CN205099555U - From clear aeration integrated constructed wetland sewage treatment system that declines - Google Patents
From clear aeration integrated constructed wetland sewage treatment system that declines Download PDFInfo
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- CN205099555U CN205099555U CN201520864486.3U CN201520864486U CN205099555U CN 205099555 U CN205099555 U CN 205099555U CN 201520864486 U CN201520864486 U CN 201520864486U CN 205099555 U CN205099555 U CN 205099555U
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Abstract
The utility model belongs to the technical field of sewage treatment, concretely relates to from clear aeration integrated constructed wetland sewage treatment system that declines. The utility model discloses the technical problem who solves is that traditional constructed wetland dissolved oxygen is on the low side, and area is great, and easy jam of packing is to high concentration sewage treatment effect subalternation problem. The utility model discloses sewage treatment system is including the pool is surveyd to include the preliminary treatment structures that are connected gradually by the pipeline, the vertical baffling wetland sewage treatment plant of aeration that declines clear certainly, ANAMMOX denitrogenation type side direction undercurrent constructed wetland sewage treatment plant and the biology of rivers intercommunication in proper order. The utility model discloses a sewage treatment system treatment effeciency is high, and the quality of water of adaptable difference changes, and the denitrogenation is effectual, and the constructed wetland of clear formula is difficult certainly blocks up, can carry out the back flush, goes out water stabilization of water quality, has ensured wetland system's operation steady in a long -term.
Description
Technical field
The utility model belongs to technical field of sewage, is specifically related to the micro-aeration composite artificial marsh sewage treatment system of self-cleaning type.
Background technology
Artificial swamp is the principle of purifying waste water according to natural bioremediation, by manually construction and supervision and control strengthen the sewage disposal technology of its detergent power.The composite system that it is made up of jointly the matrix of water-permeable, plant, water body, aerobic or anaerobion population and animal.Sewage is in artificial swamp after comprising the effect process such as biological degradation, filtration, precipitation and absorption, and the organic compound in sewage, suspended solids, some nitrogenous compounds, phosphorus and pathogenic bacteria are obtained for great reduction.
Treatment Technology of Constructed Wetland is that following water quality carries mark one big hot topic treatment technology, and it has the advantages such as reduced investment, efficiency is high, environmental benefit is good, in being applicable to very much, the sewage disposal of samll cities and towns.Traditional artificial swamp comprises surperficial flow pattern, undercurrent type and vertical flow pattern, but due to the restriction of construction itself, makes dissolved oxygen concentration on the low side, and floor space is comparatively large, and filler easily blocks.In traditional sewage disposal, aeration rate is generally gas-water ratio >3:1, and that have is even 10:1.And in the operation of Sewage Plant, the power consumption expense of aerator account for very most of, therefore, how can reduce gas-water ratio again when ensureing effluent quality, becoming the focus studied now.Investigating multiple operating artificial swamp in 2000 according to the U.S., there is blocking in various degree for 5 years afterwards coming into operation in the artificial wet land system finding that there is nearly 50%.Blocking not only can cause the reduction of wetland discharge capacity, thus cause large amount of sewage heap soil or fertilizer over and around the roots to be amassed at the surperficial also blocking oxygen of wetland to hypothallus internal diffusion, reduce wetland to the removal effect of pollutent, make effluent quality not reach standard, block the operation life that also can shorten artificial swamp in addition.Especially to vertical current constructed wetland, its blockage problem is comparatively serious.
The aggravation of nitrate pollution is also one of important factor causing the waters wawter blooms such as China lake, river and coastal waters and red tide large-scale outbreak in recent years, therefore, how to remove the extensive concern that nitrate pollution causes people.In recent years, along with the breakthrough of biological denitrificaion Theory and technology, the novel biological dinitrification technology being representative with ANAMMOX technique progresses into the people visual field.Compared with traditional biological denitride technology, ANAMMOX bacterium is chemoautotrophy type bacterium, and ANAMMOX reaction path is shorter, therefore ANAMMOX reaction does not need basicity compensate and add organic carbon source, only need to maintain lower dissolved oxygen, can realize as influent waste water C/N<3.4 or the denitrification reaction of high ammonia-nitrogen wastewater, thus save a large amount of energy and material, save running cost, there is the meaning of Sustainable development.ANAMMOX reaction is that microorganism is directly by NH
4 +-N and NO
2-N reaction is converted into N
2, reach the object of denitrogenation, wherein as the NO of electron acceptor(EA)
2 -generally be transformed by ammonia.
See that known artificial swamp such as CN102531187A " a kind of method for the treatment of domestic wastewater with combined laminated vertical flow-horizontal subsurface flow wetland ", CN203639245U " a kind of hybrid constructed wetland system ", CN103708621A " a kind of hybrid constructed wetland system and sewage water treatment method thereof " etc. mainly carry out transformation combination to the fluidised form of artificial swamp, filler, its filler easily blocks, be not suitable for the sewage processing higher concentration, floor space is larger.And in artificial swamp, back flushing is then had no report from clear technology, micro-aeration process and the artificial swamp that is applied to based on the lateral subsurface flow wetland technology simultaneity factor of ANAMMOX denitrogenation principle.
Utility model content
The technical problems to be solved in the utility model is that Traditional Man wetland dissolved oxygen is on the low side, and floor space is comparatively large, and filler easily blocks, to high-concentration sewage poor processing effect.
The technical solution of the utility model is as follows:
The self-cleaning type that the utility model proposes micro-aeration composite artificial marsh sewage treatment system comprises the pre-treatment structures of water communication successively, the vertical baffling wetland waste disposal plant of the micro-aeration of self-cleaning type, the side direction drowned flow artificial wet land waste disposal plant that can realize ANAMMOX denitrogenation and the biological observation pool; The component relationship of whole system each several part is as follows:
Pre-treatment structures are provided with system water inlet pipe;
The vertical baffling wetland waste disposal plant of the micro-aeration of self-cleaning type is made up of water distributing area, pond body and catchment area; Treatment sewage flows into water distributing area through water inlet pipe, then by the mode of overflow from inflow pond, water distributing area body, the water outlet after the body process of pond adopts the mode of overflow to flow into catchment area; Described pond body is that the vertical baffling wetland of multistage different processing functions is in series, anaerobism wetland, oxidation of coal wetland and short-cut nitrification-denitrification wetland is followed successively by along water (flow) direction, anaerobism wetland and oxidation of coal wetland respectively adopt a unit cells, and short-cut nitrification-denitrification wetland is made up of some unit cells; Anaerobism wetland is disposed with backwash tube and packing layer from bottom to top, oxidation of coal wetland and short-cut nitrification-denitrification wetland are disposed with backwash tube, micro-aeration tube, packing layer and waterplant from bottom to top, adopt the micro-aeration mode of classification, the gas-water ratio of total aeration rate is less than 2 ︰ 1, and the aeration rate controlling oxidation of coal wetland is greater than short-cut nitrification-denitrification wetland, make the wet dissolved oxygen of telluric water of oxidation of coal reach 1 ~ 2mg/L, the dissolved oxygen in short-cut nitrification-denitrification wetland water reaches 0.5mg/L;
The side direction drowned flow artificial wet land waste disposal plant that can realize ANAMMOX denitrogenation is made up of natural reaeration groove, lateral subsurface flow wetland bed, one of them natural reaeration groove connects a lateral subsurface flow wetland bed and forms one group of unit cells, and the series connection of many group unit cells forms described wet field facilities for treating sewage downwards jointly along gradient; Described natural reaeration groove is for falling the formula of jumping thin water layer natural reaeration groove; Described lateral subsurface flow wetland bed comprises wetland bed body, water distributor, header, filler, wetland plant and the settling containing ANAMMOX bacterium; Water distributor and header are all arranged on bottom lateral subsurface flow wetland bed, are arranged in feed-water end and the water side of lateral subsurface flow wetland bed, and to realize the flow uniformity in lateral subsurface flow wetland bed, the settling containing ANAMMOX bacterium is layered on filler;
Plant waterplant in the biological observation pool, be also provided with rising pipe, by the mode water outlet of overflow.
Wherein, the pond body of the vertical baffling wetland waste disposal plant of the micro-aeration of self-cleaning type is provided with across bulkhead, pond body is divided into independent unit cells along water (flow) direction, the water outlet of a upper unit cells adopts the mode of perforation overflow to flow into next unit cells, and be provided with a valve, with the water inlet in control unit pond and water outlet in perforation place; The horizontal barricade that a body of wall is vertical with water (flow) direction is provided with in each unit cells, unit cells is divided into two sections, front and back, horizontal barricade bottom opening, the current in each unit cells is seethed up and down in wetland pond and passes through, form deflector type flow shape, avoid slough.
Wherein, micro-aeration tube comprises aeration supervisor, aeration main and aeration branch pipe, aeration supervisor arranges along the outer side of artificial swamp, aeration supervisor separates several aeration main, has at least one aeration main in each unit cells, aeration main along pool wall downwards and arrange at pond bottom horizontal, aeration main separates several aeration branch pipe, aeration branch pipe is longitudinally arranged side by side, and aeration supervisor and every root aeration main are provided with valve, and the solarization air cap diameter of described aeration tube arm is 1 ~ 3mm; Described backwash tube comprises back flushing supervisor, back flushing main and back flushing arm, backwash tube is arranged in bottom the body of pond, back flushing supervisor arranges along the outer side of artificial swamp, and pick out several back flushing main, each root back flushing main extends transversely into a unit cells, back flushing main picks out the back flushing arm be longitudinally arranged side by side again, and back flushing supervisor and every root main are provided with valve; Back flushing supervisor is also provided with blow-down pipe; Unit cells is also provided with upflow tube, discharges for sewage back flushing produced.
Wherein, solarization air cap is axially set to two rows along aeration branch pipe, and the angle that two medullary rays arranging solarization air caps cross aeration branch pipe axial line is 90 °.
Wherein, the available depth height that can realize the wetland bed body of the side direction drowned flow artificial wet land waste disposal plant of ANAMMOX denitrogenation is 0.4 ~ 0.6m.
Wherein, the wet land filler particle diameter of the vertical baffling wetland waste disposal plant of the micro-aeration of self-cleaning type is 10 ~ 50mm, and according to water (flow) direction, in unit cells, packing material size reduces successively.
Wherein, the filler that can realize the side direction drowned flow artificial wet land waste disposal plant of ANAMMOX denitrogenation is one or more in rubble, aggregate or rubble, and particle diameter is 5 ~ 10mm, and according to water (flow) direction, in unit cells, packing material size reduces successively.
In the utility model, the vertical baffling wetland of the micro-aeration of self-cleaning type adopts the mode of micro-aeration, improves the dissolved oxygen content of wet land filler layer inside further, and root system of plant oxygen release and aeration combine and ensure that organism can be removed smoothly.Compared with traditional aeration mode, micro-aeration rate is slowly little, and appropriate aeration facilitates biomembranous development in wetland, makes it can not wash away because a large amount of aeration causes microbial film, reduces the accumulation of mineral substance simultaneously, ensure that the water-flowing path between filler.The mode of micro-aeration is also under guarantee effluent quality condition in addition, more saves energy consumption, decreases running cost.
In addition, what the vertical baffling wetland of the micro-aeration of self-cleaning type adopted is adjustable micro-aeration mode, and the aeration rate of keying to each reaction member by valve regulates, and makes this reactor can adapt to various different change of water quality more flexibly.When influent COD content height, make partial reaction unit carry out aeration or carry out intermittent aeration by by-pass valve control, so enhance reaction tank aerobic-anaerobic environment, strengthen organic removal effect; When influent COD content is lower, micro-aeration can be closed and adopt natural reaeration to maintain packing layer dissolved oxygen levels, save energy consumption further.
The blockage problem of artificial swamp is always relatively more serious, all there will be blocking in various degree after running for some time, and once blocking is difficult to repair.Prove through experimental study, the organic matter in its sewage of artificial swamp is mainly trapped in reactor water inlet portion by absorption, and successively decreases gradually along the organic content in the packing layer of drainage flow direction.Thus in the vertical baffling wetland of the micro-aeration of self-cleaning type of the present utility model, the packing material size of previous reaction tank is large compared with the packing material size of a rear reaction tank, and the local turbulent souring coordinating micro-aeration to be formed, filler is not easily blocked, and make reaction tank hold rearward also can adsorb and retain a certain amount of organic matter, make rear end also have comparatively sufficient carbon source to ensure the effect of biological carbon and phosphorous removal.In the vertical baffling wetland of the micro-aeration of self-cleaning type, set up back-purge system, after filler starts blocking, carry out back flushing, the permeability coefficient of packing layer can be improved, ensure that the stable of system outlet effect, also effectively extend the work-ing life of artificial swamp.
The setting of the lateral subsurface flow wetland waste disposal plant based on ANAMMOX denitrogenation principle of the present utility model, has adsorbed the nitrogen phosphorus of leading portion water outlet further.Meanwhile, because front reaction pond consumes most carbon source, and nitrogen element is removed fully, makes C/N in the water inlet of lateral subsurface flow wetland lower.For ensureing final standard water discharge discharge, the front end of side direction undercurrent bed being provided with a natural reaeration groove, thus ensure that in side direction undercurrent bed, carry out ANAMMOX biological denitrificaion provides adapt circumstance.Wherein, natural reaeration groove is that published CN102583760A " falls the formula of jumping thin water layer artificial swamp reoxygenation groove ", and water, when by natural reaeration groove, can form 5 ~ 20 millimeters of thickness water layers, water extensively contacts with air in groove, adds the dissolved oxygen in lateral subsurface flow wetland bed.
The deflector type of artificial swamp of the present utility model and undercurrent type fluidised form make the solid contact area of water large, the artificial swamp of micro-aeration is by bottom aeration, improve the dissolved oxygen in water body, enhance the effect of the microorganism in water body, and then improve the hydraulic load of wetland, therefore the floor space of native system significantly reduces compared with similar wetlands.
The biology observation pool of the present utility model is equivalent to the effect of clean water basin, plants waterplant in the pool, and other hazardous and noxious substances such as the pollution substance further in removal water and pathogenic bacteria, finally by the mode water outlet of overflow.
The beneficial effects of the utility model:
1) micro-aeration artificial swamp can the micro-aeration mode of flexible, and processing efficiency is high, can adapt to different change of water quality, and organic removal effect is good:
2) artificial swamp of self-cleaning type not easily blocks, and can carry out back flushing, stable effluent quality; Ensure that the long-term stability of wet land system is run;
3) removal of nitrogen element in water outlet is further ensured based on the lateral subsurface flow wetland bed of ANAMMOX denitrogenation principle; The natural reaeration groove set up between each stage optimizes the oxygen enrichment ability of wetland, can ensure to form low-oxygen environment in whole lateral subsurface flow wetland bed, can realize ANAMMOX biological denitrificaion without the need to artificial aeration, saves energy consumption;
4) self-cleaning type micro-aeration load artificial marsh sewage treatment system floor space is less, and technical process is short, operational management is easy; In the utility model, each pipeline is equipped with valve, the control that can be realized operational mode by the keying of by-pass valve control is switched, and whole structure of reactor is simple in addition, not easily blocks, so the technical process of planting reactor is short, operational management is easy;
5) because wet land system of the present utility model also exists the situations such as back flushing, self-cleaning type in the utility model can be carried out many groups and runs parallel at micro-aeration artificial swamp and side direction drowned flow artificial wet land, to ensure to process water continuously, and can increase or reduce cell according to actual water quality and quantity etc., reasonable employment, raises the efficiency.
Accompanying drawing explanation
Fig. 1 self-cleaning type micro-aeration composite artificial marsh sewage treatment system processing flow chart;
Fig. 2 self-cleaning type micro-aeration composite artificial marsh sewage treatment system floor map;
Fig. 3 self-cleaning type micro-aeration composite artificial marsh sewage treatment system diagrammatic cross-section;
The micro-aeration of Fig. 4 self-cleaning type vertical baffling wetland waste disposal plant sectional view;
The micro-aeration of Fig. 5 self-cleaning type vertical baffling artificial wet field facilities for treating sewage backwash tube orthographic plan;
The micro-aeration of Fig. 6 self-cleaning type vertical baffling artificial wet field facilities for treating sewage aeration tube orthographic plan;
The micro-aeration of Fig. 7 self-cleaning type vertical baffling artificial wet field facilities for treating sewage aeration branch pipe enlarged view;
Fig. 8 lateral subsurface flow wetland treatment unit and method sectional view;
Fig. 9 lateral subsurface flow wetland treatment unit and method orthographic plan;
Reference numeral: 1 system water inlet pipe, 2 pre-treatment structures, the vertical baffling wetland waste disposal plant of the micro-aeration of 3 self-cleaning type, 31 water distributing areas, 32 across bulkheads, 33 horizontal barricades, 34 catchment areas, 35 upflow tubes, 36 pond bodies, 37 unit cells, 38 waterplant, 39 packing layers, 7 aeration tubes, the 4 side direction drowned flow artificial wet land waste disposal plants that can realize ANAMMOX denitrogenation, 41 natural reaeration grooves, 42 lateral subsurface flow wetland beds, 43 water distributors, 44 headers, the 5 biological observation pools, 6 rising pipes, 71 aeration supervisors, 72 aeration mains, 73 aeration branch pipes, 75 solarization air caps, 8 backwash tubes, 81 back flushing water inlet pipes, 82 recoil supervisors, 83 back flushing mains, 84 back flushing arms, 85 blow-down pipes, 9 valves.
Embodiment
The structure of embodiment 1 the utility model Sewage treatment systems
As shown in Figures 2 and 3, the micro-aeration composite artificial marsh sewage treatment system of self-cleaning type, comprise connected successively by pipeline pre-treatment structures 2, the vertical baffling wetland waste disposal plant 3 of the micro-aeration of self-cleaning type, the side direction drowned flow artificial wet land waste disposal plant 4 that can realize ANAMMOX denitrogenation, the biological observation pool 5.
Described pre-treatment structures 2 can be a settling tank or methane-generating pit, also can be natural pools.
As shown in Figure 4, the vertical baffling wetland waste disposal plant 3 of the micro-aeration of self-cleaning type is made up of water distributing area 31, pond body 36, aeration tube 7, backwash tube 8, catchment area 34, packing layer 39 and waterplant 38.Be followed successively by anaerobism wetland, oxidation of coal wetland and short-cut nitrification-denitrification wetland along water (flow) direction, anaerobism wetland and oxidation of coal wetland respectively adopt a unit cells 37, and short-cut nitrification-denitrification wetland is made up of some unit cells.Anaerobism wetland is disposed with backwash tube and packing layer from bottom to top, and oxidation of coal wetland and short-cut nitrification-denitrification wetland are disposed with backwash tube, micro-aeration tube, packing layer and waterplant from bottom to top.Described pond body 36 is provided with multiple across bulkhead 32 vertical with water (flow) direction, pond body is divided into multiple independent unit cells 37, the water outlet of a upper unit cells 37 adopts the mode of perforation overflow to flow into next unit cells 37, and be provided with a valve 9, with the water inlet in control unit pond 37 and water outlet in perforation place; Be provided with a horizontal barricade 33 vertical with water (flow) direction in each unit cells 37, unit cells 37 be divided into two sections, front and back, horizontal barricade 33 bottom opening, the current in each unit cells 37 seethed up and down in wetland pond and passes through, avoid slough; Each unit cells 37 is equipped with upflow tube 35, and the sewage for back flushing being produced is expelled to pre-treatment structures 2.Described aeration tube 7 comprises aeration supervisor 71, aeration main 72 and aeration branch pipe 73, aeration supervisor arranges along the outer side of artificial swamp, and be divided into several aeration main 72, each root aeration main 72 along unit cells 37 wall downwards and arrange at pond bottom horizontal, at least one aeration main is had in each unit cells, aeration branch pipe 73 is longitudinally arranged side by side, and aeration supervisor 71 and every root aeration main 72 are provided with valve 9 (as shown in Figure 6).Adopt the micro-aeration mode of classification, the gas-water ratio of total aeration rate is less than 2 ︰ 1, and the aeration rate controlling oxidation of coal wetland is greater than short-cut nitrification-denitrification wetland, make the wet dissolved oxygen of telluric water of oxidation of coal reach 1 ~ 2mg/L, the dissolved oxygen in short-cut nitrification-denitrification wetland water reaches 0.5mg/L.Solarization air cap 75 diameter of described aeration tube arm 73 is 1 ~ 3mm, and solarization air cap is axially set to 2 rows along aeration branch pipe, and the angle that two medullary rays arranging solarization air caps cross aeration branch pipe axial line is 90 ° (as shown in Figure 7).Also be provided with backwash tube 8 (as shown in Figure 5), comprise back flushing supervisor 82, back flushing main 83 and back flushing arm 84, backwash tube 8 blow-down pipe 85 of holding concurrently is arranged in bottom unit cells 37, back flushing supervisor 82 arranges along the outer side of artificial swamp, and be divided into several back flushing main 83, each root back flushing main 83 extends transversely into a unit cells 37, and back flushing arm 84 is longitudinally arranged side by side, and back flushing supervisor 82 and every root back flushing main 83 are provided with valve 9.The water of back flushing comes from back flushing water inlet pipe 81.The wet land filler particle diameter of the vertical baffling wetland waste disposal plant of the micro-aeration of self-cleaning type is 10 ~ 50mm, and according to water (flow) direction, in unit cells, packing material size reduces successively.
As shown in Figure 8 and Figure 9, the side direction drowned flow artificial wet land waste disposal plant 4 of the described ANAMMOX of realization denitrogenation is made up of natural reaeration groove, lateral subsurface flow wetland bed, one of them natural reaeration groove 41 and a lateral subsurface flow wetland bed 42 form one group of unit cells 37, natural reaeration groove is arranged in lateral subsurface flow wetland bed front end, and the series connection of many group unit cells forms described wet field facilities for treating sewage downwards jointly along gradient; Also be provided with water inlet pipe and rising pipe, water inlet pipe enters lateral subsurface flow wetland treatment unit for treatment sewage stable and uniform, and rising pipe is used for the water after collection and treatment and flows out lateral subsurface flow wetland treatment unit; Described lateral subsurface flow wetland bed comprises wetland bed body, water distributor 43, header 44, packing layer 39, wetland plant 38 and the settling containing ANAMMOX bacterium; Water distributor and header are all arranged on bottom lateral subsurface flow wetland bed, are arranged in feed-water end and the water side of lateral subsurface flow wetland bed, to realize the flow uniformity in lateral subsurface flow wetland bed; Wetland plant is planted above filler; The available depth height of wetland bed body is 0.4 ~ 0.6m; Filler is one or more in rubble, aggregate or rubble, and particle diameter is 5 ~ 10mm, and according to water (flow) direction, in unit cells, packing material size reduces successively.
The biological observation pool 5 is equivalent to the effect of clean water basin, is provided with rising pipe, by the mode water outlet of overflow.Can plant waterplant and stocked carp in the pool, other hazardous and noxious substances such as the pollution substance further in removal water and pathogenic bacteria, finally by the mode water outlet of overflow.The water outlet of whole system can pass through the indicative biologies such as observation fish, and test section water-quality guideline characterizes the water quality quality of its water outlet.
Embodiment 2 adopts the utility model treatment system to carry out sewage disposal
One, embodiment is when the systems are operating normally as follows, and flow process is see Fig. 1:
Town sewage enters pre-treatment structures through system water inlet pipe, removes floating matter, suspended substance, silt and partial organic substances that particle diameter is larger.
Sewage enters pre-treatment structures from system water inlet pipe, then successively by the vertical baffling wetland waste disposal plant of the micro-aeration of self-cleaning type and the process of ANAMMOX denitrogenation-type side direction drowned flow artificial wet land waste disposal plant, then enters the biological observation pool.
The micro-aeration of self-cleaning type vertical baffling wetland waste disposal plant pond body is divided into anaerobism, aerobic and micro-oxygen three sections along water (flow) direction, wherein anaerobism section and aerobic section are respectively 1 unit cells, respectively as anaerobism wetland and oxidation of coal wetland, micro-oxygen section can arrange more than 1 or 1 unit cells as short-cut nitrification-denitrification wetland according to water quality; Sewage from pre-treatment structures is flowed in the anaerobism wetland of anaerobism section by water distributing area, in the environment of anaerobism, decompose most of hardly degraded organic substance; Flow in the oxidation of coal wetland of aerobic section again, secrete the synergy of oxygen at micro-aeration and root system of plant under, make the dissolved oxygen in water reach 1 ~ 2mg/L, by Prevent Carbon Contamination thing efficient degradation; Finally flow in the short-cut nitrification-denitrification wetland of micro-oxygen section, secrete the synergy of oxygen at micro-aeration and root system of plant under, the dissolved oxygen in water is made to reach 0.5mg/L, for short-cut nitrification and denitrification provides adapt circumstance, N pollutent in sewage is efficiently removed, and the water outlet of the short-cut nitrification-denitrification wetland of micro-oxygen section adopts the mode of overflow to flow into catchment area; The vertical baffling wetland waste disposal plant of the micro-aeration of whole self-cleaning type adopts the operation scheme of continuum micromeehanics, continuous effluent, and wetland hydraulic surface loading controls at 2m
3/ (m
2.d) below, the hydraulic detention time of total vertical baffling wetland controls at more than 24h.
Sewage from the micro-aeration of self-cleaning type vertical baffling wetland waste disposal plant catchment area is flowed into the side direction drowned flow artificial wet land waste disposal plant that can realize ANAMMOX denitrogenation by water inlet pipe, sewage flows in the natural reaeration groove of first group of unit cells by water inlet pipe, the dissolved oxygen in sewage is increased by the mode of falling the thin water layer natural reaeration of the formula of jumping, flow in lateral subsurface flow wetland bed again, water distributor is furnished with in wetland bed body, header, filler, wetland plant and the settling containing ANAMMOX bacterium, on wetland bed vertical section, condition of water quality is even, whole wetland bed inside along water (flow) direction be one to detest the aerobic of anoxic, anoxic, the alternate environment of anaerobism, secrete the synergy of oxygen at root system of plant under, sewage is totally in micro-oxygen condition, the inflow for the treatment of sewage nitrite with the microenvironment of detesting anoxic for ANAMMOX bacteria growing provides adapt circumstance, sewage is occurred in lateral subsurface flow wetland simultaneously nitrated, denitrification and ANAMMOX reaction, carbon source organism in sewage is consumed gradually along journey, C/N is than constantly reducing, remove the N pollutent in sewage simultaneously, sewage flows in the natural reaeration groove of next group unit cells subsequently, then flows in lateral subsurface flow wetland bed, proceeds reaction, through too much organizing unit cells circular treatment, until reach Effluent criteria, whole treating processes adopts the operation scheme of continuum micromeehanics, continuous effluent, intake by pretreatment process control COD and TN concentration proportion at below 2:1, inlet COD concentration, at below 60mg/L, is intake by continuous natural stability, and wetland bed hydraulic surface loading controls at 0.3m
3/ (m
2.d), the hydraulic detention time of total lateral subsurface flow wetland controls at more than 18h.
Sewage is finally entering the biological observation pool after the process of system, the biological observation pool is equivalent to the effect of clean water basin, can plant waterplant and stocked carp in the pool, other hazardous and noxious substances such as the pollution substance further in removal water and pathogenic bacteria, finally by the mode water outlet of overflow.The water outlet of whole system can pass through the indicative biologies such as observation fish, and test section water-quality guideline characterizes the water quality quality of its water outlet.
Two, when the wet land filler particle diameter of the vertical baffling wetland waste disposal plant of the micro-aeration of self-cleaning type is 10 ~ 50mm, according to water (flow) direction, in unit cells, packing material size reduces successively.Filler carries out when there is blocking:
When there is overflow in some unit cells 37, then illustrate that the packing layer 39 of this unit cells 37 there occurs blocking, its solution is: the aeration tube valve 9 of first closing valve on its water inlet pipe and rising pipe 10 and this unit cells 37, close unit cells 37 and the valve 9 be connected between front-and-back unit pond that filler blocking occurs again, the valve 10 opened the valve 9 on back flushing water inlet pipe 81 and occur on the back flushing main 83 of filler blocking unit cells 37, carries out back flushing.The sewage that back flushing produces flows into pre-treatment structures 2 by upflow tube 35 and again processes.After back flushing, then close the valve 9 on back flushing water inlet pipe 81, and open valve 9 on blow-down pipe 85, the backwashing water be trapped in unit cells 37 is discharged, and unit cells 37 is carried out emptying leave unused, after idle for some time, normal operation of can again intaking again.
Claims (7)
1. the micro-aeration composite artificial marsh sewage treatment system of self-cleaning type, comprises the pre-treatment structures of water communication successively, the vertical baffling wetland waste disposal plant of the micro-aeration of self-cleaning type, the side direction drowned flow artificial wet land waste disposal plant that can realize ANAMMOX denitrogenation and the biological observation pool; It is characterized in that:
Described pre-treatment structures are provided with system water inlet pipe;
The vertical baffling wetland waste disposal plant of the micro-aeration of described self-cleaning type is made up of water distributing area, pond body and catchment area; Treatment sewage flows into water distributing area through water inlet pipe, then in the mode of overflow from inflow pond, water distributing area body, the water outlet after the body process of pond adopts the mode of overflow to flow into catchment area; Described pond body is that the vertical baffling wetland of multistage different processing functions is in series, anaerobism wetland, oxidation of coal wetland and short-cut nitrification-denitrification wetland is followed successively by along water (flow) direction, anaerobism wetland and oxidation of coal wetland respectively adopt a unit cells, and short-cut nitrification-denitrification wetland is made up of some unit cells; Anaerobism wetland is disposed with backwash tube and packing layer from bottom to top, oxidation of coal wetland and short-cut nitrification-denitrification wetland are disposed with backwash tube, micro-aeration tube, packing layer and waterplant from bottom to top, adopt the micro-aeration mode of classification, the gas-water ratio of total aeration rate is less than 2 ︰ 1, and the aeration rate controlling oxidation of coal wetland is greater than short-cut nitrification-denitrification wetland, make the wet dissolved oxygen of telluric water of oxidation of coal reach 1 ~ 2mg/L, the dissolved oxygen in short-cut nitrification-denitrification wetland water reaches 0.5mg/L;
The side direction drowned flow artificial wet land waste disposal plant that can realize ANAMMOX denitrogenation is made up of natural reaeration groove, lateral subsurface flow wetland bed, one of them natural reaeration groove connects a lateral subsurface flow wetland bed and forms one group of unit cells, and the series connection of many group unit cells forms described wet field facilities for treating sewage downwards jointly along gradient; Described natural reaeration groove is for falling the formula of jumping thin water layer natural reaeration groove; Described lateral subsurface flow wetland bed comprises wetland bed body, water distributor, header, filler, wetland plant and the settling containing ANAMMOX bacterium; Water distributor and header are all arranged on bottom lateral subsurface flow wetland bed, are arranged in feed-water end and the water side of lateral subsurface flow wetland bed, and to realize the flow uniformity in lateral subsurface flow wetland bed, the settling containing ANAMMOX bacterium is layered on filler;
Plant waterplant in the biological observation pool, be also provided with rising pipe, by the mode water outlet of overflow.
2. Sewage treatment systems as claimed in claim 1, it is characterized in that: the pond body of the vertical baffling wetland waste disposal plant of the micro-aeration of described self-cleaning type is provided with across bulkhead, pond body is divided into independent unit cells along water (flow) direction, the water outlet of a upper unit cells adopts the mode of perforation overflow to flow into next unit cells, and be provided with a valve, with the water inlet in control unit pond and water outlet in perforation place; A horizontal barricade vertical with water (flow) direction is provided with in each unit cells, unit cells is divided into two sections, front and back, horizontal barricade bottom opening, the current in each unit cells is seethed up and down in wetland pond and passes through, form deflector type flow shape, avoid slough.
3. Sewage treatment systems as claimed in claim 1 or 2, it is characterized in that: described micro-aeration tube comprises aeration supervisor, aeration main and aeration branch pipe, aeration supervisor arranges along the outer side of artificial swamp, aeration supervisor separates several aeration main, at least one aeration main is had in each unit cells, aeration main along pool wall downwards and arrange at pond bottom horizontal, aeration main separates several aeration branch pipe, aeration branch pipe is longitudinally arranged side by side, aeration supervisor and every root aeration main are provided with valve, the solarization air cap diameter of described aeration tube arm is 1 ~ 3mm, described backwash tube comprises back flushing supervisor, back flushing main and back flushing arm, backwash tube is arranged in bottom the body of pond, back flushing supervisor arranges along the outer side of artificial swamp, and pick out several back flushing main, each root back flushing main extends transversely into a unit cells, back flushing main picks out the back flushing arm be longitudinally arranged side by side again, and back flushing supervisor and every root main are provided with valve, back flushing supervisor is also provided with blow-down pipe, unit cells is also provided with upflow tube, discharges for sewage back flushing produced.
4. Sewage treatment systems as claimed in claim 3, is characterized in that: described solarization air cap is axially set to two rows along aeration branch pipe, the angle that two medullary rays arranging solarization air caps cross aeration branch pipe axial line is 90 °.
5. Sewage treatment systems as claimed in claim 1, is characterized in that: the available depth height that can realize the wetland bed body of the side direction drowned flow artificial wet land waste disposal plant of ANAMMOX denitrogenation is 0.4 ~ 0.6m.
6. Sewage treatment systems as claimed in claim 1, is characterized in that: the wet land filler particle diameter of the vertical baffling wetland waste disposal plant of the micro-aeration of described self-cleaning type is 10 ~ 50mm, and according to water (flow) direction, in unit cells, packing material size reduces successively.
7. the Sewage treatment systems as described in any one of claim 1, it is characterized in that: the filler that can realize the side direction drowned flow artificial wet land waste disposal plant of ANAMMOX denitrogenation is one or more in rubble, aggregate or rubble, particle diameter is 5 ~ 10mm, according to water (flow) direction, in unit cells, packing material size reduces successively.
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| CN201520864486.3U CN205099555U (en) | 2015-11-02 | 2015-11-02 | From clear aeration integrated constructed wetland sewage treatment system that declines |
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| CN201520864486.3U CN205099555U (en) | 2015-11-02 | 2015-11-02 | From clear aeration integrated constructed wetland sewage treatment system that declines |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105254127A (en) * | 2015-11-02 | 2016-01-20 | 重庆大学 | Self-cleaning type micro-aeration combined constructed wetland sewage treatment system and method |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105254127A (en) * | 2015-11-02 | 2016-01-20 | 重庆大学 | Self-cleaning type micro-aeration combined constructed wetland sewage treatment system and method |
| CN105254127B (en) * | 2015-11-02 | 2018-02-13 | 重庆大学 | The micro- aeration composite artificial marsh sewage treatment system of self-cleaning type |
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