CN204779227U - Processing system is synthesized to high -efficient sewage - Google Patents
Processing system is synthesized to high -efficient sewage Download PDFInfo
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- CN204779227U CN204779227U CN201520328760.5U CN201520328760U CN204779227U CN 204779227 U CN204779227 U CN 204779227U CN 201520328760 U CN201520328760 U CN 201520328760U CN 204779227 U CN204779227 U CN 204779227U
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- Prior art keywords
- equalizing tank
- elevating lever
- sewage
- aeration
- mud
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- 239000010865 sewage Substances 0.000 title claims abstract description 109
- 238000005273 aeration Methods 0.000 claims abstract description 86
- 239000002253 acid Substances 0.000 claims abstract description 59
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 27
- 238000005189 flocculation Methods 0.000 claims abstract description 22
- 230000016615 flocculation Effects 0.000 claims abstract description 22
- 238000004140 cleaning Methods 0.000 claims abstract description 19
- 238000001914 filtration Methods 0.000 claims abstract description 15
- 239000001301 oxygen Substances 0.000 claims abstract description 15
- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 claims abstract description 15
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 15
- 230000003028 elevating Effects 0.000 claims description 74
- BVKZGUZCCUSVTD-UHFFFAOYSA-N Carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 claims description 35
- 239000000126 substance Substances 0.000 claims description 27
- 238000009795 derivation Methods 0.000 claims description 22
- 210000003128 Head Anatomy 0.000 claims description 14
- 230000000694 effects Effects 0.000 claims description 14
- 238000003756 stirring Methods 0.000 claims description 14
- 239000002699 waste material Substances 0.000 claims description 12
- 239000002351 wastewater Substances 0.000 claims description 8
- 239000011148 porous material Substances 0.000 claims description 6
- 239000007789 gas Substances 0.000 claims description 5
- 238000011084 recovery Methods 0.000 abstract 2
- 238000000034 method Methods 0.000 description 11
- 238000010276 construction Methods 0.000 description 2
- 239000003814 drug Substances 0.000 description 2
- 238000007667 floating Methods 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000006386 neutralization reaction Methods 0.000 description 2
- 239000010815 organic waste Substances 0.000 description 2
- 230000020477 pH reduction Effects 0.000 description 2
- 241000251468 Actinopterygii Species 0.000 description 1
- 206010021143 Hypoxia Diseases 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 230000000903 blocking Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000001146 hypoxic Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000035943 smell Effects 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Abstract
The utility model provides a processing system is synthesized to high -efficient sewage, including the contaminated water filtration apparatus and the oxygen sewage treatment plant that holds concurrently, contaminated water filtration apparatus includes the urceolus, the clear water delivery port, and first sewage water inlet, the cartridge filter, the rotation axis, the motor, the drain, the cleaning brush, the baffle, the opening, the oxygen sewage treatment plant that holds concurrently includes that equalizing basin main part, aeration equipment, agitating unit, top layer mud recovery unit, bottom mud collection device, acid equalizing basin, charge device, flocculation charge device and bottom deposit collection device, the utility model discloses a sewage treatment system has improved sewage treatment's efficiency greatly, has reduced sewage treatment's time, has realized the innoxious recovery processing of sewage, has improved the utilization ratio of water resource greatly, has realized the saving and the rational utilization of water resource.
Description
Technical field
The utility model relates to technical field of sewage, more specifically to high-efficiency sewage total system.
Background technology
Sewage disposal (sewagetreatment, wastewatertreatment): the process reaching a certain water body of draining or the water quality requirement that reuses for making sewage it is purified.Sewage disposal is widely used in building, agricultural, and the every field such as traffic, the energy, petrochemical industry, environmental protection, urban look, medical treatment, food and drink, also come into the daily life of common people more and more.
In recent years; the most important thing of city domestic sewage discharge to be the primary pollution source city domestic sewage process of Chinese city water be urban water conservation at present and in the future and treatment work; this just requires that we will grab the construction of process sanitary sewage facility as the important content of urban infrastructure, and is too impatient to wait thing.And current treatment tank cost of manufacture is high, poor processing effect.
In some commercial runs, as a large amount of sewage also can be discharged in the Production in Chemical Plant processes such as food, papermaking, iron and steel, and these sewage major parts belong to organic waste water, this organic sewage just need can be discharged into occurring in nature through process, otherwise be directly discharged in nature water body the dissolved oxygen that can consume rapidly in water, cause water hypoxia and affect the existence of fish and other hydrocoles, the suspended substance simultaneously in sewage easily under anaerobic decomposes and produces foul smell, worsens water quality.Except organic waste water, in some commercial runs, also can produce acidification wastewater, if these acidification wastewater are directly disposed in rivers,lakes and seas, then can cause very large impact to ecotope.
Utility model content
Current operation of sewage disposal system cost is high, poor processing effect, the utility model overcomes deficiency of the prior art, provides high-efficiency sewage total system, improve the efficiency of sewage disposal, that can classify recycles the material comprised in sewage simultaneously.
The purpose of this utility model is achieved by following technical proposals.
High-efficiency sewage total system, comprises sewage filter device and double oxygen waste disposal plant.
Described sewage filter device comprises urceolus, and outer barrel has been horizontally disposed with dividing plate, and dividing plate is connected with outer tube inner wall is airtight;
Outer barrel is vertically provided with the identical cartridge filter of three shape and structures, cartridge filter is columnar structured, and its barrel is evenly provided with filter pore, and cartridge filter top is connected with urceolus top is airtight, cartridge filter bottom is connected with dividing plate is airtight, and the junction of dividing plate and cartridge filter bottom is provided with opening; Described cartridge filter inside is coaxially arranged with turning axle, and turning axle is connected with the motor of urceolus outside, and cartridge filter inside is also provided with cleaning brush, and cleaning brush is connected with turning axle, and described cleaning brush is spirane structure, and cleaning brush is close to cartridge filter inwall;
The top of cartridge filter is provided with sewage draining exit;
Be provided with the first sewage inlet bottom urceolus, outer tube side wall be provided with the Graceful mouth of a river.
In technique scheme, the aperture of described filter pore is 0.1mm-2mm.
In technique scheme, the bottom of described urceolus is semisphere.
Described double oxygen waste disposal plant, comprise equalizing tank main body, aerating apparatus, whipping appts, top layer mud retrieving arrangement, bottom mud collection device, acid equalizing tank, chemicals dosing plant, flocculation chemicals dosing plant and bottom sediment collection device, the second sewage inlet is provided with on the left of described equalizing tank main body, described second sewage inlet is connected with wastewater influent pipeline, sewage outlet is provided with on the right side of described equalizing tank main body, described sewage outlet is provided with filtering grid, described sewage outlet is connected with described sewage drainage pipeline, described sewage drainage pipeline is provided with described sump pump, described equalizing tank main body employing cross section is the structure of inverted isosceles trapezoid, described aerating apparatus comprises aeration air intake pump, aeration admission passage and aeration devices, described aeration admission passage is arranged around described equalizing tank body interior, described aeration admission passage is provided with described aeration opening uniformly, described aeration devices is arranged in described aeration opening, described aeration devices comprises aeration head and aeration pipe connecting, described aeration head adopts cross section to be semicircular structure, aeration spout is provided with uniformly at described aeration head top, be connected with described aeration pipe connecting bottom described aeration head, described aeration admission passage one end is provided with described aeration air intake pump, described whipping appts is arranged on the top of described equalizing tank main body, described whipping appts comprises agitator motor, stirring-head and stirring elevating lever, described agitator motor is arranged on described stirring elevating lever one end, described stirring-head is arranged on the other end of described agitator motor, described stirring elevating lever comprises the first elevating lever, second elevating lever, 3rd elevating lever and elevating lever sleeve pipe, described second elevating lever of socket in described first elevating lever, described 3rd elevating lever of socket in described second elevating lever, described elevating lever sleeve pipe is arranged on the outside of described stirring elevating lever, the length of described elevating lever sleeve pipe equals described first elevating lever, the summation of described second elevating lever and described 3rd elevating lever length, described top layer mud retrieving arrangement comprises mud accumulator tank, mud collects scraper plate and scraper plate rail plate, described scraper plate rail plate is arranged on described equalizing tank main body top, what described mud collected scraper plate activity is arranged on described scraper plate rail plate, described mud accumulator tank reclaims guide rail by mud and is arranged on side, described equalizing tank main body top, described mud accumulator tank adopts " L " shape structure, described bottom mud collection device is arranged on described equalizing tank main body bottom, described bottom mud collection device comprises bottom mud derives groove, derive scraper plate, derive scraper plate slide rail and bottom mud derivation base plate, described bottom mud derives the bottom end vicinity that base plate is arranged on described equalizing tank main body, described mud derives the below that groove is arranged on described mud water outlet, described derivation scraper plate slide rail is arranged on described equalizing tank main body bottom, the activity of described derivation scraper plate be arranged on described derivation scraper plate slide rail, described sewage drainage pipeline is connected with described acid equalizing tank, both sides, described acid equalizing tank top are respectively arranged with described chemicals dosing plant and described flocculation chemicals dosing plant, PH proofing unit is provided with in described acid equalizing tank, soda acid whipping appts is provided with above described acid equalizing tank, described soda acid whipping appts comprises soda acid agitator motor, soda acid agitator arm and soda acid stirring-head, described soda acid agitator motor is arranged on described soda acid agitator arm one end, the described soda acid agitator arm the other end is provided with described soda acid stirring-head, the input terminus of described chemicals dosing plant is connected with the first output terminal of described PH proofing unit, the input terminus of described flocculation chemicals dosing plant is connected with the second output terminal of described PH proofing unit, flocculation sediment filtering grid is provided with near bottom described acid equalizing tank, the below of described flocculation sediment filtering grid is provided with described bottom sediment collection device.
Described equalizing tank main body top is provided with air outlet, and described air outlet is connected with collection gas cylinder by exhaust line.
The length sum of described first elevating lever, described second elevating lever and described 3rd elevating lever is less than or equal to the degree of depth of described equalizing tank main body, the length of described second elevating lever is the 4/5-3/4 of described first elevating lever length, and the length of described 3rd elevating lever is the 4/5-3/4 of described second elevating lever length.
The height of described derivation scraper plate is less than or equal to the distance between described bottom mud derivation base plate and described equalizing tank main body bottom, and the height of described mud collection scraper plate is the 1/6-1/5 of described equalizing tank body height.
Side, described equalizing tank main body top is provided with aeration tube import, described equalizing tank main body top opposite side is provided with aeration tube outlet, described aeration admission passage enters described equalizing tank body interior by described aeration tube import, and described aeration admission passage leaves described equalizing tank body interior by described aeration tube outlet.
The beneficial effects of the utility model are: compared with prior art, Sewage treatment systems of the present utility model is provided with aerating apparatus, by around the aerating apparatus be arranged in equalizing tank main body, substantially increase the aeration effect of equalizing tank body interior sewage, after combining with whipping appts, make sewage depths also can carry out aeration effectively, substantially increase the efficiency of sewage disposal, decrease the time needed for sewage disposal, achieve the harmless treatment of sewage, substantially increase the utilization ratio of water resources, achieve saving and the Appropriate application of water resources.
Accompanying drawing explanation
Fig. 1 is one-piece construction schematic diagram of the present utility model;
Fig. 2 is that the utility model is held concurrently the structural representation of aerating apparatus in oxygen waste disposal plant;
In figure, 1 is urceolus, 2 is the Graceful mouth of a river, 3 is the first sewage inlet, 4 is cartridge filter, 5 is turning axle, 6 is motor, 7 is sewage draining exit, 8 is cleaning brush, 9 is dividing plate, 10 is opening, 11 is equalizing tank main body, 12 is aerating apparatus, 13 is the second sewage inlet, 14 is wastewater influent pipeline, 15 is sewage outlet, 16 is sewage drainage pipeline, 17 is aeration air intake pump, 18 is aeration admission passage, 19 is aeration head, 20 is aeration pipe connecting, 21 is agitator motor, 22 is stirring-head, 23 is mud accumulator tank, 24 is mud collection scraper plate, 25 is scraper plate rail plate, 26 is air outlet, 27 is exhaust line, 28 is sump pump, 29 for stirring elevating lever, 30 is bottom mud derivation groove, 31 for deriving scraper plate, 32 for deriving scraper plate slide rail, 33 is bottom mud derivation base plate, 34 is acid equalizing tank, 35 is chemicals dosing plant, 36 is flocculation chemicals dosing plant, 37 is PH proofing unit, 38 is soda acid agitator motor, 39 is soda acid agitator arm, 40 is soda acid stirring-head, 41 is flocculation sediment filtering grid.
Embodiment
Below by specific embodiment, the technical solution of the utility model is further described.
As depicted in figs. 1 and 2, 1 is urceolus, 2 is the Graceful mouth of a river, 3 is the first sewage inlet, 4 is cartridge filter, 5 is turning axle, 6 is motor, 7 is sewage draining exit, 8 is cleaning brush, 9 is dividing plate, 10 is opening, 11 is equalizing tank main body, 12 is aerating apparatus, 13 is the second sewage inlet, 14 is wastewater influent pipeline, 15 is sewage outlet, 16 is sewage drainage pipeline, 17 is aeration air intake pump, 18 is aeration admission passage, 19 is aeration head, 20 is aeration pipe connecting, 21 is agitator motor, 22 is stirring-head, 23 is mud accumulator tank, 24 is mud collection scraper plate, 25 is scraper plate rail plate, 26 is air outlet, 27 is exhaust line, 28 is sump pump, 29 for stirring elevating lever, 30 is bottom mud derivation groove, 31 for deriving scraper plate, 32 for deriving scraper plate slide rail, 33 is bottom mud derivation base plate, 34 is acid equalizing tank, 35 is chemicals dosing plant, 36 is flocculation chemicals dosing plant, 37 is PH proofing unit, 38 is soda acid agitator motor, 39 is soda acid agitator arm, 40 is soda acid stirring-head, 41 is flocculation sediment filtering grid.
High-efficiency sewage total system, comprises sewage filter device and double oxygen waste disposal plant.
Described sewage filter device comprises urceolus, and outer barrel has been horizontally disposed with dividing plate, and dividing plate is connected with outer tube inner wall is airtight;
Outer barrel is vertically provided with the identical cartridge filter of three shape and structures, cartridge filter is columnar structured, and its barrel is evenly provided with filter pore, and cartridge filter top is connected with urceolus top is airtight, cartridge filter bottom is connected with dividing plate is airtight, and the junction of dividing plate and cartridge filter bottom is provided with opening; Described cartridge filter inside is coaxially arranged with turning axle, and turning axle is connected with the motor of urceolus outside, and cartridge filter inside is also provided with cleaning brush, and cleaning brush is connected with turning axle, and described cleaning brush is spirane structure, and cleaning brush is close to cartridge filter inwall;
The top of cartridge filter is provided with sewage draining exit;
Be provided with the first sewage inlet bottom urceolus, outer tube side wall be provided with the Graceful mouth of a river.
In technique scheme, the aperture of described filter pore is 0.1mm-2mm.
In technique scheme, the bottom of described urceolus is semisphere.
When this sewage filter device uses, sewage enters outer barrel from the first sewage inlet, and three cartridge filters filter sewage, and the clear water after filtration is discharged from the Graceful mouth of a river, and mud and the impurity of filtration are discharged by sewage draining exit.Simultaneously, driven by motor turning axle rotates, turning axle drives cleaning brush to clean cartridge filter inwall, prevent cartridge filter from blocking, because cleaning brush 8 is spirane structure, therefore the mud in cartridge filter can be driven to assemble to sewage draining exit 7 by the spiral effect of cleaning brush, improve the rate of discharge of mud, effectively prevent the mud brushed down from falling after rise to the first sewage inlet place simultaneously.
Described double oxygen waste disposal plant, comprise equalizing tank main body, aerating apparatus, whipping appts, top layer mud retrieving arrangement, bottom mud collection device, acid equalizing tank, chemicals dosing plant, flocculation chemicals dosing plant and bottom sediment collection device, the second sewage inlet is provided with on the left of described equalizing tank main body, described second sewage inlet is connected with wastewater influent pipeline, sewage outlet is provided with on the right side of described equalizing tank main body, described sewage outlet is provided with filtering grid, described sewage outlet is connected with described sewage drainage pipeline, described sewage drainage pipeline is provided with described sump pump, described equalizing tank main body employing cross section is the structure of inverted isosceles trapezoid, described aerating apparatus comprises aeration air intake pump, aeration admission passage and aeration devices, described aeration admission passage is arranged around described equalizing tank body interior, described aeration admission passage is provided with described aeration opening uniformly, described aeration devices is arranged in described aeration opening, described aeration devices comprises aeration head and aeration pipe connecting, described aeration head adopts cross section to be semicircular structure, aeration spout is provided with uniformly at described aeration head top, be connected with described aeration pipe connecting bottom described aeration head, described aeration admission passage one end is provided with described aeration air intake pump, described whipping appts is arranged on the top of described equalizing tank main body, described whipping appts comprises agitator motor, stirring-head and stirring elevating lever, described agitator motor is arranged on described stirring elevating lever one end, described stirring-head is arranged on the other end of described agitator motor, described stirring elevating lever comprises the first elevating lever, second elevating lever, 3rd elevating lever and elevating lever sleeve pipe, described second elevating lever of socket in described first elevating lever, described 3rd elevating lever of socket in described second elevating lever, described elevating lever sleeve pipe is arranged on the outside of described stirring elevating lever, the length of described elevating lever sleeve pipe equals described first elevating lever, the summation of described second elevating lever and described 3rd elevating lever length, described top layer mud retrieving arrangement comprises mud accumulator tank, mud collects scraper plate and scraper plate rail plate, described scraper plate rail plate is arranged on described equalizing tank main body top, what described mud collected scraper plate activity is arranged on described scraper plate rail plate, described mud accumulator tank reclaims guide rail by mud and is arranged on side, described equalizing tank main body top, described mud accumulator tank adopts " L " shape structure, described bottom mud collection device is arranged on described equalizing tank main body bottom, described bottom mud collection device comprises bottom mud derives groove, derive scraper plate, derive scraper plate slide rail and bottom mud derivation base plate, described bottom mud derives the bottom end vicinity that base plate is arranged on described equalizing tank main body, described mud derives the below that groove is arranged on described mud water outlet, described derivation scraper plate slide rail is arranged on described equalizing tank main body bottom, the activity of described derivation scraper plate be arranged on described derivation scraper plate slide rail, described sewage drainage pipeline is connected with described acid equalizing tank, both sides, described acid equalizing tank top are respectively arranged with described chemicals dosing plant and described flocculation chemicals dosing plant, PH proofing unit is provided with in described acid equalizing tank, soda acid whipping appts is provided with above described acid equalizing tank, described soda acid whipping appts comprises soda acid agitator motor, soda acid agitator arm and soda acid stirring-head, described soda acid agitator motor is arranged on described soda acid agitator arm one end, the described soda acid agitator arm the other end is provided with described soda acid stirring-head, the input terminus of described chemicals dosing plant is connected with the first output terminal of described PH proofing unit, the input terminus of described flocculation chemicals dosing plant is connected with the second output terminal of described PH proofing unit, flocculation sediment filtering grid is provided with near bottom described acid equalizing tank, the below of described flocculation sediment filtering grid is provided with described bottom sediment collection device.
Described equalizing tank main body top is provided with air outlet, and described air outlet is connected with collection gas cylinder by exhaust line.
The length sum of described first elevating lever, described second elevating lever and described 3rd elevating lever is less than or equal to the degree of depth of described equalizing tank main body, the length of described second elevating lever is the 4/5-3/4 of described first elevating lever length, and the length of described 3rd elevating lever is the 4/5-3/4 of described second elevating lever length.
The height of described derivation scraper plate is less than or equal to the distance between described bottom mud derivation base plate and described equalizing tank main body bottom, and the height of described mud collection scraper plate is the 1/6-1/5 of described equalizing tank body height.
Side, described equalizing tank main body top is provided with aeration tube import, described equalizing tank main body top opposite side is provided with aeration tube outlet, described aeration admission passage enters described equalizing tank body interior by described aeration tube import, and described aeration admission passage leaves described equalizing tank body interior by described aeration tube outlet.
This double oxygen waste disposal plant is provided with aerating apparatus, by around the aerating apparatus be arranged in equalizing tank main body, substantially increase the aeration effect of equalizing tank body interior sewage, after combining with whipping appts, make sewage depths also can carry out aeration effectively, substantially increase the efficiency of sewage disposal, decrease the time needed for sewage disposal; The setting of top layer mud retrieving arrangement, makes the mud floating on sewage upper strata in advance collected by top layer mud retrieving arrangement, the mud floating on sewage upper strata can be made can not to affect the aeration effect of sewage, also reduce the content of mud in sewage simultaneously; Described equalizing tank main body top is provided with air outlet, air outlet is connected with collection gas cylinder, the biogas and other gas that produce in sewage treatment process can be collected in, so not only efficiently utilize the various by products produced in sewage treatment process, also can ensure the stable of equalizing tank body interior pressure simultaneously, ensure the running of equalizing tank Soil stability; Be provided with bottom mud collection device, derived by bottom mud that base plate is temporary is separated being deposited on equalizing tank main body bottom mud with the sewage in equalizing tank main body, recycling derives the motion of scraper plate on the derivation scraper plate slide rail being arranged on equalizing tank main body bottom, the mud being deposited on equalizing tank main body bottom is made all to be scraped near mud derivation groove, then derive groove by mud the mud of equalizing tank main body bottom is derived, further reduce the content of mud in sewage, improve the efficiency of sewage disposal; Being provided with acid equalizing tank, neutralization reaction can being carried out in acid equalizing tank, with the emission standard making it reach national regulation, to preserve the ecological environment by going out the sour water of mud; PH proofing unit, soda acid whipping appts and chemicals dosing plant is provided with in acid equalizing tank, by adding in alkalescence and medicine in the detection control chemicals dosing plant oxytropism equalizing tank of PH proofing unit, under the effect of soda acid whipping appts, make to carry out effective neutralization reaction with medicine in sour water and alkalescence, after treating that PH proofing unit detects that the pH value of sour water is up to standard, control to add flocculation agent in flocculation chemicals dosing plant oxytropism equalizing tank, to purify waste water further, finally will be passed through outside the sour water discharger of purification by water port.
Above the utility model has been described in detail, but described content being only preferred embodiment of the present utility model, can not being considered to for limiting practical range of the present utility model.All equalizations done according to the utility model application range change and improve, and all should still belong within patent covering scope of the present utility model.
Claims (7)
1. high-efficiency sewage total system, is characterized in that: comprise sewage filter device and double oxygen waste disposal plant,
Described sewage filter device comprises urceolus, and outer barrel has been horizontally disposed with dividing plate, and dividing plate is connected with outer tube inner wall is airtight;
Outer barrel is vertically provided with the identical cartridge filter of three shape and structures, cartridge filter is columnar structured, and its barrel is evenly provided with filter pore, and cartridge filter top is connected with urceolus top is airtight, cartridge filter bottom is connected with dividing plate is airtight, and the junction of dividing plate and cartridge filter bottom is provided with opening; Described cartridge filter inside is coaxially arranged with turning axle, and turning axle is connected with the motor of urceolus outside, and cartridge filter inside is also provided with cleaning brush, and cleaning brush is connected with turning axle, and described cleaning brush is spirane structure, and cleaning brush is close to cartridge filter inwall; The top of cartridge filter is provided with sewage draining exit; Be provided with the first sewage inlet bottom urceolus, outer tube side wall be provided with the Graceful mouth of a river;
Described double oxygen waste disposal plant comprises equalizing tank main body, aerating apparatus, whipping appts, top layer mud retrieving arrangement, bottom mud collection device, acid equalizing tank, chemicals dosing plant, flocculation chemicals dosing plant and bottom sediment collection device, the second sewage inlet is provided with on the left of described equalizing tank main body, described second sewage inlet is connected with wastewater influent pipeline, sewage outlet is provided with on the right side of described equalizing tank main body, described sewage outlet is provided with filtering grid, described sewage outlet is connected with described sewage drainage pipeline, described sewage drainage pipeline is provided with described sump pump, described equalizing tank main body employing cross section is the structure of inverted isosceles trapezoid, described aerating apparatus comprises aeration air intake pump, aeration admission passage and aeration devices, described aeration admission passage is arranged around described equalizing tank body interior, described aeration admission passage is provided with described aeration opening uniformly, described aeration devices is arranged in described aeration opening, described aeration devices comprises aeration head and aeration pipe connecting, described aeration head adopts cross section to be semicircular structure, aeration spout is provided with uniformly at described aeration head top, be connected with described aeration pipe connecting bottom described aeration head, described aeration admission passage one end is provided with described aeration air intake pump, described whipping appts is arranged on the top of described equalizing tank main body, described whipping appts comprises agitator motor, stirring-head and stirring elevating lever, described agitator motor is arranged on described stirring elevating lever one end, described stirring-head is arranged on the other end of described agitator motor, described stirring elevating lever comprises the first elevating lever, second elevating lever, 3rd elevating lever and elevating lever sleeve pipe, described second elevating lever of socket in described first elevating lever, described 3rd elevating lever of socket in described second elevating lever, described elevating lever sleeve pipe is arranged on the outside of described stirring elevating lever, the length of described elevating lever sleeve pipe equals described first elevating lever, the summation of described second elevating lever and described 3rd elevating lever length, described top layer mud retrieving arrangement comprises mud accumulator tank, mud collects scraper plate and scraper plate rail plate, described scraper plate rail plate is arranged on described equalizing tank main body top, what described mud collected scraper plate activity is arranged on described scraper plate rail plate, described mud accumulator tank reclaims guide rail by mud and is arranged on side, described equalizing tank main body top, described mud accumulator tank adopts " L " shape structure, described bottom mud collection device is arranged on described equalizing tank main body bottom, described bottom mud collection device comprises bottom mud derives groove, derive scraper plate, derive scraper plate slide rail and bottom mud derivation base plate, described bottom mud derives the bottom end vicinity that base plate is arranged on described equalizing tank main body, described mud derives the below that groove is arranged on described mud water outlet, described derivation scraper plate slide rail is arranged on described equalizing tank main body bottom, the activity of described derivation scraper plate be arranged on described derivation scraper plate slide rail, described sewage drainage pipeline is connected with described acid equalizing tank, both sides, described acid equalizing tank top are respectively arranged with described chemicals dosing plant and described flocculation chemicals dosing plant, PH proofing unit is provided with in described acid equalizing tank, soda acid whipping appts is provided with above described acid equalizing tank, described soda acid whipping appts comprises soda acid agitator motor, soda acid agitator arm and soda acid stirring-head, described soda acid agitator motor is arranged on described soda acid agitator arm one end, the described soda acid agitator arm the other end is provided with described soda acid stirring-head, the input terminus of described chemicals dosing plant is connected with the first output terminal of described PH proofing unit, the input terminus of described flocculation chemicals dosing plant is connected with the second output terminal of described PH proofing unit, flocculation sediment filtering grid is provided with near bottom described acid equalizing tank, the below of described flocculation sediment filtering grid is provided with described bottom sediment collection device.
2. high-efficiency sewage total system according to claim 1, is characterized in that: the aperture of filter pore described in described sewage filter device is 0.1mm-2mm.
3. high-efficiency sewage total system according to claim 1, is characterized in that: the bottom of urceolus described in described sewage filter device is semisphere.
4. high-efficiency sewage total system according to claim 1, is characterized in that: in described double oxygen waste disposal plant, described equalizing tank main body top is provided with air outlet, and described air outlet is connected with collection gas cylinder by exhaust line.
5. high-efficiency sewage total system according to claim 1, it is characterized in that: the length sum of the first elevating lever described in described double oxygen waste disposal plant, described second elevating lever and described 3rd elevating lever is less than or equal to the degree of depth of described equalizing tank main body, the length of described second elevating lever is the 4/5-3/4 of described first elevating lever length, and the length of described 3rd elevating lever is the 4/5-3/4 of described second elevating lever length.
6. high-efficiency sewage total system according to claim 1, it is characterized in that: the height of deriving scraper plate described in described double oxygen waste disposal plant is less than or equal to described bottom mud derives distance between base plate and described equalizing tank main body bottom, the height that described mud collects scraper plate is the 1/6-1/5 of described equalizing tank body height.
7. high-efficiency sewage total system according to claim 1, it is characterized in that: in described double oxygen waste disposal plant, side, described equalizing tank main body top is provided with aeration tube import, described equalizing tank main body top opposite side is provided with aeration tube outlet, described aeration admission passage enters described equalizing tank body interior by described aeration tube import, and described aeration admission passage leaves described equalizing tank body interior by described aeration tube outlet.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520328760.5U CN204779227U (en) | 2015-05-20 | 2015-05-20 | Processing system is synthesized to high -efficient sewage |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520328760.5U CN204779227U (en) | 2015-05-20 | 2015-05-20 | Processing system is synthesized to high -efficient sewage |
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| CN204779227U true CN204779227U (en) | 2015-11-18 |
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| CN201520328760.5U Expired - Fee Related CN204779227U (en) | 2015-05-20 | 2015-05-20 | Processing system is synthesized to high -efficient sewage |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107601754A (en) * | 2016-07-12 | 2018-01-19 | 天津宏晟新环保科技有限公司 | A kind of settler for Wastewater treatment |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107601754A (en) * | 2016-07-12 | 2018-01-19 | 天津宏晟新环保科技有限公司 | A kind of settler for Wastewater treatment |
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