CN202080985U - Mini-type sewage-disposal device driven by wind power energy - Google Patents
Mini-type sewage-disposal device driven by wind power energy Download PDFInfo
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- CN202080985U CN202080985U CN2011200817866U CN201120081786U CN202080985U CN 202080985 U CN202080985 U CN 202080985U CN 2011200817866 U CN2011200817866 U CN 2011200817866U CN 201120081786 U CN201120081786 U CN 201120081786U CN 202080985 U CN202080985 U CN 202080985U
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/33—Wastewater or sewage treatment systems using renewable energies using wind energy
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Abstract
The utility model discloses a mini-type sewage-disposal device driven by wind power energy. The mini-type sewage-disposal device comprises an air supply device, a pre-treatment pool and an integrated biological-treatment device, wherein an air storage reservoir of the air supply device is connected with the pre-treatment pool and the integrated biological-treatment device through an air delivery pipe; the integrated biological-treatment device comprises a first-section biological mixing bed, a second-section biological mixing bed and a sedimentation tank which are arranged in a box body in parallel; a water inlet of the pre-treatment pool is connected with a sewage source, the water outlet of the pre-treatment pool is connected with a water inlet of the first-section biological mixing bed through a pipeline, the bottom of the first-section biological mixing bed is communicated with the bottom of the second-section biological mixing bed, the second-section biological mixing bed is communicated with the sedimentation tank through a diversion pipe, and a water outlet of the sedimentation tank is formed on the box body of the integrated biological-treatment device and is communicated with the outside through a water outlet pipe; and suspended fillers, gas-liquid mixing lift pipes and air pipes are arranged in the first-section biological mixing bed as well as the second-section biological mixing bed. After sewage is treated in the pre-treatment pool, pollutants in the sewage are removed in the first-section biological mixing bed and the second-section biological mixing bed through oxidation and decomposition.
Description
Technical field
The utility model relates to waste disposal plant, particularly relates to the aerobic biochemical sewage treatment unit that utilizes the wind energy air feed.
Background technology
For city, factories and miness, quantity of wastewater effluent is big, discharge point is concentrated, more easily realizes the concentrated improvement of sewage.And railway station along the line sewage discharge point disperses, quantity is many, and quantity of wastewater effluent is little, has increased difficulty for the improvement of sewage.If these type of source of pollution can not effectively be administered, also physical environment is produced bigger influence, therefore, the sewage disposal at railway station along the line more and more obtains paying attention in Environment in Railway Engineering Construction.
At present, the Small Sewage Treatment Equipment of railway station along the line operated by rotary motion aerobic biochemical technology, use motor fan aeration aerating in sewage lagoon, producing air water contact, mixing effect and water cycle in the aeration zone flows, keep microorganism, substrate, dissolved oxygen state balance in the sewage, for the microbiological deterioration organism provides favourable biochemical reaction condition.
The Small Sewage Treatment Equipment of the employing aerobic biochemical technology of railway station setting along the line, have stable, the characteristics that floor space is little.But, the existing apparatus energy consumption is higher, sewage promotes and the power consumption of blast aeration accounts for 60% of operation cost, in addition, the impact load that the biochemistry pool of waste disposal plant can not the fine adaptation Various Seasonal sewage water yield, change of water quality causes, the utilization ratio of blast aeration oxygenation is also restricted, and being difficult to provides best biochemical reaction condition for the microbiological deterioration organism.
Summary of the invention
The problem that exists at the aerobic biochemical technology Small Sewage Treatment Equipment of prior art, the utility model is released the Small Sewage Treatment Equipment of utilizing wind energy, its purpose is wind energy conversion system, the integration biological treatment device that biological mixed bed of Gas flow-limiting pressure reducer and two-part and settling tank constitute combines, utilize the energy of reproducible wind energy as water cycle and oxygenation, in the interior biological mixed bed of establishing floating stuffing, make microorganism in the sewage, substrate, dissolved oxygen fully contacts mixing, microorganism is adsorbed organism in the sewage, oxidation, decompose, realize the purifying treatment of sewage.
Wind energy described in the utility model drives Small Sewage Treatment Equipment and comprises air feeder, pretreatment pool and integration biological treatment device.Air feeder comprises wind energy conversion system, gas-holder, and wind energy conversion system connects gas-holder by wind conveying pipe, and the wind wheel blade of wind energy conversion system rotates in the wind, drives wind-force pneumatics pump and produces pressurized gas, is transported in the gas-holder.Gas-holder is connected with integration biological treatment device with pretreatment pool by the air output tube, integration biological treatment device comprises one section biological mixed bed being set up in parallel in the casing, two sections biological mixed beds and settling tank, and two sections biological mixed beds place between one section biological mixed bed and the settling tank.The water-in of pretreatment pool connects source of sewage, water outlet is by the water-in of one section biological mixed bed of pipe connection, one section biological mixed bed and two sections biological mixed bed bottoms are communicated with, two sections biological mixed beds and settling tank are communicated with by thrust-augmenting nozzle, and the water outlet of settling tank places on the casing of integration biological treatment device and by rising pipe and external communications.In one section biological mixed bed and two sections biological mixed beds floating stuffing, raising mixed gas and liquid pipe and blast main are set respectively, floating stuffing is arranged on the middle part in the mixed bed, the raising mixed gas and liquid pipe is vertically disposed pipe, blast main enters and is inserted in the raising mixed gas and liquid pipe from the casing outside, and the blast main epimere connects the air output tube of air feeder gas-holder by the Gas flow-limiting pressure reducer.
Pretreatment pool inside is provided with partition wall, and pretreatment pool is divided into two sections of front and back, and the water-in that connects source of sewage is arranged on the leading portion sidewall.Partition wall top is provided with water hole, and leading portion and back segment in the pretreatment pool are communicated with.The pretreatment pool back segment vertically is provided with sewage riser tube and pretreatment pool blast main, and sewage riser tube lower port places the pretreatment pool bottom, and the upper port of sewage riser tube connects the water-in of one section biological mixed bed by extension tube.The pretreatment pool blast main enters pretreatment pool from top and inserts in the sewage riser tube lower port, and pretreatment pool blast main epimere connects the air output tube of air feeder gas-holder by the first Gas flow-limiting pressure reducer.
The floating stuffing that is provided with in one section biological mixed bed and the two sections biological mixed beds is that voidage height, specific surface area are big, proportion is less than 1 macromolecule material filler, places to be set in parallel in the going up between an interception net and the following backplate of biological mixed bed inside.The raising mixed gas and liquid pipe is vertically disposed pipe, and its upper and lower port all becomes the hydraucone shape, the upper port of raising mixed gas and liquid pipe place interception net above, the lower port of raising mixed gas and liquid pipe place down prop up backplate below.Blast main enters biological mixed bed and is inserted in the raising mixed gas and liquid pipe from the casing outside, and reaches the bottom of raising mixed gas and liquid pipe.The blast main epimere connects the air output tube of air feeder gas-holder by the Gas flow-limiting pressure reducer.
Thrust-augmenting nozzle, settling tank blast main, reflux sludge tube, traverse baffle, effluent weir are set in the settling tank, and thrust-augmenting nozzle, settling tank blast main, reflux sludge tube are for vertically being inserted in the pipe in the settling tank respectively.The upper end of thrust-augmenting nozzle is communicated with the water outlet on two sections biological mixed bed tops, and the lower end places the bottom of settling tank, and lower end water outlet and level are to being 45 ° of angles, and many thrust-augmenting nozzles are evenly distributed in tank wall one side of separating two sections biological mixed beds and settling tank.The returned sluge infratubal port places the settling tank bottom, and the reflux sludge tube epimere passes settling tank and is connected to the muddy water import on one section biological mixed bed top and the muddy water import on pretreatment pool top.The settling tank blast main enters settling tank from the casing outside and is inserted into the reflux sludge tube bottom, and settling tank blast main epimere connects the air output tube of air feeder gas-holder by the 4th Gas flow-limiting pressure reducer.
At inboard setting of the settling tank tank wall that sets out water pipe and the wide effluent weir of this tank wall, effluent weir comprises riser and leveling board two portions, and along continuous straight runs is evenly arranged gully-hole on the riser.The effluent weir bottom is provided with traverse baffle, and traverse baffle is oblique to be fixed on the effluent weir riser bottom, and traverse baffle and effluent weir riser are wide.
The air output tube of air feeder gas-holder connects the blast main of pretreatment pool, one section biological mixed bed, two sections biological mixed beds and settling tank respectively by the Gas flow-limiting pressure reducer, with the compressed air delivery of gas-holder in pretreatment pool, biological mixed bed and settling tank.
The Gas flow-limiting pressure reducer is the cylinder of hollow and the parts of round platform unitized construction, comprise the first Gas flow-limiting pressure reducer, the second Gas flow-limiting pressure reducer, the 3rd Gas flow-limiting pressure reducer and the 4th Gas flow-limiting pressure reducer, be used to control the pressure and the flow of compressed-air actuated work output and input pretreatment pool and integration biological treatment device gas.
The Gas flow-limiting pressure reducer comprises nozzle, gas receiving chamber, gas mixing chamber, gas diffusion chamber.The inner chamber of gas receiving chamber, gas mixing chamber, gas diffusion chamber is communicated with, and the internal diameter of gas receiving chamber is greater than the internal diameter of gas mixing chamber.One end of gas mixing chamber connects gas receiving chamber, and the other end connects gas diffusion chamber.Gas diffusion chamber becomes the hydraucone shape, and the outlet of gas diffusion chamber is connected with the blast main of pretreatment pool and integration biological treatment device.In the gas receiving chamber nozzle is set, nozzle is connected with gas-holder, and the sidewall of gas receiving chamber is provided with the injection air suction inlet, on the injection air suction inlet air filter is installed.
Nozzle in the gas receiving chamber will spray from the air after the gas-holder pressure regulation, drive extraneous air simultaneously and enter receiving chamber through filter and injection air suction inlet, two portions air is successively through gas mixing chamber and gas diffusion chamber's current limliting decompression back output, enter pretreatment pool and integration biological treatment device through blast main again, for providing air water, mixes and the round-robin motivating force by waste disposal plant, for sewage being carried out the microorganism oxygen supply of biochemical action.
Sewage at first enters the pretreatment pool leading portion, remove inorganic silt particle and part suspended substance, water hole by partition wall top enters the pretreatment pool back segment again, pressurized air from the pretreatment pool blast main enters the sewage riser tube with sewage from lower port, and along the rising of sewage riser tube, the upper port from the sewage riser tube enters one section biological mixed bed by extension tube then.Sewage utilizes compressed-air actuated lifting in pretreatment pool, can reach certain preaeration effect.
Sewage enters one section biological mixed bed from the water-in on top, forms down and passes the bottom that floating stuffing arrives biological mixed bed to stream; Then, form gas-liquid mixed with pressurized air at the first raising mixed gas and liquid infratubal port from first blast main, rise along the first raising mixed gas and liquid pipe, and flow out from the upper port of the first raising mixed gas and liquid pipe, and with returning biological mixed bed bottom to stream down.One section biological mixed bed bottom, most of sewage advances the first raising mixed gas and liquid pipe again and promotes, and small part enters two sections biological mixed beds from the bottom.
Enter the sewage of two sections biological mixed beds, enter in the pipe from lower port when the second raising mixed gas and liquid pipe rises with pressurized air again from second blast main, and the upwelling that forms gas-liquid mixed rises along the second raising mixed gas and liquid pipe, the upwelling of gas-liquid mixed flows out from the upper port of the second raising mixed gas and liquid pipe, most of sewage is got back to biological mixed bed bottom to the dirty floating stuffing that passes again, and small part sewage enters settling tank by thrust-augmenting nozzle.
Under compressed-air actuated castering action from blast main, sewage circulates up and down in one section biological mixed bed and two sections biological mixed beds, and pass floating stuffing in the biological mixed bed repeatedly, what form in floating stuffing is following to air water mixed flow and the abundant contact-impact of upward flow sewage, realize oxygen by the conduction of sewage, utilize biomembranous absorption, oxidation, Decomposition to remove pollutants in sewage to floating stuffing surface biological film.
Sewage after biochemical treatment enters settling tank by thrust-augmenting nozzle from two sections biological mixed beds, at the inner eddy flow that forms muddy water mixed solution of settling tank, the mud that returns from settling tank bottom stops through traverse baffle and returns the settling tank bottom, realize mud-water separation, water after the upper strata clear water of settling tank is promptly handled flows out through the aperture on the effluent weir riser, again through settling tank posticum gravity flow discharging.Mud in the sewage is at settling tank bottom settlings, concentrated, enter in the pipe from lower port when reflux sludge tube rises with pressurized air from the settling tank blast main, and formation mud blended upwelling rises along reflux sludge tube, extension tube through reflux sludge tube enters one section biological mixed bed and pretreatment pool respectively again, and further circulation mixes and the promotion biochemical action.
The related waste disposal plant of the utility model rationally utilizes wind energy, does not have power consumption, satisfies original intention and self demand to the energy that environmental protection facility is preserved the ecological environment, has the characteristics of obvious energy-saving and environmental protection in the small-scale sewage process field.
Waste disposal plant of the present utility model utilizes the microbial film on the floating stuffing to be easy to growth and breeding, and the characteristics of longer microorganism generation time that can grow improve the device capacity of resisting impact load; Sewage purification process is divided into placed in-line two sections biological mixed beds, all multiply and enter the microorganism that this section sewage quality adapts for every section, and form the advantage kind, help the degraded with organic pollutant given full play to of microorganism metabolic function, assurance device effluent quality stable.
The inner no any movable part of the utility model device, management is simple, arranges compactness, suitable the wind energy resources abundant relatively medium and small station of railway and other respective site of being arranged on.
Description of drawings
Fig. 1 is a basic structure synoptic diagram of the present utility model;
Fig. 2 is an integration biological treatment device cross-sectional view of the present utility model;
Fig. 3 is a Gas flow-limiting pressure reducer cross-sectional view of the present utility model.
Description of symbols among the figure:
A, wind energy conversion system B, gas-holder
C1, the first Gas flow-limiting pressure reducer C2, the second Gas flow-limiting pressure reducer
C3, the 3rd Gas flow-limiting pressure reducer C4, the 4th Gas flow-limiting pressure reducer
D, pretreatment pool E, integration biological treatment device
I, one section biological mixed bed II, two sections biological mixed beds
III, settling tank
1, air output tube 2, pretreatment pool blast main
3, sewage riser tube 4, partition wall
5, reflux sludge tube 6, first blast main
7, the first raising mixed gas and liquid pipe 8, second blast main
9, the second raising mixed gas and liquid pipe 10, thrust-augmenting nozzle
11, settling tank blast main 12, floating stuffing
13, tackle net 14 on, prop up backplate down
15, traverse baffle 16, effluent weir
17, rising pipe 18, air filter
19, gas receiving chamber 20, nozzle
21, gas mixing chamber 22, gas diffusion chamber.
Embodiment
In conjunction with the accompanying drawings the technical solution of the utility model is further described.Fig. 1 and Fig. 2 have shown basic structure of the present utility model, and Fig. 3 has shown the basic structure of the Gas flow-limiting pressure reducer among Fig. 1 and Fig. 2.
As shown in the figure, wind energy driving Small Sewage Treatment Equipment described in the utility model comprises air feeder, pretreatment pool D and integration biological treatment device E.Air feeder comprises wind energy conversion system A, gas-holder B, and wind energy conversion system A connects gas-holder B by wind conveying pipe, and the wind wheel blade of wind energy conversion system A rotates in the wind, drives wind-force pneumatics pump and produces pressurized gas, is transported in the gas-holder B.Gas-holder B is connected with integration biological treatment device E with pretreatment pool D by air output tube 1, integration biological treatment device E comprises one section biological mixed bed I being set up in parallel in the casing, two sections biological mixed bed II and settling tank III, and two sections biological mixed bed II place between one section biological mixed bed I and the settling tank III.The water-in of pretreatment pool D connects source of sewage, water outlet is by the water-in of one section biological mixed bed I of pipe connection, one section biological mixed bed I and two sections biological mixed bed II bottoms are communicated with, two sections biological mixed bed II and settling tank III are communicated with by thrust-augmenting nozzle 10, and the water outlet of settling tank III places on the casing of integration biological treatment device E and by rising pipe 17 and external communications.
Be provided with respectively in one section biological mixed bed I and the two sections biological mixed bed II floating stuffing 12, raising mixed gas and liquid pipe, on tackle net 13, prop up backplate 14 and blast main down, floating stuffing 12 is arranged on going up between an interception net 13 and the following backplate 14 of middle part in the mixed bed.
Have in one section biological mixed bed I in 6, two sections biological mixed bed II of the first raising mixed gas and liquid pipe 7 and first blast main second raising mixed gas and liquid pipe 9 and second blast main 8 are arranged.First blast main 6 enters one section biological mixed bed I and is inserted in the first raising mixed gas and liquid pipe 7 from the casing outside, and reaching the bottom of the first raising mixed gas and liquid pipe 7, the epimere of first blast main 6 connects the air output tube 1 of air feeder gas-holder by the second Gas flow-limiting pressure reducer C2.Second blast main 8 enters two sections biological mixed bed II and is inserted in the second raising mixed gas and liquid pipe 9 from the casing outside, and reaching the bottom of the second raising mixed gas and liquid pipe 9, the epimere of second blast main 8 connects the air output tube 1 of air feeder gas-holder by the 3rd Gas flow-limiting pressure reducer C3.
Pretreatment pool D inside is provided with partition wall 4, and pretreatment pool D is divided into two sections of front and back, and the water-in that connects source of sewage is arranged on the leading portion sidewall.Partition wall 4 tops are provided with water hole, and leading portion and back segment in the pretreatment pool D are communicated with.Pretreatment pool D back segment vertically is provided with sewage riser tube 3 and pretreatment pool blast main 2, and sewage riser tube 3 lower port place the bottom of pretreatment pool D, and the upper port of sewage riser tube 3 connects the water-in of one section biological mixed bed I by extension tube.Pretreatment pool blast main 2 enters pretreatment pool D from top and inserts in sewage riser tube 3 lower port, and pretreatment pool blast main 2 epimeres connect the air output tube 1 of air feeder gas-holder by the first Gas flow-limiting pressure reducer C1.
Thrust-augmenting nozzle 10, pretreatment pool blast main 11, reflux sludge tube 5, traverse baffle 15, effluent weir 16 are set in the pretreatment pool III, and thrust-augmenting nozzle 10, pretreatment pool blast main 11, reflux sludge tube 9 are for vertically being inserted in the pipe in the settling tank III respectively.The upper end of thrust-augmenting nozzle 10 is communicated with the water outlet on two sections biological mixed bed II tops, and the lower end places the bottom of settling tank III, and lower end water outlet and level are to being 45 ° of angles.Many thrust-augmenting nozzles 10 are evenly distributed in tank wall one side of separating two sections biological mixed bed II and settling tank III, and many thrust-augmenting nozzles 10 are the 3-5 root.Reflux sludge tube 5 lower port place the bottom of settling tank III, and reflux sludge tube 5 epimeres pass settling tank III and are connected to the muddy water import on one section biological mixed bed I top and the muddy water import on pretreatment pool D top.Pretreatment pool blast main 11 enters settling tank III and is inserted into reflux sludge tube 5 bottoms from the casing outside, the epimere of pretreatment pool blast main 11 connects the air output tube 1 of air feeder gas-holder by the 4th Gas flow-limiting pressure reducer C4.
Effluent weir comprises riser and leveling board two portions, and along continuous straight runs is evenly arranged gully-hole on the riser.The traverse baffle 15 oblique effluent weir riser bottoms of being fixed in.
At inboard setting of the settling tank III tank wall that sets out water pipe 17 and the wide effluent weir 16 of this tank wall, effluent weir 16 comprises riser and leveling board two portions, and along continuous straight runs is evenly arranged gully-hole on the riser.Effluent weir 16 bottoms are provided with traverse baffle 15, traverse baffle 15 oblique being fixed on the effluent weir 16 riser bottoms, and traverse baffle 15 is wide with effluent weir 16 risers.
Gas flow-limiting pressure reducer C1, C2, C3, C4 are the cylinder of hollow and the parts of round platform unitized construction, the pressure and the flow that are used to control compressed-air actuated work output and import pretreatment pool D, one section biological mixed bed I, two sections interior gases of biological mixed bed II, settling tank III.
Gas flow-limiting pressure reducer C1, C2, C3, C4 comprise nozzle 20, gas receiving chamber 19, gas mixing chamber 21, gas diffusion chamber 22 respectively.The inner chamber of gas receiving chamber 19, gas mixing chamber 21, gas diffusion chamber 22 is communicated with, and gas mixing chamber 21 places between gas receiving chamber 19 and the gas diffusion chamber 22, and an end of gas mixing chamber 21 connects gas receiving chamber 19, and the other end connects gas diffusion chamber 22.The internal diameter of gas receiving chamber 19 is greater than the internal diameter of gas mixing chamber 21,22 one-tenth hydraucone shapes of gas diffusion chamber, and the outlet of gas diffusion chamber 22 is connected with the blast main of integration biological treatment device E with pretreatment pool D.Nozzle 20 is set in the gas receiving chamber 19, and nozzle 20 is connected with gas-holder B, and the sidewall of gas receiving chamber 19 is provided with the injection air suction inlet, and air filter 18 is installed on the injection air suction inlet.
The first Gas flow-limiting pressure reducer C1 will be from the air of nozzle and injection air mixed after pretreatment pool blast main 2 be sent into pretreatment pool D, the second Gas flow-limiting pressure reducer C2 will be from the air of nozzle and injection air mixed after first blast main 6 be sent into one section biological mixed bed I pond, the 3rd Gas flow-limiting pressure reducer C3 will be from the air of nozzle and injection air mixed after second blast main 8 be sent into two sections biological mixed bed II, the 4th Gas flow-limiting pressure reducer C4 will be from the air of nozzle and injection air mixed after settling tank blast main 11 be sent into settling tank III, for providing air water, mixes and the round-robin motivating force by waste disposal plant, for sewage being carried out the microorganism oxygen supply of biochemical action.
Claims (6)
1. a wind energy drives Small Sewage Treatment Equipment, it is characterized in that: described wind energy drives Small Sewage Treatment Equipment and comprises air feeder, pretreatment pool (D) and integration biological treatment device (E), air feeder comprises wind energy conversion system (A), gas-holder (B), wind energy conversion system (A) connects gas-holder (B) by wind conveying pipe, the pressurized gas that wind energy conversion system (A) drives the generation of wind-force pneumatics pump is transported in the gas-holder (B), and gas-holder (B) is connected with integration biological treatment device (E) with pretreatment pool (D) by air output tube (1); Integration biological treatment device (E) comprises one section biological mixed bed (I), two sections biological mixed beds (II) and the settling tank (III) that is set up in parallel in the casing, and two sections biological mixed beds (II) place between one section biological mixed bed (I) and the settling tank (III); The water-in of pretreatment pool (D) connects source of sewage, water outlet is by the water-in of one section biological mixed bed of pipe connection (I), one section biological mixed bed (I) and two sections biological mixed beds (II) bottom are communicated with, two sections biological mixed beds (II) and settling tank (III) are communicated with by thrust-augmenting nozzle (10), and the water outlet of settling tank (III) places on the casing of integration biological treatment device (E) and by rising pipe (17) and external communications; In one section biological mixed bed (I) and the two sections biological mixed beds (II) floating stuffing (12), raising mixed gas and liquid pipe and blast main are set respectively, floating stuffing (12) is arranged on the middle part in the mixed bed, the raising mixed gas and liquid pipe is vertically disposed pipe, blast main enters and is inserted in the raising mixed gas and liquid pipe from the casing outside, and the blast main epimere connects the air output tube (1) of air feeder gas-holder (B) by the Gas flow-limiting pressure reducer.
2. drive Small Sewage Treatment Equipment according to the wind energy described in the claim 1, it is characterized in that: described pretreatment pool (D) inside is provided with partition wall (4), pretreatment pool (D) is divided into two sections of front and back, the water-in that connects source of sewage is arranged on the leading portion sidewall, partition wall (4) top is provided with water hole, and leading portion and back segment in the pretreatment pool (D) are communicated with; Pretreatment pool (D) back segment vertically is provided with sewage riser tube (3) and pretreatment pool blast main (2), sewage riser tube (3) lower port places the bottom of pretreatment pool (D), the upper port of sewage riser tube (3) connects the water-in of one section biological mixed bed (I) by extension tube, pretreatment pool blast main (2) enters pretreatment pool (D) from top and inserts in sewage riser tube (3) lower port, and pretreatment pool blast main (2) epimere connects the air output tube (1) of air feeder gas-holder by Gas flow-limiting pressure reducer (C1).
3. drive Small Sewage Treatment Equipment according to the wind energy described in the claim 1, it is characterized in that: the floating stuffing (12) in one section biological mixed bed (I) and the two sections biological mixed beds (II) is set in parallel between an interception net (13) and the following backplate (14); The first raising mixed gas and liquid pipe (7) and first blast main (6) are set in one section biological mixed bed (I), the second raising mixed gas and liquid pipe (9) and second blast main (8) are arranged in two sections biological mixed beds (II); First blast main (6) enters one section biological mixed bed (I) from the casing outside and is inserted in the first raising mixed gas and liquid pipe (7), and reaching the bottom of the first raising mixed gas and liquid pipe (7), the epimere of first blast main (6) connects the air output tube (1) of air feeder gas-holder by the second Gas flow-limiting pressure reducer (C2); Second blast main (8) enters two sections biological mixed beds (II) from the casing outside and is inserted in the second raising mixed gas and liquid pipe (9), and reaching the bottom of the second raising mixed gas and liquid pipe (9), the epimere of second blast main (8) connects the air output tube (1) of air feeder gas-holder by the 3rd Gas flow-limiting pressure reducer (C3).
4. drive Small Sewage Treatment Equipment according to the wind energy described in the claim 1, it is characterized in that, thrust-augmenting nozzle (10) is set in the described settling tank (III), settling tank blast main (11), reflux sludge tube (5), traverse baffle (15), effluent weir (16), thrust-augmenting nozzle (10), settling tank blast main (11), reflux sludge tube (5) is for vertically being inserted in the pipe in the settling tank (III) respectively, the upper end of thrust-augmenting nozzle (10) is communicated with the water outlet on two sections biological mixed beds (II) top, the lower end places the bottom of settling tank (III), thrust-augmenting nozzle (10) lower end water outlet and level are to being 45 ° of angles, many thrust-augmenting nozzles (10) are evenly distributed in tank wall one side of separating two sections biological mixed beds (II) and settling tank (III), and many thrust-augmenting nozzles (10) are the 3-5 root; Reflux sludge tube (5) lower port places the bottom of settling tank (III), and reflux sludge tube (5) epimere passes settling tank (III) and is connected to the muddy water import on one section biological mixed bed (I) top and the muddy water import on pretreatment pool (D) top; Settling tank blast main (11) enters settling tank (III) and is inserted into reflux sludge tube (5) bottom from the casing outside, the epimere of settling tank blast main (11) connects the air output tube (1) of air feeder gas-holder by Gas flow-limiting pressure reducer (C4).
5. drive Small Sewage Treatment Equipment according to the wind energy described in the claim 1, it is characterized in that, at inboard setting of the tank wall of the settling tank that sets out water pipe (17) (III) and the wide effluent weir (16) of this tank wall, effluent weir (16) comprises riser and leveling board two portions; Along continuous straight runs is evenly arranged gully-hole on effluent weir (16) riser, the oblique fixedly traverse baffle in bottom (15) of effluent weir (16) riser, and traverse baffle (15) is wide with effluent weir (16) riser.
6. drive Small Sewage Treatment Equipment according to the wind energy described in the claim 1, it is characterized in that, described Gas flow-limiting pressure reducer comprises nozzle (20), gas receiving chamber (19), gas mixing chamber (21), gas diffusion chamber (22), the inner chamber of gas receiving chamber (19), gas mixing chamber (21), gas diffusion chamber (22) is communicated with, gas mixing chamber (21) places between gas receiving chamber (19) and the gas diffusion chamber (22), one end of gas mixing chamber (21) connects gas receiving chamber (19), and the other end connects gas diffusion chamber (22); The internal diameter of gas receiving chamber (19) is greater than the internal diameter of gas mixing chamber (21), and gas diffusion chamber (22) becomes the hydraucone shape, and the outlet of gas diffusion chamber (22) is connected with the blast main of pretreatment pool (D) with integration biological treatment device (E); Nozzle (20) is set in the gas receiving chamber (19), and nozzle (20) is connected with gas-holder (B), and the sidewall of gas receiving chamber (19) is provided with the injection air suction inlet, and air filter (18) is installed on the injection air suction inlet.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011200817866U CN202080985U (en) | 2011-03-25 | 2011-03-25 | Mini-type sewage-disposal device driven by wind power energy |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011200817866U CN202080985U (en) | 2011-03-25 | 2011-03-25 | Mini-type sewage-disposal device driven by wind power energy |
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| Publication Number | Publication Date |
|---|---|
| CN202080985U true CN202080985U (en) | 2011-12-21 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011200817866U Expired - Lifetime CN202080985U (en) | 2011-03-25 | 2011-03-25 | Mini-type sewage-disposal device driven by wind power energy |
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| Country | Link |
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| CN (1) | CN202080985U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102173543A (en) * | 2011-03-25 | 2011-09-07 | 铁道第三勘察设计院集团有限公司 | Wind driven small sewage treatment device |
-
2011
- 2011-03-25 CN CN2011200817866U patent/CN202080985U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102173543A (en) * | 2011-03-25 | 2011-09-07 | 铁道第三勘察设计院集团有限公司 | Wind driven small sewage treatment device |
| CN102173543B (en) * | 2011-03-25 | 2012-10-10 | 铁道第三勘察设计院集团有限公司 | Wind driven small sewage treatment device |
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