water and handle the mixed diluting of diluted mixture liquid, according to water quality treatment, enter quantity of reflux by adjusting and be set at anoxic condition or anaerobic state respectively, realize denitrogenation or phosphorus removal functional; Enter lifting zone 2 by the bottom communication passage, under promoting, air-lift device 7 enters aerobic annular ditch 3, form unidirectional circulation under current puopulsion unit 10 plug-flows: part mixing muddy water is by the pool wall perforate or enter settling region 4 communicating pipe, carries out mud-water separation, and clarification and effluent is discharged system; A part mix muddy water by aerobic annular ditch by the pool wall perforate or enter into that water hybrid reaction district 1 forms cycle of treatment (partial circulating) communicating pipe, a part is mixed muddy water circulation (systemic circulation) in annular ditch, realize short distance nitration/denitrification denitrogenation synchronously, and degradation of organic substances.According to the actual treatment situation, adjust the gas amount of putting forward respectively and enter settling tank, the water inlet hybrid reaction district water yield.Settling tank precipitating sludge, part are communicated with by the bottom and are back to into water hybrid reaction district, rest part as unnecessary mud by scrape/suction dredger discharges.Through experimental test: when flow velocity in the annular ditch reach 0.3m/s and more than, sludge concentration is not found the sludge settling phenomenon at 8g/l.
Pollutant load is lower when intaking, single-pass is crossed tap drain and is circulated in the time of can reaching processing requirements, can stop gas carrying, Open valve, keep the circulation of an amount of water inlet substitute, keep the required nutrition of microbial metabolism, be implemented in saving lifting energy consumption under the assurance processing requirements, and avoid causing the harm that microbial metabolism under-nutrition causes because of closing to promote to cause nothing to intake and substitute to circulate.
Under the heavy rain situation, flooding quantity strengthens, and concentration of wastewater reduces, but also temporarily shut lifting gear, and sewage directly enters the settling region and divides the directly discharge of dried up back through filler.Thereby avoided causing the sludge loss phenomenon, improved uprising rain impact capacity because of heavy rain causes big flow; Open valve is kept the circulation of an amount of water inlet substitute simultaneously, keeps the required nutrition of microbial metabolism, and the system that is easy to replys and uses.
Embodiment 3: referring to Fig. 4, as embodiment 2, annular ditch 3 changes oval racetrack into.
Embodiment 4: referring to Fig. 5, as embodiment 1, annular ditch 3 changes oval racetrack into, and lifting zone 2 is designed to semicircle, and settling region 4 is designed to circular settling tank, and reciprocating type scraping/suction dredger is replaced by to rotate and is scraped/suction dredger.
Embodiment 5: referring to Fig. 6, as embodiment 1, it is parallel with annular ditch 3 long faces that wherein gas is carried district 2.
Embodiment 6: referring to Fig. 7, as described above, wherein settling tank 4 is gentle carry district 2 and be set to respectively about 2.Both can move side by side simultaneously, also can be in maintenance 1 of isolated operation during equipment in it, thus not out of service when guaranteeing to overhaul.
Embodiment 7: referring to Fig. 8,9,10, as embodiment 6, the hybrid reaction of wherein intaking district 1 also is set to 2 arranged side by side, and both can move side by side simultaneously, also can be in maintenance 1 of isolated operation during equipment in it, thus not out of service when guaranteeing to overhaul.
Aforementioned water inlet hybrid reaction district, water lifting zone, settling region both can be provided with two separately, also can be provided with two simultaneously.
Embodiment 8: referring to Figure 11,12, as described above, annular ditch can be designed to two ditches or many ditches shrink-fit structure, two of current propeller design or more than.
In addition, when handling high ammonia-nitrogen wastewater, can also on aerobic annular ditch, increase oxygenate apparatus such as rotating disk, perhaps strengthen end aeration rate, perhaps the employing table device that exposes to the sun substitutes the end device that exposes to the sun, and improves oxygenation capacity, realization guarantees that to the processing of high ammonia-nitrogen wastewater water outlet is nitrogen discharged up to standard.
To those skilled in the art; under this patent design and specific embodiment enlightenment; some distortion that can directly derive or associate from this patent disclosure and general knowledge; those of ordinary skills will recognize also can adopt additive method; or the substituting of known technology commonly used in the prior art; and the mutual various combination between feature; the for example change of each process island shape; the change of current puopulsion unit in the annular ditch; for example adopt rotating disk, the change of aerating apparatus, hydraulic propeller changes suction flow type or stirring-type in the inhalant region; the positive and negative plug-flow in the gap of current puopulsion unit; or the like unsubstantiality change, can be employed equally, can both realize this patent representation function and effect; launch for example no longer one by one to describe in detail, all belong to this patent protection domain.
The utility model device according to handling the water yield, can be the prefabrication structure, also can on-the-spot structures.
Claims (14)
1. the biological multiplication process waste disposal plant of efficient stable, comprise the water inlet hybrid reaction district, water lifting zone, aeration aerobic zone and the settling region that are communicated with by biology multiplication treatment scheme water, it is characterized in that the aeration aerobic zone is an annular ditch, the current puopulsion unit is arranged in the annular ditch, water inlet hybrid reaction district, water lifting zone, built-in annular ditch inboard, settling region, annular ditch are communicated with settling region and water inlet hybrid reaction district respectively.
2. according to the biological multiplication process waste disposal plant of the described efficient stable of claim 1, it is characterized in that the aeration aerobic zone is by end aeration oxygen supply.
3. according to the biological multiplication process waste disposal plant of the described efficient stable of claim 2, it is characterized in that end aeration oxygen supply is a micro-hole aerator.
4. according to the biological multiplication process waste disposal plant of the described efficient stable of claim 1, at least one is arranged on and is lifted out near the pool to it is characterized in that the current puopulsion unit.
5. according to the biological multiplication process waste disposal plant of the described efficient stable of claim 1, it is characterized in that the water lifting gear is the air-lift unit air-lift device in the water lifting zone.
6. according to the biological multiplication process waste disposal plant of the described efficient stable of claim 1, it is characterized in that in the water hybrid reaction district mixing of acceleration wake turbulence device being arranged.
7. according to the biological multiplication process waste disposal plant of the described efficient stable of claim 1, it is characterized in that the accelerate precipitation separating filler is arranged in the settling region.
8. according to the biological multiplication process waste disposal plant of the described efficient stable of claim 1, it is characterized in that communicating aperture and controllable gate or valve are arranged on water lifting zone and the annular ditch common wall.
9. the biological multiplication process waste disposal plant of described according to Claim 8 efficient stable is characterized in that the current puopulsion unit is arranged on controllable gate or the mobile direction front end of valve water in the annular ditch.
10. according to the biological multiplication process waste disposal plant of the described efficient stable of claim 1, it is characterized in that rotating disk is arranged on the annular ditch, change brush.
11., it is characterized in that into water hybrid reaction district, water lifting zone, settling region are provided with two individually or simultaneously according to the biological multiplication process waste disposal plant of the described efficient stable of claim 1.
12., it is characterized in that connected entrance all has controllable gate between each treating pond according to the biological multiplication process waste disposal plant of the described efficient stable of claim 1.
13. according to the biological multiplication process waste disposal plant of the described efficient stable of arbitrary claim in the claim 1 to 12, it is characterized in that annular ditch have two of fits and more than.
14., it is characterized in that scraping in the settling region and/or inhaling the mud mud discharging device according to claim 1 or the biological multiplication process waste disposal plant of 7 described efficient stables.
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| CN2010202363844U CN201999827U (en) | 2010-06-22 | 2010-06-22 | High-efficiency stable sewage treatment device with bio-doubling process |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102180543A (en) * | 2010-06-22 | 2011-09-14 | 凌志环保有限公司 | Highly-efficient stable bio-doubling sewage treatment device |
| CN102795745A (en) * | 2012-08-18 | 2012-11-28 | 江苏凌志市政工程设计研究院有限公司 | Integrated multi-cycle biological multiplication sewage treatment system |
| CN106145533A (en) * | 2016-08-08 | 2016-11-23 | 哈尔滨北方环保工程有限公司 | A kind of plug-flow method of biological multiplication process system mixed liquor |
-
2010
- 2010-06-22 CN CN2010202363844U patent/CN201999827U/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102180543A (en) * | 2010-06-22 | 2011-09-14 | 凌志环保有限公司 | Highly-efficient stable bio-doubling sewage treatment device |
| CN102795745A (en) * | 2012-08-18 | 2012-11-28 | 江苏凌志市政工程设计研究院有限公司 | Integrated multi-cycle biological multiplication sewage treatment system |
| CN106145533A (en) * | 2016-08-08 | 2016-11-23 | 哈尔滨北方环保工程有限公司 | A kind of plug-flow method of biological multiplication process system mixed liquor |
| CN106145533B (en) * | 2016-08-08 | 2019-01-18 | 哈尔滨北方环保工程有限公司 | A kind of plug-flow method of biology multiplication process system mixed liquor |
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