CN206014490U - A kind of sewage-treatment plant - Google Patents
A kind of sewage-treatment plant Download PDFInfo
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- CN206014490U CN206014490U CN201620873904.XU CN201620873904U CN206014490U CN 206014490 U CN206014490 U CN 206014490U CN 201620873904 U CN201620873904 U CN 201620873904U CN 206014490 U CN206014490 U CN 206014490U
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- sewage
- sedimentation tank
- treatment plant
- cell body
- basin
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Abstract
This utility model is related to the technical field of sewage treatment equipment of power plant and chemical enterprise, discloses a kind of sewage-treatment plant, including：Cell body, wherein, demarcation strip and deflection plate are provided with compartment from left to right successively in the cell body, so as to the cell body to be separated into coagulating basin, flocculation basin and sedimentation tank successively from left to right, the coagulating basin, the flocculation basin and the sedimentation tank are sequentially communicated, wherein, the demarcation strip and the deflection plate with the cell body in fluid excessively stream direction perpendicular.The sewage-treatment plant can also be recycled and saving water resource with the liquid after processing the efficiency high of sewage, processing.
Description
Technical field
This utility model is related to the technical field of sewage treatment equipment of power plant and chemical enterprise, more particularly to a kind of sewage
Processing meanss.
Background technology
At present, existing steam power plant and chemical enterprise adopt lime coagulation during processing, generally to sewage
Handling process is softened, i.e. by adding Calx and assisted reaction agent into sedimentation tank so that sewage respectively with stone
There is chemical reaction to generate alumen ustum in ash and assisted reaction agent.By continuing to add assisted reaction agent into sedimentation tank, so that
Obtain the assisted reaction agent and continue chemical reaction, the alumen ustum bigger so as to generate quality with the alumen ustum for generating.
However, as existing sewage disposal process is carried out in same sedimentation tank, this will cause generation
Alumen ustum is shorter because of the time contacted with the liquid in sedimentation tank, and the speed for causing alumen ustum to generate is more slow, causes the dirt for processing
Because there is the body refuse not reacted completely in water, so that sewage has that during process treatment effeciency is low.
Utility model content
(1) technical problem to be solved
The purpose of this utility model is to provide a kind of sewage-treatment plant, to solve present in prior art due to sewage
Processing procedure in same sedimentation tank, thus the vitriol that sewage and assisted reaction agent generated after there is chemical reaction can be caused
The time that Hua Yin is contacted with the liquid in sedimentation tank is shorter, causes the sewage in sedimentation tank to fail to react completely, so as to there is dirt
The low problem of the treatment effeciency of water.
(2) technical scheme
In order to solve above-mentioned technical problem, according to the utility model proposes a kind of sewage-treatment plant, including：Cell body,
Wherein, demarcation strip and deflection plate are provided with from left to right successively in compartment in the cell body, so as to by the cell body successively from
Left-to-right is separated into coagulating basin, flocculation basin and sedimentation tank, and the coagulating basin, the flocculation basin and the sedimentation tank connect successively
Logical, wherein, the demarcation strip and the deflection plate with the cell body in fluid excessively stream direction perpendicular.
Wherein, the upper port in the cell body is provided with support beam.
Wherein, in the support beam and the region of the corresponding coagulating basin is provided with the first agitator, first stirring
Device is included the first motor being arranged in the support beam and is connected and energy with the outfan of first motor
Towards the first puddler that the inside of the coagulating basin extends, and it is arranged on the elongated end of first puddler and first stirs
Mix piece.
Wherein, the sewage-treatment plant also includes guide shell, the bottom of the first end of the guide shell and the coagulating basin
Wall is connected, and the second end of the guide shell passes through the diapire of the flocculation basin and can extend into the inside of the flocculation basin.
Wherein, in the support beam and the region of the corresponding flocculation basin is provided with the second agitator, second stirring
Device is included the second motor being arranged in the support beam and is connected and energy with the outfan of second motor
Towards the second puddler that the inside of the flocculation basin extends, and it is arranged on the elongated end of second puddler and second stirs
Mix piece.
Wherein, the second end of the guide shell is oppositely arranged and is spaced apart in the vertical with second stirring sheet.
Wherein, accommodating chamber is configured with the diapire of the sedimentation tank.
Wherein, being provided with the sedimentation tank can be by the precipitate scraping delivery in the sedimentation tank to the receiving intracavity
Mud scraper.
Wherein, the mud scraper includes the 3rd driving electricity in the region of the corresponding described sedimentation tank for being arranged on the support beam
Machine and the rotary shaft for being connected with the outfan of the 3rd motor and extending towards the inside of the sedimentation tank, and
It is arranged on the cleaning shoe of the end of the diapire of the direction sedimentation tank of the rotary shaft.
Wherein, the outer surface of the cleaning shoe is matched with the lubrication groove profile surface of the sedimentation tank.
Wherein, water leg is provided with the sedimentation tank, the upper port of the upper port of the water leg and the sedimentation tank
Flush, on the side wall of the water leg, multiple pod apertures are provided with compartment.
(3) beneficial effect
The sewage-treatment plant that this utility model is provided, compared with prior art, has the advantage that：
The sewage-treatment plant by being provided with demarcation strip and deflection plate in cell body from left to right successively in compartment, so as to
Cell body is separated into coagulating basin, flocculation basin and sedimentation tank successively from left to right.Wherein, the coagulating basin, flocculation basin and precipitation
Pond is sequentially communicated.So, as cell body to be configured to multiple cell body of relatively independent formula, so as to pass through successively into each cell body
Corresponding reactant is added, so that the reactant is fully contacted with the sewage in corresponding cell body and aggregation occurs with life
Into floccule, so just can enable the impurity in sewage that aggregation thoroughly occurs, so, just greatly increase dirt
The treatment effeciency of water, to obtain the water of satisfactory reusable edible.
Additionally, by arranging the first agitator in coagulating basin such that it is able to accelerate the sewage and flocculant in coagulating basin
Reaction, and cause reaction more thoroughly, the second agitator be set in flocculation basin such that it is able to accelerate the first floccule and
The reaction of flocculation aid, and cause reaction thoroughly.So, the setting of first agitator and the second agitator, greatly increases
The treatment effeciency of sewage.
In addition, by setting up mud scraper in sedimentation tank such that it is able to improve the treatment effeciency of precipitate, save artificial
Process the time of precipitate, improve work efficiency.
Description of the drawings
Fig. 1 is the overall structure diagram of the sewage-treatment plant of embodiment of the present utility model.
In figure, 100：Sewage-treatment plant；1：Cell body；11：Coagulating basin；12：Flocculation basin；13：Sedimentation tank；121：Flocculation basin
Diapire；131：Lubrication groove profile surface；132：The upper port of sedimentation tank；133：The diapire of sedimentation tank；134：Accommodating chamber；2：Demarcation strip；
3：Deflection plate；4：Support beam；5：First agitator；51：First motor；52：First puddler；53：First stirring sheet；6：
Guide shell；61：The first end of guide shell；62：Second end of guide shell；7：Second agitator；71：Second motor；72：The
Two puddlers；73：Second stirring sheet；8：Mud scraper；81：3rd motor；82：Rotary shaft；83：Cleaning shoe；831：Scrape mud
The outer surface of plate；9：Water leg；91：The upper port of water leg；92：The side wall of water leg；921：Pod apertures；10：Kinetic pump；
101：Pipeline.
Specific embodiment
With reference to the accompanying drawings and examples, specific embodiment of the present utility model is described in further detail.Below
Example is used for this utility model to be described, but is not limited to scope of the present utility model.
As shown in figure 1, Fig. 1 show schematically show the sewage-treatment plant 100 includes cell body 1, demarcation strip 2, deflection plate
3rd, coagulating basin 11, flocculation basin 12 and sedimentation tank 13.
Cell body 1 is configured to the internal square or rectangular configuration with cavity, and the setting of the cell body 1 is mainly used in accommodating liquid
Body.Easy to understand, the liquid is defined as the sewage with impurity through power plant or chemical plant emission out.
The profile of demarcation strip 2 is generally rectangular shaped or square, it is readily appreciated that, the outer surface of the demarcation strip 2 is interior with cell body 1
Contoured surface matches, thus, the concrete shape of the demarcation strip 2 can be determined by the lubrication groove profile surface of cell body 1.
The profile of deflection plate 3 is substantially square or rectangle, and its outer surface is matched with the lubrication groove profile surface of cell body 1.However,
Upper surface of the upper surface of the deflection plate 3 less than cell body 1.So, when the liquid level residing for the liquid in flocculation basin 12 is higher than baffling
During the upper surface of plate 3, then the liquid being located in flocculation basin 12 can be crossed the deflection plate 3 and enter in sedimentation tank 13.So,
Flocculation basin 12 and sedimentation tank 13 are separated, the liquid in flocculation basin 12 by the setting of the deflection plate 3 to a certain extent
After residing liquid level is higher than the upper surface of deflection plate 3, just can cross the deflection plate 3 and enter in sedimentation tank 13, it is achieved thereby that
Flocculation basin 12 is connected with sedimentation tank 13.
By being provided with demarcation strip 2 and deflection plate 3 from left to right successively in compartment in cell body 1, so as to by cell body 1 successively
Coagulating basin 11, flocculation basin 12 and sedimentation tank 13 are separated into from left to right.Wherein, the coagulating basin 11, flocculation basin 12 and precipitation
Pond 13 is sequentially communicated.So, as cell body 1 to be configured to multiple cell body of relatively independent formula, so as to pass through successively to each pond
Corresponding reactant is added in vivo, so that the reactant is fully contacted and aggregation occurs with the sewage in corresponding cell body
To generate floccule, so just can enable the impurity in sewage that aggregation thoroughly occurs, so as to greatly increase
The treatment effeciency of sewage, to obtain the water of satisfactory reusable edible.Further, due to through the sewage-treatment plant
100 pairs of sewage can also be recycled again with the liquid of the clarification for obtaining after processing, thus, it is saved greatly and uses water
Amount, the waste for avoiding water resource.
Demarcation strip 2 and deflection plate 3 with cell body 1 in fluid excessively stream direction perpendicular.That is, 2 He of demarcation strip
Deflection plate 3 is perpendicular with the front-rear side walls of cell body 1 such that it is able to by cell body 1 be separated into above-mentioned coagulating basin 11, flocculation basin 12 with
And sedimentation tank 13.
As shown in figure 1, Fig. 1 also schematically shows the upper port in the cell body 1 is provided with support beam 4.Specifically, this
Support beam 4 can directly be overlapped on the left and right two ends of the upper port of cell body 1, so, just achieve the fixed installation of the support beam 4.
Easy to understand, the support beam 4 primarily serves the effect of support, thus, the support beam 4 should have certain structure
Intensity, thus, the support beam 4 should be fabricated by by the material with certain structural strength.For example, the support beam 4 can be by closing
Golden steel matter is fabricated by.
In one embodiment, Fig. 1 is also schematically shows in the support beam 4 and the region of corresponding coagulating basin 11 sets
There is the first agitator 5.Wherein, the setting of first agitator 5, primarily serves the effect of stirring.
First agitator 5 include the first motor 51 being arranged in support beam 4 and with first motor 51
Outfan the first puddler 52 for being connected and can extending towards the inside of coagulating basin 11, and be arranged on first puddler
First stirring sheet 53 of 52 elongated end.Specifically, by starting the first motor 51, in the band of first motor 51
Under dynamic, the rotation that promotes the first puddler 52 to synchronize, so as to pass through the rotation of first puddler 52, drives first to stir
The rotation of piece 53.So, by the rotation of first stirring sheet 53 so that the sewage in coagulating basin 11 be added into
Flocculant be fully contacted the generation for there is aggregation, further accelerating the first floccule as described below.By
This is visible, the setting of first agitator 5, can accelerate the contact of flocculant and the sewage in coagulating basin 11, so that should
There is aggregation with sewage in flocculant, to generate the first floccule.
In one embodiment, first stirring sheet 53 can be multiple, and each first stirring sheet 53 is along the first puddler
The circumference of 52 elongated end is distributed in equidistant formula.Wherein, the solderable elongated end in the first puddler 52 of each first stirring sheet 53
On.
In one embodiment, Fig. 1 also schematically shows the sewage-treatment plant 100 also includes guide shell 6, and this is led
The first end 61 of flow cartridge 6 is connected with the diapire 111 of coagulating basin 11, and the second end of the guide shell 6 passes through the diapire of flocculation basin 12
121 and the inside of flocculation basin 12 can be extend into.Specifically, the guide shell 6 is configured to the larger tubular structure in aperture, and which acts primarily as
To the effect of the flow direction of guiding fluid, i.e. can be by the liquid in coagulating basin 11 in the presence of kinetic pump 10 as described below
It is transported in flocculation basin 12.
In addition, being higher by the diapire 121 of flocculation basin 12 and extending into flocculation basin 12 by causing the second end 62 of guide shell 6
Inside, so, just can be effectively prevented the sewage containing the first floccule entered in flocculation basin 12 from coagulating basin 11 straight
Connect and cross deflection plate 3 and be flowed in sedimentation tank 13, further, it is to avoid the sewage containing the first floccule is another because not carrying out
Secondary aggregation and enter directly in sedimentation tank 13, cause impurity in sewage to be caused miscellaneous due to fully reacting
There is the halfway of process in matter.
As shown in figure 1, Fig. 1 also schematically shows in the support beam 4 and the region of corresponding flocculation basin 12 is provided with the
Two agitators 7.As second agitator 7 plays a part of to play a part of with above-mentioned first agitator 5 identical, it is to save a piece
For the sake of width, it is not detailed herein.
Second agitator 7 include the second motor 71 being arranged in support beam 4 and with second motor 71
Outfan the second puddler 72 for being connected and can extending towards the inside of flocculation basin 12, and be arranged on the second puddler 72
Elongated end the second stirring sheet 73.Specifically, by starting the second motor 71, in the drive of second motor 71
Under, the rotation that promotes the second puddler 72 to synchronize, so as to pass through the rotation of second puddler 72, drives the second stirring sheet
73 rotation.So, by the rotation of second stirring sheet 73 so that in flocculation basin 12 containing the first floccule
Sewage be fully contacted with the flocculation aid being added into there is aggregation, further, accelerate as described below second
The generation of floccule.As can be seen here, the setting of second agitator 7, can accelerate sewage in flocculation aid and flocculation basin 12
Contact, so that there is aggregation with the sewage containing the first floccule in the flocculation aid, to generate the second floccule.
As shown in figure 1, in one embodiment, Fig. 1 also schematically shows the second end 62 and second of the guide shell 6
Stirring sheet 72 is oppositely arranged in the vertical and is spaced apart.So, in the presence of kinetic pump 10 as described below, will be contained
The sewage of one floccule is pumped into after flocculation basin 12 from coagulating basin 11, and the sewage containing the first floccule can be caused directly just right
Second stirring sheet 73, can be occurred sufficiently instead with the flocculation aid being added into the sewage containing the first floccule so as to convenient
Should, bigger so as to generate quality the second floccule.
In addition, by causing the second end 62 of guide shell 6 with the 72 longitudinally opposed setting of the second stirring sheet and being spaced apart.This
Sample, is also avoided that the drawbacks of the second stirring sheet 72 moves interference with the second end 62 of guide shell 6 during work.
Fig. 1 also schematically shows and be configured with accommodating chamber 134 on the diapire 133 of sedimentation tank 13.Specifically, the receiving
Chamber 134 may be provided at the center of the diapire 133 of sedimentation tank 13.So, convenient through the heavy of 8 scraping delivery of mud scraper as described below
Starch as often as possible can be transported in accommodating chamber 134.Wherein, the activated sludge for entering in accommodating chamber 134 will be back to wadding
In solidifying pond 12, remaining sludge then forms mud cake after the processed of pressure filter (not shown), and the mud cake will be by
The place that specifies is transported to, the liquid of abjection can be recycled.
As shown in figure 1, Fig. 1 also schematically shows, be provided with the sedimentation tank 13 can be by the precipitation in sedimentation tank 13
Mud scraper 8 of the thing scraping delivery in accommodating chamber 134.The setting of the mud scraper 8, can in large quantity by the precipitate in sedimentation tank 13
Scraping delivery so as to improve the treatment effeciency of precipitate, saves the time of artificial scraping delivery precipitate in accommodating chamber 134.
In another embodiment, the mud scraper 8 includes the 3rd of the region of the corresponding sedimentation tank 13 for being arranged on support beam 4
Motor 81, and the rotation for being connected with the outfan of the 3rd motor 81 and extending towards the inside of sedimentation tank 13
Axle 82, and it is arranged on the cleaning shoe 83 of the end of the diapire 133 towards sedimentation tank 13 of the rotary shaft 82.Specifically, this
Three motors 81 can be directly placed in support beam 4, under the drive of the 3rd motor 81, can promote rotary shaft 82 with
The rotation that motor 81 is synchronized, so as to drive cleaning shoe 83 to be circumferentially rotated around rotary shaft 82, in cleaning shoe 83
During being circumferentially rotated, just can be right so as to realize by the precipitate scraping delivery of the bottom of sedimentation tank 13 in accommodating chamber 134
The reprocessing of precipitate.
In a specific embodiment, the profile of cleaning shoe 83 is similar to as square or rectangle, however, scraping mud to reduce
The cleaning shoe 83 can be configured to fence type structure by resistance of the plate 83 during rotation.
As shown in figure 1, Fig. 1 also schematically shows the outer surface 831 of the cleaning shoe 83 and the lubrication groove of sedimentation tank 13
Profile surface 131 matches.In this manner it is ensured that cleaning shoe 83 is during being rotated with rotary shaft 82 so that cleaning shoe 83
The rotation that can be well in sedimentation tank 13, it is to avoid move the phenomenon of interference.
As shown in figure 1, Fig. 1 also schematically shows is provided with water leg 9 in the sedimentation tank 13, the water leg 9 upper
Port 91 is flushed with the upper port 132 of sedimentation tank 13.So, the installation and dismounting of the water leg 9 are facilitated, meanwhile, also strengthen
The structural strength of the upper port 91 of water leg 9, extends service life.
Multiple pod apertures 921 are provided with compartment on the side wall 92 of the water leg 9.So, in the effect of kinetic pump 10
Under, after the sewage containing the second floccule in flocculation basin 12 is pumped in sedimentation tank 13, after static a period of time, in gravity
In the presence of, precipitate can be located at the bottom of sedimentation tank 13, and clear liquid is located at the upper strata of sedimentation tank 13.Due in the water leg 9
Multiple pod apertures 921 are configured with side wall 92, thus, the stillness of night, in the presence of kinetic pump 10, just can be entered through the pod apertures 921
Dao water leg 9 in, so as to realize the collection to the stillness of night.
In one embodiment, above-mentioned flocculant is iron sulfate, and above-mentioned flocculation aid is polyacrylamide.
In sum, the sewage-treatment plant 100 is by being provided with demarcation strip in compartment successively from left to right in cell body 1
2 and deflection plate 3, so as to cell body 1 to be separated into coagulating basin 11, flocculation basin 12 and sedimentation tank 13 successively from left to right.Wherein, should
Coagulating basin 11, flocculation basin 12 and sedimentation tank 13 are sequentially communicated.So, as cell body 1 is configured to the multiple of relatively independent formula
Cell body, so as to pass through to add corresponding reactant into each cell body successively so that the reactant with corresponding cell body
Sewage is fully contacted and aggregation occurs to generate floccule, and the impurity in sewage so just can be enabled thoroughly to occur
Aggregation, so as to greatly increase the treatment effeciency of sewage, to obtain the water of satisfactory reusable edible.
Additionally, passing through to arrange the first agitator 5 in coagulating basin 11 such that it is able to accelerate the sewage and wadding in coagulating basin 11
The reaction of solidifying agent, and cause reaction more thorough.Second agitator 7 is set in flocculation basin 12 such that it is able to accelerate first
Floccule and the reaction of flocculation aid, and cause reaction thoroughly.So, the setting of first agitator 5 and the second agitator 7, greatly
The earth improves the treatment effeciency of sewage.
In addition, passing through to set up mud scraper 8 in sedimentation tank 13 such that it is able to improve the treatment effeciency of precipitate, save
The time of artificial treatment precipitate, improve work efficiency.
Above-mentioned sewage-treatment plant 100 also includes kinetic pump 10, and the kinetic pump 10 is connected with coagulating basin 11 by pipeline 101
Logical.
Embodiment 1：The specific work process of the sewage-treatment plant 100 is, first, by throwing in wadding into coagulating basin 11
Solidifying agent is so that flocculant is contacted with the liquid in coagulating basin 11.Specifically, by into coagulating basin 11 throw in flocculant with
So that flocculant is contacted with the impurity in the sewage in coagulating basin 11.
Secondly, by starting the first agitator 5 so that the liquid in flocculant and coagulating basin 11 occur aggregation from
And generate the first floccule.Specifically, by starting the first motor 51, turn so as to drive the first puddler 52 to synchronize
Dynamic, further, promote the first stirring sheet 53 to be circumferentially rotated, so as to play a part of to stir flocculant and sewage, to add
Fast flocculant occurs fully to react with the impurity in sewage, so as to generate the first floccule.
Secondly, by kinetic pump 10 by the liquid pumping containing the first floccule in flocculation basin 12.
Secondly, by throwing in flocculation aid into flocculation basin 12 so that flocculation aid is contacted with the first floccule.
Secondly, by starting the second agitator 7 so that flocculation aid and the first floccule generation agglutination are so as to generating
Second floccule.That is, by starting the second motor 71, so as to drive the second puddler 72 to be circumferentially rotated, further
Ground, promotes the second stirring sheet 73 to be circumferentially rotated, so as to play a part of to stir flocculation aid and the second floccule, to accelerate to help
There is aggregation with the second floccule in solidifying agent, so as to generate the second floccule.
Then, the liquid pumping containing the second floccule is interior to be precipitated to sedimentation tank 13 by kinetic pump 10, from
And the bottom in sedimentation tank 13 forms precipitate, clear liquid is formed on the upper strata of sedimentation tank 13.Specifically, when containing the second floccule
Liquid enter into sedimentation tank 13 under the pumping of kinetic pump 10 after, static through after a while, under gravity,
Two floccules can be deposited in the bottom of sedimentation tank 13, and the stillness of night is formed in the upper strata of sedimentation tank 13.
Finally, by start mud scraper 8 with by precipitate scraping delivery in accommodating chamber 134, by kinetic pump 10 by stillness of night pump
It is sent in water leg 9.So, the separation of precipitate and the stillness of night in just achieving to sewage, the precipitate that isolates is through overvoltage
Mud cake is formed after the processed of filter, the mud cake is transported to by appointed place by Transporting equipment, the stillness of night that isolates can quilt
Recycle, so as to be saved greatly water resource, save Financial cost.
In one embodiment, quality of the quality of second floccule more than the first floccule.It follows that by inciting somebody to action
There is aggregation to generate the first floccule with flocculant in the sewage in coagulating basin 11, then will in the presence of kinetic pump 10
Liquid containing the first floccule is transported in flocculation basin 12, by throwing in flocculation aid into flocculation basin 12, so as to further
So that there is aggregation the second floccule bigger to generate quality with flocculation aid in the first floccule.As can be seen here, by making
The impurity obtained in sewage experiences aggregations different twice, so that sewage is thoroughly purified, greatly increases dirt
The treatment effeciency of water.
In one embodiment, first floccule and the second floccule can be alumen ustum.
Preferred embodiment of the present utility model is the foregoing is only, not in order to limit this utility model, all at this
Within the spirit and principle of utility model, any modification, equivalent substitution and improvements that is made etc. should be included in this utility model
Protection domain within.
Claims (11)
1. a kind of sewage-treatment plant, it is characterised in that include：
Cell body, wherein, is provided with demarcation strip and deflection plate in the cell body from left to right successively in compartment, so as to by the pond
Body is separated into coagulating basin, flocculation basin and sedimentation tank, the coagulating basin, the flocculation basin and the sedimentation tank successively from left to right
Be sequentially communicated, wherein, the demarcation strip and the deflection plate with the cell body in fluid excessively stream direction perpendicular.
2. sewage-treatment plant according to claim 1, it is characterised in that be provided with support in the upper port of the cell body
Beam.
3. sewage-treatment plant according to claim 2, it is characterised in that in the support beam and the corresponding cohesion
The region in pond is provided with the first agitator, first agitator include the first motor being arranged in the support beam and with
The first puddler that the outfan of first motor is connected and can extend towards the inside of the coagulating basin, Yi Jishe
Put the first stirring sheet of the elongated end in first puddler.
4. sewage-treatment plant according to claim 2, it is characterised in that the sewage-treatment plant also includes water conservancy diversion
Cylinder, the first end of the guide shell are connected with the diapire of the coagulating basin, and the second end of the guide shell passes through the flocculation
The diapire in pond simultaneously can extend into the inside of the flocculation basin.
5. sewage-treatment plant according to claim 4, it is characterised in that in the support beam and the corresponding flocculation
The region in pond is provided with the second agitator, second agitator include the second motor being arranged in the support beam and with
The second puddler that the outfan of second motor is connected and can extend towards the inside of the flocculation basin, Yi Jishe
Put the second stirring sheet of the elongated end in second puddler.
6. sewage-treatment plant according to claim 5, it is characterised in that the second end of the guide shell and described second
Stirring sheet is oppositely arranged in the vertical and is spaced apart.
7. sewage-treatment plant according to claim 2, it is characterised in that be configured with appearance on the diapire of the sedimentation tank
Receive chamber.
8. sewage-treatment plant according to claim 7, it is characterised in that being provided with the sedimentation tank can will be described
Precipitate scraping delivery in sedimentation tank is to the mud scraper for accommodating intracavity.
9. sewage-treatment plant according to claim 8, it is characterised in that the mud scraper includes being arranged on the support
3rd motor in the region of the corresponding described sedimentation tank of beam and it is connected and energy with the outfan of the 3rd motor
Towards the rotary shaft that the inside of the sedimentation tank extends, and be arranged on the diapire of the direction sedimentation tank of the rotary shaft
The cleaning shoe of end.
10. sewage-treatment plant according to claim 9, it is characterised in that the outer surface of the cleaning shoe with described
The lubrication groove profile surface of sedimentation tank matches.
11. sewage-treatment plants according to claim 1, it is characterised in that be provided with water leg in the sedimentation tank, institute
The upper port and the upper port of the sedimentation tank for stating water leg flushes, and is provided with compartment many on the side wall of the water leg
Individual pod apertures.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620873904.XU CN206014490U (en) | 2016-08-12 | 2016-08-12 | A kind of sewage-treatment plant |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620873904.XU CN206014490U (en) | 2016-08-12 | 2016-08-12 | A kind of sewage-treatment plant |
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| Publication Number | Publication Date |
|---|---|
| CN206014490U true CN206014490U (en) | 2017-03-15 |
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ID=58248062
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620873904.XU Active CN206014490U (en) | 2016-08-12 | 2016-08-12 | A kind of sewage-treatment plant |
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| Country | Link |
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| CN (1) | CN206014490U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106145447A (en) * | 2016-08-12 | 2016-11-23 | 内蒙古君正氯碱化工技术研究院 | A kind of sewage-treatment plant and the method processing sewage thereof |
-
2016
- 2016-08-12 CN CN201620873904.XU patent/CN206014490U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106145447A (en) * | 2016-08-12 | 2016-11-23 | 内蒙古君正氯碱化工技术研究院 | A kind of sewage-treatment plant and the method processing sewage thereof |
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