CN208648891U - A kind of composite flow manual-rapid infiltration ecological bed - Google Patents

A kind of composite flow manual-rapid infiltration ecological bed Download PDF

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CN208648891U
CN208648891U CN201720089819.9U CN201720089819U CN208648891U CN 208648891 U CN208648891 U CN 208648891U CN 201720089819 U CN201720089819 U CN 201720089819U CN 208648891 U CN208648891 U CN 208648891U
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bed
layer
buffer layer
packet air
detained
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张建强
黄雯
冯程瑜
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Southwest Jiaotong University
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Abstract

The utility model discloses a kind of composite flow manual-rapid infiltration ecological beds, including seeping pond ontology fastly, fast seep is equipped with inhalant region in the ontology of pond, buffer layer one, level-one packet air-bed, separate layer, it is detained bed, connectivity layer, full water bed, buffer layer two, secondary packet air-bed and supporting layer, connectivity layer is set to the lower section for being detained bed and full water bed, discharge outlet one is equipped at buffer layer two, discharge outlet two is equipped at supporting layer, treatment sewage is intake in a manner of downstream, buffer layer one is successively penetrated into from inhalant region, level-one packet air-bed, separate layer, it is detained bed, full water bed is successively penetrated into through connectivity layer up-flow, buffer layer two, secondary packet air-bed is successively penetrated into a manner of downstream via water outlet one again, supporting layer, it is discharged by discharge outlet two, level-one packet air-bed, it is detained bed, microorganism is attached in the filler surface of full water bed and secondary packet air-bed.The composite flow manual-rapid infiltration ecological bed, capital expenditure is few, and operating cost is low, and process flow is simple, can effectively remove the pollutants such as organic matter, nitrogen, phosphorus.

Description

A kind of composite flow manual-rapid infiltration ecological bed
Technical field
The utility model belongs to technical field of sewage treatment equipment, and in particular to a kind of composite flow manual-rapid infiltration ecological bed.
Background technique
In recent years, the water supply project of rural areas in our country gradual perfection, and drainage system falls behind relatively, many rural areas Sanitary sewage is directly discharged to river, irrigation canals and ditches without any processing, or is allowed to permeate the ground after being discharged into soil, or through septic tank It is discharged after simple process, causes water body or soil pollution, while destroying rural area entirety ecological environment and landscape, it is also possible to directly Or indirect threats are to the health of rural residents.Therefore, reinforce that domestic sewage in rural areas is effectively treated, avoid because life is dirty Rural area water body, soil and pollution of agricultural products caused by water direct emission are urgently solved during improving Rural Human Settlements Certainly the problem of.
Domestic sewage in rural areas is mainly derived from waste waste water, flushing waste water and the kitchen waste water generated during resident living Deng, it has the following characteristics that (1) since rural area takes up a large area, and population is relatively fewer or disperses, opposite point of sewage discharge It dissipates and discharges wide;(2) intermittent discharge, fluctuation is larger, is relatively concentrated in the early, middle and late Deng periods;(3) sewage quality is opposite Stablize, wherein the content of the pollutants such as organic matter, nitrogen, phosphorus is relatively high.Since the investment of traditional cities sewage treatment mode is big, energy Consumption is high, operating cost is high, complex management, it is difficult to adapt to the processing of such sewage, application and popularization difficulty are larger;And it is existing artificial Although cost is relatively low for the technologies such as wetland, biological pond, soil filtration, poor, denitrogenation dephosphorizing low efficiency that there are reoxygenations, easily blocking etc. Defect, longtime running effect are undesirable.So, in addition to energy qualified discharge, more to be built when selecting decentralized type sewage purification techniques If with low investment, operational management is conveniently, operating cost is low, secondary pollution is small, large and medium-sized scale municipal sewage cannot be adopted and indiscriminately imitated Treatment process and design parameter, and economic, efficient, energy conservation and easy-to-use principle should be followed.However, China is directed to agriculture at present The processing technique deposit of this kind of decentralized type sewage of village's sanitary sewage is obvious insufficient, and there are also very big development spaces.Therefore, one is developed Kind is easy to operate, convenient for management, cost is relatively low, efficient purification techniques carrys out the better purification for adapting to decentralized type sewage, It is of great significance to the recycling rate of waterused of raising water resource, alleviation the contradiction of supply and demand for the water resource, improvement Regional Eco-environmental Quality.
Utility model content
The purpose of this utility model is to solve the above problems, and provides that a kind of simple process, low in cost, scavenging effect is good Composite flow manual-rapid infiltration ecological bed.
In order to solve the above technical problems, the technical solution of the utility model is: a kind of composite flow manual-rapid infiltration ecological bed, packet Fast infiltration pond ontology is included, the fast infiltration pond ontology is interior to be successively arranged inhalant region, buffer layer one, level-one by treatment sewage row stream direction Packet air-bed, separate layer, delay bed, connectivity layer, full water bed, buffer layer two, secondary packet air-bed and supporting layer, the connectivity layer are set It is placed in the lower section for being detained bed and full water bed, discharge outlet one is equipped at buffer layer two, is equipped with discharge outlet two, dirt to be processed at supporting layer Water is intake in a manner of downstream, and buffer layer one is successively penetrated into from inhalant region, level-one packet air-bed, separate layer, is detained bed, through connectivity layer Up-flow successively penetrates into full water bed, buffer layer two, then secondary packet air-bed, support are successively penetrated into a manner of downstream via water outlet one Layer, is discharged by discharge outlet two, the level-one packet air-bed, be detained it is attached in the filler surface of bed, full water bed and secondary packet air-bed Have microorganism.
Preferably, it further includes by the sequentially connected water tank of pipeline, peristaltic pump, sprinkler, the fast infiltration that this is ecological bed Pond ontology is located at below sprinkler, is equipped with microcomputer time controller, the peristaltic pump on the pipeline of the water tank and peristaltic pump Flowmeter is installed on pipeline between sprinkler.
Preferably, the delay bed is identical with the height of full water bed.
Preferably, the level-one packet air-bed is uniform according to volume ratio 7:2:1 using natural river sand, zeolite sand, Dali stone sand Filler is used as after mixing, the partial size of natural river sand is 0.5~1.0mm, and the partial size of zeolite sand is 2~3mm, the partial size of Dali stone sand For 3~5mm.
Preferably, the delay bed and full water bed are all made of natural river sand, zeolite sand, shell sand according to volume ratio 8:1:1 It is used as filler after evenly mixing, the partial size of natural river sand is 0.2~0.5mm, and the partial size of zeolite sand is 1~2mm, the grain of shell sand Diameter is 2~3mm.
Preferably, the secondary packet air-bed is uniformly mixed using natural river sand, zeolite sand, shale sand according to volume ratio 3:1:1 Filler is used as after conjunction, the partial size of natural river sand is 0.5~1.0mm, and the partial size of zeolite sand is 2~3mm, and the partial size of shale sand is 3 ~5mm.
Preferably, the buffer layer one, separate layer, connectivity layer, buffer layer two and supporting layer are all made of gravel as filler, Grain size of gravel is 3~5mm.
Preferably, the inhalant region height is 10~15cm, is not filled with any filler.
Preferably, the inhalant region height is 10~15cm, and the height of the level-one packet air-bed is 50~80cm, described stagnant Staying the height of bed and full water bed is 30~50cm, the buffer layer one, separate layer, connectivity layer, buffer layer two and supporting layer Height is 2~5cm, and the height of the secondary packet air-bed is 30~50cm.
The beneficial effects of the utility model are: composite flow manual-rapid infiltration ecological bed provided by the utility model, capital expenditure Few, operating cost is low, without being aerated oxygen supply;Process flow is simple, and operational management is very convenient;Occupied area is small, is suitable for dividing Formula, small-scale sewage treatment are dissipated, the region that village, small towns and other city planting ductworks not yet cover comprehensively is particularly suitable for;Using " under The compound water intake mode that row stream+upstream+downstream " combines makes to generate differentiation oxygen environment and hydraulic retention between bed Time realizes effectively removing for the pollutants such as organic matter, nitrogen, phosphorus under middle-low load service condition.
Detailed description of the invention
Fig. 1 is the utility model composite flow manual-rapid infiltration ecological bed structure schematic diagram.
Description of symbols: 1, water tank;2, microcomputer time controller;3, peristaltic pump;4, flowmeter;5, sprinkler;6, into Pool;7, buffer layer one;8, level-one packet air-bed;9, separate layer;10, it is detained bed;11, connectivity layer;12, full water bed;13, buffer layer Two;14, discharge outlet one;15, secondary packet air-bed;16, supporting layer;17, discharge outlet two.
Specific embodiment
The utility model is described further in the following with reference to the drawings and specific embodiments:
As shown in Figure 1, the composite flow manual-rapid infiltration ecological bed of the utility model, including pond ontology is seeped fastly, it is fast to seep pond ontology It is interior by treatment sewage row stream direction be successively arranged inhalant region 6, buffer layer 1, level-one packet air-bed 8, separate layer 9, be detained bed 10, Connectivity layer 11, full water bed 12, buffer layer 2 13, secondary packet air-bed 15 and supporting layer 16.Connectivity layer 11, which is set to, is detained bed 10 With the lower section of full water bed 12, it is equipped with discharge outlet 1 at buffer layer 2 13, is equipped with discharge outlet 2 17 at supporting layer 16.Dirt to be processed Water is intake in a manner of downstream, and buffer layer 1 is successively penetrated into from inhalant region 6, level-one packet air-bed 8, separate layer 9, is detained bed 10, warp The up-flow of connectivity layer 11 successively penetrates into full water bed 12, buffer layer 2 13, then two are successively penetrated into a manner of downstream via water outlet one Grade packet air-bed 15, supporting layer 16, are discharged by discharge outlet 2 17, and level-one packet air-bed 8 is detained bed 10, full water bed 12 and secondary packet Microorganism is attached in the filler surface of air-bed 15.
In the present embodiment, level-one packet air-bed 8, be detained bed 10, full water bed 12, secondary packet air-bed 15 filler before filling It is all made of microbial inoculum and carries out microbial inoculant, the specific method is as follows: filler is mixed with sanitary sewage according to solid-liquid volume ratio 1:5, It adds 0.5g microbial inoculum in every 10L sanitary sewage, periodic agitation and replaces new sanitary sewage, filler is taken out after 2~3d, is inserted Corresponding bed.
Further, in the present embodiment, this is ecological bed further include by the sequentially connected water tank 1 of pipeline, peristaltic pump 3, Sprinkler 5, the fast pond ontology that seeps are located at 5 lower section of sprinkler.Sprinkler 5 is used for water distribution uniformity.The pipeline of water tank 1 and peristaltic pump 3 On microcomputer time controller 2 is installed, flowmeter 4 is installed on the pipeline between peristaltic pump 3 and sprinkler 5.Microcomputer time controller 2 For controlling flooding time, flowmeter 4 is for controlling flow of inlet water.The water intake mode for the treatment of sewage and flow control are simultaneously unlimited In the present embodiment, the other conventional water intake modes in this field also can be used.
6 height of inhalant region is 10~15cm, is not filled with any filler.The height of level-one packet air-bed 8 is 50~80cm, is used Natural river sand, zeolite sand, Dali stone sand are used as filler according to volume ratio 7:2:1 after evenly mixing, and the partial size of natural river sand is 0.5 ~1.0mm, the partial size of zeolite sand are 2~3mm, and the partial size of Dali stone sand is 3~5mm.It is detained the height of bed 10 and full water bed 12 It is identical, it is 30~50cm, is all made of natural river sand, zeolite sand, shell sand and is used as and fills out after evenly mixing according to volume ratio 8:1:1 Material, the partial size of natural river sand are 0.2~0.5mm, and the partial size of zeolite sand is 1~2mm, and the partial size of shell sand is 2~3mm.Second level The height of packet air-bed 15 be 30~50cm, using natural river sand, zeolite sand, shale sand according to volume ratio 3:1:1 after evenly mixing As filler, the partial size of natural river sand is 0.5~1.0mm, and the partial size of zeolite sand is 2~3mm, the partial size of shale sand is 3~ 5mm.Buffer layer 1, separate layer 9, connectivity layer 11, buffer layer 2 13 and supporting layer 16 height be 2~5cm, be all made of gravel Masonry is filler, and grain size of gravel is 3~5mm.
It is worth noting that the specific height and ratio of each section, can be according to realities there is no specifically limited in reaction tank Border requires to be set accordingly.In addition, the filler of each section is arranged, including filling kind, composition, ratio and specific ruler It is very little etc., be also not limited to described in the present embodiment, can be used in this field other conventional filling kinds and corresponding parameter into Row loads.
Composite flow manual-rapid infiltration ecological bed provided by the utility model, the removal principle to organic matter, nitrogen, phosphorus is:
(1) to the removal principle of organic matter: waste water is contacted with filler flowing for a long time, gradually forms biology in filler surface Film.Since the surface area of filler particles in each bed is very big, and it is attached with well-grown biomembrane, therefore, sewage can be made In organic matter be adsorbed, removed from water rapidly.Dry reoxygenation phase, micro- life are fallen in level-one packet air-bed 8 and secondary packet air-bed 15 A portion is used to synthesize new cellular material using organic matter as nutriment by object, and another part then passes through oxidation The synthesis for obtaining energy supply neoblast is decomposed, so that most of organic matter be enable to degrade, reaction process can be sketched are as follows: complicated Organic matter+O2→CO2↑+H2O+ stable product.In addition, organic matter can be used as denitrifying being detained in bed 10 and full water bed 12 Carbon source not only ensure that going on smoothly for denitrification process, but also can further decrease the concentration of outlet water organic substance.Meanwhile it is organic Object is also possible to remove by anaerobic metabolism, and reaction process can be sketched are as follows: complicated organic matter → CO2↑+CH4↑+unstable product, by Slow in anaerobic metabolic process, the effect is relatively small to the contribution of organic matter removal.
(2) to the removal principle of nitrogen: sewage penetrates into level-one packet air-bed 8, the nitrogen pollutant in the waterflooding phase, in sewage first It is trapped or is adsorbed on the surface of filler particles, is falling dry spell, level-one packet air-bed 8 starts reoxygenation, micro- life of filler surface attachment Object is by nitrification by mineralized nitrogen at nitrite nitrogen or nitrate nitrogen: NH4 +→NO2 -→NO3 -;Subsequently into be detained bed 10, by It is located at 8 lower section of level-one packet air-bed in being detained bed 10, reoxygenation effect is poor, and part nitrate nitrogen is made under anaerobic environment by denitrification It is removed with gaseous form is converted to: NO3 -→NO2 -→NO→N2O→N2;Full water bed 12 is subsequently entered, due to water bed 12 of satisfying Contour and bottom is interconnected with delay bed 10, is constantly in waterflooding state, ensure that good scarce/anaerobic environment, simultaneously Also hydraulic detention time is extended, the further removal of nitrogen pollutant is conducive to.When the water inlet of next period, it is detained bed 10 Sewage enters full water bed 12 in level-one packet air-bed 8 under the pressure of sewage, the water outlet of full water bed 12 enters secondary packet air-bed 15, leads to Cross waterflooding -- the natural reaeration process for falling dry alternate run further strengthens ecological bed denitrification effect.
(3) to the removal principle of phosphorus: the composite flow manual-rapid infiltration ecological bed is to there are mainly three types of the removals of phosphorus element pollutant Approach: first is that the assimilation of microorganism, phosphorus is used as indispensable nutriment in microorganism growth metabolism by microorganism In synthesis Self substances or it is converted into ATP;Second is that since the dissolved oxygen content of different zones in bed has differences, aerobic and anaerobism Environment is alternately present, the excess accumulation for being conducive to phosphorus and excessively release;Third is that the physics chemical action of filler, main includes absorption It with two aspects of chemical precipitation, is combined using a variety of fillers, there is good absorption and rejection effect to phosphorus element pollutant, And zeolite sand, shale sand etc. is used to be used as filler, wherein chemistry can occur with soluble phosphate for Ca, Fe and Al for being rich in etc. instead It answers, solubility low calcium phosphate, ferric phosphate or aluminum phosphate is generated, to enhance the dephosphorization ability of bed.
The utility model is described further below by experimental example, further show the utility model the advantages of and Principle, in following two experimental examples, inhalant region 6, level-one packet air-bed 8 are detained bed 10, full water bed 12, secondary packet air-bed 15 Height is respectively 10cm, 50cm, 30cm, 30cm, 30cm, buffer layer 1, separate layer 9, connectivity layer 11, buffer layer 2 13, support The height of layer 16 is 2cm.
Experimental example
The sanitary sewage of composite flow manual-rapid infiltration ecological bed processing is derived from Chengdu Pixian County peasant household, main water quality indicator As follows: COD concentration is 140~195mg/L, NH3- N concentration is 10~20mg/L, TN concentration is 12~30mg/L, TP concentration is 1 ~4mg/L, SS concentration is 70~100mg/L, pH value is 7.1~7.8, and sewage enters multiple after the pretreatment of simple precipitation and separation Collaborate manual-rapid infiltration ecological bed.Carrying out practically parameter is as follows: 25 DEG C of room temperature or so, hydraulic loading 0.3m3/(m2D), it transports daily 1:1,1:2,1:3 is respectively adopted in 3 periods of row, each periodic duty 8h, wet-dry ratio, detects 1~2 effluent quality daily.Knot Fruit is as shown in table 1:
Table 1: certain rural household's life wastewater treatment efficiency
Experimental example 2
The sanitary sewage of composite flow manual-rapid infiltration ecological bed processing is derived from Chengdu Pixian County villages and small towns community, main water quality Index is as follows: COD concentration is 200~350mg/L, NH3- N concentration is 30~50mg/L, TN concentration is 35~60mg/L, TP is dense Degree is 2~5mg/L, SS concentration is 100~300mg/L, pH value is 7.0~7.8.Sewage is after the pretreatment of simple precipitation and separation Into composite flow manual-rapid infiltration ecological bed.Carrying out practically parameter is as follows: 25 DEG C of room temperature or so, hydraulic loading 0.2m3/(m2D), 1:1,1:3,1:5 is respectively adopted in 2 periods of operation, each periodic duty 12h, wet-dry ratio daily, detects 1~2 water outlet daily Water quality.The results are shown in Table 2:
Table 2: certain villages and small towns community's life wastewater treatment efficiency
The main item controlled highest of effluent quality and " integrated wastewater discharge standard (GB8978-1996) " is allowed to discharge Concentration, which compares, to be obtained, and when handling certain rural household's life sewage and certain villages and small towns community's life sewage, be discharged COD, NH3-N、SS Concentration can reach " integrated wastewater discharge standard (GB8978-1996) " primary standard, also can reach certain removal to TN, TP Effect.Difference is, when handling certain rural household's life sewage, can get more preferably treatment effect under conditions of wet-dry ratio 1:3, and When handling certain villages and small towns community's life sewage, more preferably treatment effect can get under conditions of wet-dry ratio 1:5, this is because compound Turning flow artificial rapid infiltration ecological bed is closely related to the factors such as the treatment effect of sanitary sewage and influent quality, hydraulic loading, wet-dry ratio. In general, being contemplated that appropriate reduction hydraulic loading or extension fall the dry time, to obtain when pollutional load of intaking is higher More ideal wastewater purifying efficiency.
Those of ordinary skill in the art will understand that the embodiments described herein, which is to help reader, understands this reality With novel principle, it should be understood that the scope of the present invention is not limited to such specific embodiments and embodiments. Those skilled in the art can be made according to the technical disclosures disclosed by the utility model it is various do not depart from it is practical Novel substantive various other specific variations and combinations, these variations and combinations are still within the protection scope of the present invention.

Claims (6)

1. a kind of composite flow manual-rapid infiltration ecological bed, it is characterised in that: including seeping pond ontology fastly, in the fast infiltration pond ontology by Processing sewage row stream direction is successively arranged inhalant region (6), buffer layer one (7), level-one packet air-bed (8), separate layer (9), is detained bed (10), connectivity layer (11), full water bed (12), buffer layer two (13), secondary packet air-bed (15) and supporting layer (16), the connection Layer (11) is set to the lower section for being detained bed (10) and full water bed (12), is equipped with discharge outlet one (14), support at buffer layer two (13) Discharge outlet two (17) is equipped at layer (16), treatment sewage is intake in a manner of downstream, successively penetrates into buffer layer from inhalant region (6) Bed (10), separate layer (9), are detained at level-one packet air-bed (8) in one (7), through connectivity layer (11) up-flow successively penetrate into full water bed (12), Buffer layer two (13), then secondary packet air-bed (15), supporting layer (16) are successively penetrated into a manner of downstream via water outlet one, by arranging The mouth of a river two (17) discharge, the level-one packet air-bed (8), be detained bed (10), full water bed (12) and secondary packet air-bed (15) are filled out Material is attached with microorganism on surface.
2. composite flow manual-rapid infiltration ecological bed according to claim 1, it is characterised in that: it further includes passing through pipe that this is ecological bed The sequentially connected water tank in road (1), peristaltic pump (3), sprinkler (5), the fast infiltration pond ontology are located at below sprinkler (5), institute It states and is equipped on the pipeline of water tank (1) and peristaltic pump (3) microcomputer time controller (2), the peristaltic pump (3) and sprinkler (5) Between pipeline on flowmeter (4) are installed.
3. composite flow manual-rapid infiltration ecological bed according to claim 1, it is characterised in that: the delay bed (10) and full water The height of bed (12) is identical.
4. composite flow manual-rapid infiltration ecological bed according to claim 1 to 3, it is characterised in that: the buffer layer one (7), separate layer (9), connectivity layer (11), buffer layer two (13) and supporting layer (16) are all made of gravel as filler, grain size of gravel For 3~5mm.
5. composite flow manual-rapid infiltration ecological bed according to claim 1 to 3, it is characterised in that: the inhalant region (6) Height is 10~15cm, is not filled with any filler.
6. composite flow manual-rapid infiltration ecological bed according to claim 1 to 3, it is characterised in that: the inhalant region (6) Height is 10~15cm, and the height of the level-one packet air-bed (8) is 50~80cm, bed (10) and the full water bed (12) of being detained Height is 30~50cm, the buffer layer one (7), separate layer (9), connectivity layer (11), buffer layer two (13) and supporting layer (16) height is 2~5cm, and the height of the secondary packet air-bed (15) is 30~50cm.
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110127955A (en) * 2019-06-12 2019-08-16 成都工业学院 A kind of double pond manual controlled infusions and method for low C/N than wastewater efficient denitrogenation

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110127955A (en) * 2019-06-12 2019-08-16 成都工业学院 A kind of double pond manual controlled infusions and method for low C/N than wastewater efficient denitrogenation
CN110127955B (en) * 2019-06-12 2024-04-30 成都工业学院 Double-pond artificial rapid infiltration system and method for high-efficiency denitrification of low-C/N ratio sewage

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