CN206069520U - A kind of integrated waste-water treater for livestock and poultry breeding industry - Google Patents

A kind of integrated waste-water treater for livestock and poultry breeding industry Download PDF

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Publication number
CN206069520U
CN206069520U CN201621107226.2U CN201621107226U CN206069520U CN 206069520 U CN206069520 U CN 206069520U CN 201621107226 U CN201621107226 U CN 201621107226U CN 206069520 U CN206069520 U CN 206069520U
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chamber
anaerobic reaction
reaction chamber
livestock
connectedness
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CN201621107226.2U
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刘情生
钟世民
曾郴林
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刘情生
钟世民
曾郴林
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Abstract

The utility model discloses a kind of integrated waste-water treater for livestock and poultry breeding industry, including control room, equipment for separating liquid from solid;Equipment for separating liquid from solid liquid outlet is connected with drain pipe, and drain pipe is drained to the waste water after solid-liquid separation in the first anaerobic reaction chamber;Deadening plate is installed in the first anaerobic reaction chamber, plate deadened and the first anaerobic reaction chamber is divided into into the front compartment and rear compartment that two bottoms are connected by convective tank;Deaden plate to be provided with toward the inclined folding surface in corner inclined-plane in convective tank one end;First anaerobic reaction top of chamber is connected with the second anaerobic reaction top of chamber by connectedness;Second anaerobic reaction top of chamber is connected with the 3rd anaerobic reaction top of chamber also by connectedness;3rd anaerobic reaction top of chamber is connected with the first aerobic reaction top of chamber by connectedness;First aerobic reaction bottom of chamber portion is connected with the second aerobic reaction chamber bottom by connectedness, and the second aerobic reaction chamber bottom is connected with the 3rd aerobic reaction bottom of chamber portion by connectedness.

Description

A kind of integrated waste-water treater for livestock and poultry breeding industry
Technical field
This utility model is related to a kind of sewage treatment equipment, and more particularly to a kind of integration for livestock and poultry breeding industry is given up Water treatment facilities.
Background technology
With the raising of people's environmental protection consciousness, nowadays wastewater treatment has been important one in environmental conservation Ring, which mainly does to waste water after purified treatment and discharges again, prevents the Organic substance in waste water, virus etc. from leaking, to reach The purpose of water conservation.
And livestock and poultry breeding industry is used as the important generation ground of waste water, and there is the features such as being mainly feces of livestock and poultry in its waste water, therefore Need using the wastewater treatment equipment and technique being adapted with its feature.
In Publication No. CN105271610A, a kind of entitled Chinese invention of plant's cow manure wastewater integrated conduct method is special A kind of handling process for cow manure wastewater is disclosed in profit mainly to be included, solid-liquid separation, Impurity removal, anaerobic treatment, aerobic The step such as process, be designed the characteristics of which is directed to cow manure wastewater, and achieve good using effect.
A kind of culturing wastewater processing system is disclosed in the Chinese invention patent application of Publication No. CN105152473A And its method, its process step substantially is essentially identical with above-mentioned patent.
But, currently used for the wastewater treatment equipment of livestock and poultry breeding industry, to there is impact resistance poor, and anaerobic and aerobic process is not The problems such as enough thorough, easy blocking short circuits.Trace it to its cause, the concentration ratio of mainly this kind of waste water is larger, Organic substance is too many, if If processing simply by an anaerobic and aerobic, its clean-up effect is very limited.And, if during purified treatment not Using stream-handling, equipment blocking short circuit is also easily caused, the normal operation of equipment is had a strong impact on.
Therefore it is applicant's understanding that designing one kind possesses multistage anaerobic and Aerobic Process for Treatment storehouse, and it is prevented from the waste water of short circuit Processing meanss are very necessary, can solve the problem that various problems present in current livestock and poultry breeding industry wastewater treatment.
Utility model content
In view of the drawbacks described above of prior art, technical problem to be solved in the utility model is to provide a kind of for raiseeing The integrated waste-water treater of poultry breeding industry, which can carry out multistage anaerobic and aerobic and process to waste water, and can also prevent Only blocking, short circuit.
For achieving the above object, this utility model provides a kind of integrated wastewater treatment dress for livestock and poultry breeding industry Put, including control room, equipment for separating liquid from solid, described control interior are provided with oxygenerator;
The inlet of described equipment for separating liquid from solid, slag-drip opening, liquid outlet are connected with feed tube, scum pipe, drain pipe respectively Connect, described drain pipe is drained to the waste water after solid-liquid separation in the first anaerobic reaction chamber;
Deadening plate is installed in the first described anaerobic reaction chamber, the first anaerobic reaction chamber is divided into by described deadening plate Front compartment and rear compartment that two bottoms are connected by convective tank;
Described deadening plate is provided with toward the inclined folding surface in corner inclined-plane in convective tank one end;
The first described anaerobic reaction top of chamber is connected with the second anaerobic reaction top of chamber by connectedness;
The second described anaerobic reaction top of chamber is connected with the 3rd anaerobic reaction top of chamber also by connectedness;
The 3rd described anaerobic reaction top of chamber is connected with the first aerobic reaction top of chamber by connectedness;
The first described aerobic reaction bottom of chamber portion is connected with the second aerobic reaction chamber bottom by connectedness, and described second Aerobic reaction bottom of chamber portion is connected with the 3rd aerobic reaction bottom of chamber portion by connectedness.
Used as further improvement of the utility model, described equipment for separating liquid from solid is solid-liquid separating machine.
Used as further improvement of the utility model, described connectedness is connecting pipe or cell body, opening.
Used as further improvement of the utility model, described the first anaerobic reaction chamber, the second anaerobic reaction chamber, the 3rd detest Gas skirt is provided with the top of oxygen reaction chamber.
Used as further improvement of the utility model, the first described aerobic reaction top of chamber is provided with blender, described Blender puddler stretch into the first aerobic reaction chamber in and described puddler on be fixed with stirring vane and aeration plate;Institute The aeration plate stated connects to be introduced in aeration plate with the oxygen for producing oxygenerator by trachea with oxygenerator carries out aeration.
Used as further improvement of the utility model, described puddler is hollow state, and trachea loads the interior of puddler Kong Zhongwei aeration plates are supplied.
Used as further improvement of the utility model, the 3rd described aerobic reaction top of chamber is by connectedness and precipitation chamber Top connection, described precipitation top of chamber are provided with discharge outlet, and described discharge outlet is connected with drain pipe;Described precipitation bottom of chamber portion Be additionally provided with two down relative tilt lead mud inclined-plane, described precipitation bottom of chamber portion is additionally provided with mud discharging mouth.
Used as further improvement of the utility model, described the first anaerobic reaction chamber, the second anaerobic reaction chamber, the 3rd detest Oxygen reaction cavity configuration is identical.
It is as further improvement of the utility model, described the first aerobic reaction chamber, the second aerobic reaction chamber, the 3rd good Oxygen reaction cavity configuration is identical.
As further improvement of the utility model, described puddler, including the body of rod, the described body of rod are provided with close Sealing groove, the first slot rolling, inside air channel, and the described body of rod it is passage;
Sealing ring is installed in described seal groove;The first described slot rolling and ball engagement;
Two envelope gas hoods are the symmetrical structure of two structures, and its section for cooperating is a complete annulus;
Described envelope gas hood, including, the gentle cavity shell part in mounting portion, described mounting portion are provided with spherical pore, Ball is installed in described spherical pore;
On the outside of described mounting portion with mounting ring on the inside of by threaded engagement assemble;
Air cavity is provided with the inside of described air cavity housing parts;
Air cavity of one of envelope gas hood is connected with connecting tube, described connecting tube for oxygenerator output oxygen Pipeline communication;
The described body of rod is provided with air channel on air cavity part;
Two envelope gas hoods after Screw assembly ring screws assembling pass through to compress sealing ring and the body of rod on the inside of two envelope gas hoods Between realize sealing;
By being mutually adjacent to realization sealing between two envelope gas hoods.
The beneficial effects of the utility model are:
1st, this utility model simple structure, purification efficiency and degree of purification are high, substantially increase the discharge standard of waste water, energy Enough effective protection environment, or even the waste water after processing can directly be reclaimed and be reused.
2nd, this utility model carries out aerobic and anaerobic reaction using multistage anaerobic chamber and aerobic cavity so that each reaction chamber energy It is enough that the bacterium colony for most adapting to the reaction chamber is tamed out according to the characteristics of waste water, effectively increase clean-up effect.
3rd, this utility model adopts pure oxygen aeration, can greatly improve oxygen molecule activity, so as to improve the effect of aerobic reaction Rate, and reduce the yield of sludge.
Description of the drawings
Fig. 1 is a kind of knot of the integrated waste-water treater specific embodiment for livestock and poultry breeding industry of this utility model Structure schematic diagram.
Fig. 2 is a kind of stirring for integrated waste-water treater specific embodiment for livestock and poultry breeding industry of this utility model Mix bar structural representation.
Fig. 3 is a kind of stirring for integrated waste-water treater specific embodiment for livestock and poultry breeding industry of this utility model Mix bar structural representation.
Fig. 4 is a kind of stirring for integrated waste-water treater specific embodiment for livestock and poultry breeding industry of this utility model Mix bar structural representation.
Fig. 5 is the enlarged drawing of F1 in Fig. 4.
Specific embodiment
The utility model is described in further detail with reference to the accompanying drawings and examples:
Referring to Fig. 1, a kind of integrated waste-water treater for livestock and poultry breeding industry, including control room 100, solid-liquid point Oxygenerator 101 is provided with device 200, described control room 100;
The inlet of described equipment for separating liquid from solid 200, slag-drip opening, liquid outlet respectively with feed tube 201, scum pipe 202, Drain pipe 203 connects, and described drain pipe 203 is drained to the waste water after solid-liquid separation in the first anaerobic reaction chamber 401;
Described equipment for separating liquid from solid 200 carries out solid-liquid separation for the waste water that will be entered from feed tube 201, wherein separating Solid out is discharged from scum pipe 202, liquid is entered in the first anaerobic reaction chamber 401 from drain pipe 203.Described solid-liquid point Can be solid-liquid separating machine from device 200.
Deadening plate 701 is installed in the first described anaerobic reaction chamber 401, described deadening plate 701 will be the first anaerobism anti- Chamber 401 is answered to be divided into two bottoms to pass through front compartment 410 and the rear compartment 411 that convective tank 706 is connected;
Described deadening plate 701 is provided with toward 901 inclined folding surface 705 of corner inclined-plane in 706 one end of convective tank;Described Folding surface 705 is prevented from the sludge of 410 bottom of front compartment and is directly entered in rear compartment 411, causes convective tank 706 to block;
Connected with the top of the second anaerobic reaction chamber 402 by connectedness 800 at the top of the first described anaerobic reaction chamber 401; Described connectedness 800 can be connecting pipe or cell body, opening etc., for two cavitys are connected;
Also by connecting at the top of connectedness 800 and the 3rd anaerobic reaction chamber 403 at the top of the second described anaerobic reaction chamber 402 It is logical;
Described the first anaerobic reaction chamber 401, the second anaerobic reaction chamber 402, the complete phase of 403 structure of the 3rd anaerobic reaction chamber Together;And the first described anaerobic reaction chamber 401, the second anaerobic reaction chamber 402, it is provided with gas collection at the top of the 3rd anaerobic reaction chamber 403 Cover 300, described gas skirt 300 is for by the first anaerobic reaction chamber 401, the second anaerobic reaction chamber 402, the 3rd anaerobic reaction chamber The gases such as the biogas produced by 403 are collected, and are then drawn by exhaustor 301 and use or store.
During use, waste water can be introduced in front compartment 410, then carry out reacting and gradually dirty in front compartment 410, most Flowed in rear compartment 411, when after entering in compartment 411 by convective tank 706 afterwards, convection current can be formed at convective tank 706, this Sludge in rear compartment 411 can just can slide to 410 bottom of front compartment, finally by spoil disposal downwards along corner inclined-plane 901 Bank of tubes goes out, and prevents sludge blockage convective tank 706 from causing short circuit.
This wastewater treatment equipment passes through the first anaerobic reaction chamber 401, the second anaerobic reaction chamber 402, the 3rd anaerobic reaction chamber 403 three-level anaerobic treatment, it is possible to increase the anaerobic treatment time of waste water, and per grade progressively purify, and can greatly improve purification Degree.
A series of vertically arranged deadening plates used in each anaerobic reaction chamber, can make processed waste water on reaction intracavity edge Deaden plate to flow up and down, by means of the biogas that intracavity generation is reacted in processing procedure make the microbial solid of reaction intracavity every Make to expand in each compartment that baffle-wall is formed up and down and precipitate motion, and the current of intracavity are entirely reacted then with slower speed Make bottom horizontal flow sheet.
As waste water is in the presence of plate is deadened, current make current in the total of the flow path of reaction intracavity around plate flowing is deadened Length increases, and deadens the stop of plate and the settlement action of sludge in addition, and biosolids are effectively trapped in reaction intracavity.Together After baffle-wall low side arrange a corner inclined-plane, so as to promote water distribution uniformity, reduce dead band, make waste water in upward flow room more It is evenly distributed and promotes good muddy water to mix.
Stop and compartmentation due to deadening plate up and down, makes fluidised form of the current in different compartments be in be thoroughly mixed state (The rising of current and the stirring action of aerogenesis), and plug-flow state is then shown as in the whole flow process direction of reaction chamber.It is dynamic from reaction From the perspective of mechanics, this compound fluidised form combined with plug-flow that is thoroughly mixed is very beneficial to ensure the volume profit of reaction chamber With rate, the stability that treatment effect and promotion run is improved, be a kind of splendid flow patterns.Meanwhile, in certain disposal ability Under, this reaction chamber volume needed for compound fluidised form is also much lower than the single reaction chamber volume for being thoroughly mixed formula.
The unique cell structure in each anaerobic reaction chamber and pulling flow type fluidised form can tame culture in causing each reaction chamber Go out the superior microorganism population being adapted with the waste water quality, environmental condition flowing in the reaction chamber.For example positioned at reaction chamber In the front compartment of front end, mainly based on hydrolysis and acid-producing bacteria, and in the rear compartment of the reaction chamber behind relatively, then with methane backeria Based on.For methane backeria, with the passage of compartment, its population from based on Sarcina gradually to methanothrix sp category, heterotrophism first Alkane bacterium and Desulfovibrio etc. change, and so by the change of room, are that superior microorganism population is able to good growth and breeding, make to give up Pollutant in water are degraded in different compartments respectively.
The 3rd described anaerobic reaction top of chamber is connected with the top of the first aerobic reaction chamber 501 by connectedness 800, described The first aerobic reaction chamber 501 at the top of blender 707 is installed, it is aerobic that the puddler 704 of described blender 707 stretches into first Stirring vane 703 and aeration plate 702 are fixed with reaction chamber 501 and on described puddler 704;Described aeration plate 702 leads to Crossing trachea and connecting with oxygenerator 101 carries out aeration so that the oxygen that oxygenerator 101 is produced is introduced in aeration plate 702;
Described puddler 704 is preferably hollow state, is aeration plate during now trachea can load the endoporus of puddler 704 702 supply;
Described 501 bottom of the first aerobic reaction chamber is connected with 502 bottom of the second aerobic reaction chamber by connectedness 800, Described 502 bottom of the second aerobic reaction chamber is connected with 503 bottom of the 3rd aerobic reaction chamber by connectedness 800;
Described the first aerobic reaction chamber 501, the second aerobic reaction chamber 502, the complete phase of 503 structure of the 3rd aerobic reaction chamber Together.
Waste water is imported at the top of the first aerobic reaction chamber 501 by connector 800 at the top of the 3rd described anaerobic cavity 403, And waste water to be imported 501 bottom of the first aerobic reaction chamber the structure of 502 bottom of the second aerobic reaction chamber by connector 800, Possesses following benefit:
The aeration plate in the first aerobic reaction chamber 501 is located at its bottom, the waste water meeting entered from the 3rd anaerobic reaction chamber 403 Fully mix with the waste water in the first aerobic reaction chamber in the presence of aeration, finally just the second aerobic reaction chamber is entered from bottom In, this can increase the time of staying of waste water in the first aerobic reaction chamber and with aerobic bacteria time of contact, improve its purification efficiency.
The 3rd described aerobic reaction top of chamber is connected with precipitation top of chamber by connector 800 and can similarly increase useless Purification efficiency of the water in the 3rd aerobic reaction chamber.
Described the first aerobic reaction chamber 501, the second aerobic reaction chamber 502, the 3rd aerobic reaction chamber 503 adopt oxygenerator The 101 direct aerations of pure oxygen for producing, are pure oxygen aeration activated sludge process, also known as oxygen-enriched aeration activated sludge process, due in air The content of oxygen is only 21%, and the content in pure oxygen is 90%~95%, and partial pressure of oxygen is higher than air 4.4~4.7 times, is carried out with pure oxygen Aeration, can improve oxygen to the transmission capacity in waste water.
The major advantage of pure oxygen aeration activated sludge process is as follows.
(1)Coefficient of oxygen utilization is up to 80%~90%, and blast aeration system is only 10% or so.
(2)In Aeration tank, the MLSS values of mixed liquor may be up to 4000~7000mg/L, it is possible to increase the volume of Aeration tank is born Lotus.
(3)In Aeration tank, the SVI values of mixed liquor are relatively low, are generally lower than 100, and it is less that sludge bulking phenomenon occurs.
(4)In pure oxygen, the intrinsic standoff ratio air of oxygen is about high 5 times, the transfer efficiency that pure oxygen aeration can be carried significantly.
(5)The rate of transform of oxygen can bring up to 80-90%, and general blast aeration is only 10% or so.
(6)Activated sludge concentration in Aeration tank can be made to be up to 4000 ~ 7000mg/l, the volume of Aeration tank can be greatly improved Load
(7)Excess sludge production is few, and SVI values are also low, typically the worry without sludge bulking.Pure oxygen aeration develops speed abroad Degree is of wide application general very much, but the application in China is mainly with petroleum chemical industry as break-through point, according to external experience Pure oxygen aeration also has extensive prospect in terms of municipal wastewater reason, develops traditional sludge method rapidly and will there is exposure with economical Gas is limited in one's ability, and processing equipment is huge to wait not enough.As the pressure of pure oxygen is higher than the partial pressure of oxygen in air, pure oxygen aeration can be notable The transfer rate of oxygen is improved, the deficiency of traditional activated sludge process can obviously improve using pure oxygen aeration.
Using live variable-pressure adsorption equipment(Oxygenerator)The operating cost of the IS-O pure oxygen aeration technologies of oxygen processed is less than normal The blast aeration mode of rule, it is especially even more so where electricity charge level is higher.
Air aeration is replaced using pure oxygen (or oxygen-enriched), the concentration of dissolved oxygen can be neatly adjusted according to technological requirement, Make aeration system process that there is good performance.The transfer rate of motive force and oxygen of the oxygen in water is significantly improved, to active dirty The penetration power of mud granule is strong.As the MLSS in pure oxygen aeration pond is far above blast aeration tank, in equal wastewater treatment capacity situation Under, the hydraulic detention time and volume in pure oxygen aeration pond are far below blast aeration tank.The noise of pure oxygen aeration system is far below drum Wind aerating system, is also substantially absent from the gas escape of VOC (VOC), reduces waste water treatment plant to week The adverse effect in collarette border.
Operation result shows, in terms of aeration time, the volume of Aeration tank and floor space, during the aeration of pure-oxygen aeration method Between generally air aeration method 1/3 ~ 1/4, therefore the volume of Aeration tank also just 3 ~ 4 times of difference, the total floor space for the treatment of plant can Save 20% or so;In terms of the energy, the energy consumption of pure-oxygen aeration method saves 30% or so, economic operating cost 10% ~ 20%;In capital cost The capital cost of aspect pure-oxygen aeration method saves 10% ~ 20%, sludge output few 30% or so.
This utility model using three-level aerobic cavity process by the way of, according to other following characteristics:
(1), respectively along tank body segmentation injection aeration chamber, organic loading distribution is more balanced for pure oxygen, improve keeping speed with Contradiction between aerobic speed, advantageously reduces energy consumption;
(2)Waste water segmentation injection, improves the adaptability of Aeration tank impact load;
(3)The also tail gas containing pure oxygen in the waste gas of discharge, can be recycled into each oxygen aeration chamber, further by air exhauster Improve content in water;
(4)Activated sludge concentration in mixed liquor is gradually reduced along pond length, and the sludge for going out to flow mixed liquor is relatively low, is mitigated secondary The load of sedimentation tank, is conducive to improving secondary sedimentation tank solid, liquid separating effect.
Connected with the top of precipitation chamber 600 by connectedness 800 at the top of the 3rd described aerobic reaction chamber 503, described is heavy Discharge outlet is provided with the top of shallow lake chamber 600, described discharge outlet is connected with drain pipe 601;Described 600 bottom of precipitation chamber is additionally provided with two Individual down relative tilt leads mud inclined-plane 902, and described 600 bottom of precipitation chamber is additionally provided with mud discharging mouth 602.
Referring to Fig. 2-Fig. 5, described puddler 704, including body of rod A100, described body of rod A100 are provided with seal groove A101, the first slot rolling A102, inside air channel A103, and described body of rod A100 it is passage A104;
Sealing ring A500 is installed in described seal groove A101;
The first described slot rolling A102 and ball A600 coordinates, and described ball A600 can be rolled in the first slot rolling A102 It is dynamic;
Two envelope gas hood A300 are the substantially symmetrical structure of two structures, and the section which cooperates is exactly one Complete annulus;
Described envelope gas hood A300, including, the gentle cavity shell part A302 of mounting portion A301, described mounting portion A301 is provided with spherical pore A3011, is provided with ball A600 in described spherical pore A3011(Similar to retainer in bearing with The structure of rolling element);
On the outside of described mounting portion A301 with mounting ring A200 on the inside of by threaded engagement assemble;
Air cavity A3021 is provided with the inside of described air cavity housing parts A302;
Air cavity A3021 of one of envelope gas hood A300 is connected with connecting tube A400, described connecting tube 400 for Oxygenerator exports the pipeline communication of oxygen;
Described body of rod A100 is provided with air channel A103 on air cavity A3021 parts.During use, the oxygen of oxygenerator passes through Connecting tube A400 is entered in passage A104 by air channel A103 from air cavity A3021 again into after air cavity A3021, and is passed through Passage A104 carries out aeration into aeration plate.
During use, body of rod A100 is connected with blender output shaft, and blender drives the body of rod to rotate, and seals gas hood A300 and pass through Ball A600 and body of rod A100 is relatively rotated, and this is not driven by body of rod A100 it is ensured that sealing gas hood A300, and can also be with the body of rod Relatively rotate.
Two envelope gas hood A300 after Screw assembly ring A200 screws assembling pass through to compress on the inside of two envelope gas hood A300 Sealing is realized between sealing ring A500 and body of rod A100.
By being mutually adjacent to realization sealing between two envelope gas hood A300;
Further, two described envelope gas hood A300 can be made of one structure and be enclosed within body of rod A100, so can Substantially reduce the demand precision of the manufacturing cost to two envelope gas hood A300.
Further, in order that being more prone to roll between ball A600 and mounting ring A200, can be in mounting ring A200 The second slot rolling A201 is set in inner side and ball A600 contact portions, the second described slot rolling A201 can reduce ball with assembling Contact area on the inside of ring, so as to reduce the frictional force between them.
Preferred embodiment of the present utility model described in detail above.It should be appreciated that the ordinary skill people of this area Member just can make many modifications and variations according to design of the present utility model without the need for creative work.Therefore, all this technology necks In domain, technical staff passes through logical analyses, reasoning or limited reality on the basis of existing technology according to design of the present utility model Available technical scheme is tested, all should be in the protection domain being defined in the patent claims.

Claims (10)

1. a kind of integrated waste-water treater for livestock and poultry breeding industry, including control room, equipment for separating liquid from solid;
The inlet of described equipment for separating liquid from solid, slag-drip opening, liquid outlet are connected with feed tube, scum pipe, drain pipe respectively, institute The drain pipe stated is drained to the waste water after solid-liquid separation in the first anaerobic reaction chamber;It is characterized in that:
Deadening plate is installed in the first described anaerobic reaction chamber, the first anaerobic reaction chamber is divided into two by described deadening plate Front compartment and rear compartment that bottom is connected by convective tank;
Described deadening plate is provided with toward the inclined folding surface in corner inclined-plane in convective tank one end;
The first described anaerobic reaction top of chamber is connected with the second anaerobic reaction top of chamber by connectedness;
The second described anaerobic reaction top of chamber is connected with the 3rd anaerobic reaction top of chamber also by connectedness;
The 3rd described anaerobic reaction top of chamber is connected with the first aerobic reaction top of chamber by connectedness;
The first described aerobic reaction bottom of chamber portion is connected with the second aerobic reaction chamber bottom by connectedness, and described second is aerobic Reaction chamber bottom is connected with the 3rd aerobic reaction bottom of chamber portion by connectedness.
2. a kind of integrated waste-water treater for livestock and poultry breeding industry as claimed in claim 1, is characterized in that:Described Equipment for separating liquid from solid is solid-liquid separating machine.
3. a kind of integrated waste-water treater for livestock and poultry breeding industry as claimed in claim 1, is characterized in that:Described Connectedness is connecting pipe or cell body, opening.
4. a kind of integrated waste-water treater for livestock and poultry breeding industry as claimed in claim 1, is characterized in that:Described First anaerobic reaction chamber, the second anaerobic reaction chamber, the 3rd anaerobic reaction top of chamber are provided with gas skirt.
5. a kind of integrated waste-water treater for livestock and poultry breeding industry as claimed in claim 1, is characterized in that:Described First aerobic reaction top of chamber is provided with blender, during the puddler of described blender stretches into the first aerobic reaction chamber and described Puddler on be fixed with stirring vane and aeration plate;Described aeration plate connects to produce oxygenerator by trachea with oxygenerator Raw oxygen carries out aeration in being introduced into aeration plate.
6. a kind of integrated waste-water treater for livestock and poultry breeding industry as claimed in claim 5, is characterized in that:Described Puddler is hollow state, is supplied for aeration plate in the endoporus of trachea loading puddler.
7. a kind of integrated waste-water treater for livestock and poultry breeding industry as claimed in claim 1, is characterized in that:Described 3rd aerobic reaction top of chamber is connected with precipitation top of chamber by connectedness, and described precipitation top of chamber is provided with discharge outlet, described Discharge outlet connect with drain pipe;Described precipitation bottom of chamber portion be additionally provided with two down relative tilt lead mud inclined-plane, it is described Precipitation bottom of chamber portion is additionally provided with mud discharging mouth.
8. a kind of integrated waste-water treater for livestock and poultry breeding industry as described in claim 1-7 is arbitrary, is characterized in that: Described the first anaerobic reaction chamber, the second anaerobic reaction chamber, the 3rd anaerobic reaction cavity configuration are identical.
9. a kind of integrated waste-water treater for livestock and poultry breeding industry as described in claim 1-7 is arbitrary, is characterized in that: Described the first aerobic reaction chamber, the second aerobic reaction chamber, the 3rd aerobic reaction cavity configuration are identical.
10. a kind of integrated waste-water treater for livestock and poultry breeding industry as claimed in claim 1, is characterized in that:It is described Puddler, including, the body of rod, the described body of rod is provided with seal groove, the first slot rolling, inside air channel, and the described body of rod is Passage;
Sealing ring is installed in described seal groove;The first described slot rolling and ball engagement;
Two envelope gas hoods are the symmetrical structure of two structures, and its section for cooperating is a complete annulus;
Described envelope gas hood, including, the gentle cavity shell part in mounting portion, described mounting portion is provided with spherical pore, described Spherical pore in ball is installed;
On the outside of described mounting portion with mounting ring on the inside of by threaded engagement assemble;
Air cavity is provided with the inside of described air cavity housing parts;
The air cavity of one of envelope gas hood is connected with connecting tube, and described connecting tube is for the pipeline with oxygenerator output oxygen Connection;
The described body of rod is provided with air channel on air cavity part;
Two envelope gas hoods after Screw assembly ring screws assembling pass through to compress between sealing ring and the body of rod on the inside of two envelope gas hoods Realize sealing;
By being mutually adjacent to realization sealing between two envelope gas hoods.
CN201621107226.2U 2016-10-09 2016-10-09 A kind of integrated waste-water treater for livestock and poultry breeding industry Expired - Fee Related CN206069520U (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106946414A (en) * 2017-04-28 2017-07-14 重庆蓬辖生猪养殖有限公司 A kind of Pig farm wastewater treatment system
CN110255726A (en) * 2019-06-28 2019-09-20 盐城恒清河湖整治有限公司 A kind of poultry farms sewage disposal device

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106946414A (en) * 2017-04-28 2017-07-14 重庆蓬辖生猪养殖有限公司 A kind of Pig farm wastewater treatment system
CN110255726A (en) * 2019-06-28 2019-09-20 盐城恒清河湖整治有限公司 A kind of poultry farms sewage disposal device

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