CN209226738U - A kind of high-concentration sewage quick treatment device - Google Patents
A kind of high-concentration sewage quick treatment device Download PDFInfo
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- CN209226738U CN209226738U CN201821885205.2U CN201821885205U CN209226738U CN 209226738 U CN209226738 U CN 209226738U CN 201821885205 U CN201821885205 U CN 201821885205U CN 209226738 U CN209226738 U CN 209226738U
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Abstract
The utility model discloses a kind of high-concentration sewage quick treatment devices.Described device includes the first order purification device, second level purification device and third level purification device set gradually from inside to outside.First order purification device makes most of particle rapid subsidence by cyclonic separation, fine particle without being sufficiently separated revolves reactor by rapids and forms big floc sedimentation, the sedimentation separation again in the purification device of the second level, guarantee effluent quality requirement, the particle obtained by sedimentation is discharged by the bottom of third level purification device, and the clear water obtained by sedimentation is then discharged from the middle and upper part of third level purification device.The utility model ensure that the purification efficiency of high-concentration sewage.In addition, the utility model has, separative efficiency is high, occupied area is few, treating capacity is big, low power consumption and other advantages.
Description
Technical field
The utility model belongs to technical field of sewage more particularly to a kind of high-concentration sewage quick treatment device.
Background technique
High-concentration sewage, complicated component, solid content is high, and particle size distribution is wide, and natural subsidence is difficult.High-concentration sewage
Processing technique is roughly divided into materialization, chemistry and biological three categories, and traditional wastewater processing unit recycles inefficient, land occupation face
Product is big, is unable to meet production requirement.In existing highly concentrated sewage disposal device, coagulating treatment equipment can remove colloidal state
The pollutants such as solid particle, suspended matter and grease, but sludge quantity is big, cost is high；Electrolytic processing apparatus can change
The property and structure of pollutant, makes organic matter degrade, but since power consumption is excessive, at high cost, and this equipment is confined to handle
A small amount of sewage；It is neutralized there is also the excessively high problem of use cost using chemical agent merely and be easy to cause secondary dirt
Dye.
Utility model content
The purpose of this utility model is that a kind of high-concentration sewage quick treatment device is proposed, to guarantee high-concentration sewage
Purification efficiency, while reducing cost.
The utility model to achieve the goals above, adopts the following technical scheme that
A kind of high-concentration sewage quick treatment device, comprising:
First order purification device, second level purification device and the third level purification device set gradually from inside to outside；
First order purification device includes cyclone and Venturi tube；
No.1 feed pipe, No.1 overflow pipe and No.1 underflow opening are equipped on cyclone；No.1 feed pipe, No.1 overflow pipe
Middle and upper part, the top and bottom of cyclone are located at No.1 underflow opening；
One end of Venturi tube is connect with No.1 feed pipe, and the other end is connect with high-concentration sewage feed pipe；
Second level purification device includes second level purification device shell, rapid rotation reactor and several cones with filter hole
Disk；
Wherein, the top of second level purification device shell is in the form of a column, and lower part is tapered；
Cyclone is located at the inside of second level purification device shell；And
The No.1 underflow opening of the cyclone is stretched down to the lower part of second level purification device shell；
No. two feed pipes, No. two overflow pipes and No. two underflow openings are equipped on the purification device shell of the second level；No. two chargings
Pipe, No. two overflow pipes and No. two underflow openings are located at the middle and upper part of second level purification device shell, top and bottom；
Rapids rotation reactor includes three imports and one outlet；Wherein:
No.1 overflow pipe, which is connected up to rapids, revolves one import of reactor, remaining import of rapids rotation reactor is dosing mouth；
The outlet of rapids rotation reactor is connected to downwards No. two feed pipes；
All cone disks are mounted on the outside of cyclone, and each cone disk is arranged successively from top to bottom；
It is equipped at No. two underflow openings for the No.1 blowdown valve to the third level purification device discharge；
Third level purification device includes third level purification device shell；
The top of third level purification device shell is in the form of a column, and lower part is tapered；
Second level purification device shell is located at the inside of third level purification device shell；And the cyclone, described second
Grade purification device shell, the third level purification device shell coaxial line in the vertical direction；
Clear water output and No. three underflow openings are equipped on third level purification device shell；Clear water output and No. three underflow openings point
Not Wei Yu third level purification device shell middle and upper part and bottom；
No. two blowdown valves for outwardly discharge are installed at No. three underflow openings；
No. two overflow pipes are connected to the inside of the third level purification device shell；
It is equipped in the inside middle and upper part of third level purification device shell cricoid for filtering the inclined plate of sedimented particle；
The mounting height of inclined plate is lower than the mounting height of clear water output；
The medial support of inclined plate is on the purification device shell of the second level, and outside-supporting is on third level purification device shell.
Preferably, the cone disk is welded to connect in the outside of cyclone.
Preferably, the mounting height of the clear water output is higher than the height of Venturi tube.
Preferably, the rapid rotation reactor is located at the outer upper side of third level purification device shell；
It is passed through at the top of the third level purification device shell equipped with the confession No.1 overflow pipe and No. two feed pipes
Through-hole.
Preferably, the top of the cyclone is in the form of a column, and lower part is tapered；And upper diameter, the cone disk of the cyclone
Maximum gauge and second level purification device upper part of the housing size have following relationship:
The upper diameter for defining cyclone is D, then:
The maximum gauge for boring disk is 1.5D-2.5D, and the diameter of second level purification device upper part of the housing is 3D-3.5D.
The utility model has the advantages that
The utility model design has the three-level purification device of embedded structure, and first order purification device passes through cyclonic separation
Make most of particle rapid subsidence, the fine particle without being sufficiently separated revolves reactor by rapids and forms big floc sedimentation, in the second level
Sedimentation separation again in purification device guarantees effluent quality requirement, passes through third level purification device by the particle that sedimentation obtains
Bottom discharge, the clear water obtained by sedimentation is then discharged from the middle and upper part of third level purification device.The utility model ensure that
The purification efficiency of high-concentration sewage.In addition, the utility model has, separative efficiency is high, occupied area is few, treating capacity is big, low energy consumption
The advantages that.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model embodiment middle and high concentration sewage quick treatment device；
Fig. 2 is the schematic of fluid flow of the utility model embodiment middle and high concentration sewage quick treatment device；
Fig. 3 is the structural schematic diagram of rapid rotation reactor in the utility model embodiment；
Fig. 4 is the structural schematic diagram (top view) that disk is bored in the utility model embodiment；
Fig. 5 is the structural schematic diagram (cross-sectional view) of the utility model embodiment middle swash plate；
Fig. 6 is the flow diagram of the utility model embodiment middle and high concentration sewage immediate processing method.
Wherein, 1- cyclone, 2- Venturi tube, 3- No.1 feed pipe, 4- No.1 overflow pipe, 5- No.1 underflow opening, 6- high
Concentration sewage feed pipe, the second level 7- purification device shell, 8- rapids rotation reactor, 9- cone disk, No. bis- feed pipes of 10-, 11- bis-
Overflow pipe, No. bis- underflow openings of 12-, 13- No.1 blowdown valve, 14- third level purification device shell, 15- clear water output, 16- tri-
Underflow opening, No. bis- blowdown valves of 17-, 18- inclined plate, 19- filter hole, 20- first class purification contour stealth, 21- first class purification inward eddy,
22- second level eddy flow, 23- second level eddy flow ascending current, the compressional zone 24-, the settling zone 25-, the clear water zone 26-, 27- ascending current.
Specific embodiment
With reference to the accompanying drawing and specific embodiment is described in further detail the utility model:
As shown in connection with fig. 1, a kind of high-concentration sewage quick treatment device, design have the purification dress of multistage embedded structure
It sets, for realizing the purified treatment of high-concentration sewage, for example has three-level in the present embodiment.
First order purification device, second level purification device and third level purification device are set gradually from inside to outside.Using upper
Embedded structure is stated, is conducive to reduce occupied area.Wherein, first order purification device includes cyclone 1 and Venturi tube 2.
Cyclone 1 can use cyclone common in the art, and structure is, for example:
The top of cyclone 1 is in the form of a column, and lower part is tapered.
No.1 feed pipe 3, No.1 overflow pipe 4 and No.1 underflow opening 5 are equipped on cyclone；No.1 feed pipe 3, No.1 are overflow
Flow tube 4 and No.1 underflow opening 5 are located at the middle and upper part of cyclone, top and bottom.
Wherein, No.1 feed pipe 3 is the opening of horizontal direction, and No.1 overflow pipe 4 and No.1 underflow opening 5 are vertical open
Mouthful.
Venturi tube 2 is also arranged horizontally, and connection relationship is as follows:
One end of Venturi tube 2 is connect with No.1 feed pipe 3, and the other end is connect with high-concentration sewage feed pipe 6.
Wherein, high-concentration sewage is delivered to Venturi tube 2 via high-concentration sewage feed pipe 6, and further arrive No.1 into
Expects pipe 3.
High-concentration sewage is diluted by the present embodiment by the Absorb Water effect of Venturi tube 2, makes to enter sewage treatment
The concentration of wastewater of device reaches the optimum range of cyclonic separation, improves separation effect of settling.
Second level purification device includes second level purification device shell 7, rapid rotation reactor 8 and several cone disks 9.
Wherein, the top of second level purification device shell 7 is in the form of a column, and lower part is tapered.
Cyclone 1 is located at the inside of second level purification device shell 7, and No.1 underflow opening 5 is stretched down to the second level and purified
The lower part (stretching to the cone section part of shell 7) of device housing.
10, No. two overflow pipes 11 of No. two feed pipes and No. two underflow openings 12 are equipped on second level purification device shell 7.
Wherein, 10, No. two overflow pipes 11 of No. two feed pipes and No. two underflow openings 12 are located at second level purification device shell
Middle and upper part, the top and bottom of body 7.No. two feed pipes 10 connect and (are explained in detail below) with rapids rotation reactor 8.
No. two overflow pipes 11 and No. two underflow openings 12 are vertical opening.
Rapid rotation reactor 8 in the present embodiment can be using existing pipe-line mixer in the prior art.Its role is to,
Make subparticle quick agglomerate under the action of medicament, to form big floc sedimentation.
It is PAM (flocculant) that medicament in the present embodiment, which is PAC (flocculation aid), medicament 2 for example including medicament 1,.
As shown in figure 3, the structure of rapid rotation reactor 8 for example can be comprising three imports A1, A2, B and one outlet C.
No.1 overflow pipe 4 is connected up to the import B of rapid rotation reactor.
Import A1 and import A2 is dosing mouth, wherein import A1 is for adding medicament 1, i.e. PAC (flocculation aid), import
A2 is for adding medicament 2, i.e. PAM (flocculant).As seen from Figure 3, the dosing mouth 2 in the present embodiment is located at dosing mouth 1
Downstream.Both the above medicament is added simultaneously from import A1 and import A2.
The outlet C of rapids rotation reactor 8 is connected to No. two feed pipes 10.
Cone disk 9 in the present embodiment have it is multiple, structure as shown in figure 4, it is each cone disk 9 surface on be equipped with filtering
Hole 19.All cone disks 9 are mounted on the outside of cyclone, and each cone disk is arranged successively from top to bottom.
By above-mentioned design, so that small floc sedimentation can be detached from rapidly cyclonic action, when small floc sedimentation exists when encountering cone disk 9
It is deposited on cone disk 9 after forming big floc sedimentation to a certain extent, cone 9 resistance of disk can be overcome, slide sedimentation downwards.
Preferably, the outside that disk 9 is installed on cyclone 1 by welding is bored in the present embodiment.
As shown in Figure 1, (i.e. cone 9 sectional dimension of disk gradually expands cone disk 9 from top to bottom for installation downward on cyclone 1
Greatly).
No.1 blowdown valve 13 is installed at No. two underflow openings 12, it, can be with by periodically turning on for the No.1 blowdown valve 13
The precipitating particle (particulate matter) of 7 bottom of second level purification device shell is periodically discharged to third level purification device.
Third level purification device includes third level purification device shell 14.
The top of third level purification device shell 14 is in the form of a column, and lower part is tapered.
Second level purification device shell 7 is located at the inside of third level purification device shell 14；And cyclone 1, the second level are net
Change device housing 7, third level purification device shell 14 coaxial line in the vertical direction.
Clear water output 15 and No. three underflow openings 16 are equipped on third level purification device shell 14.Clear water output 15 and No. three
Underflow opening 16 is located at the middle and upper part and bottom of third level purification device shell 14.
No. two blowdown valves 17 for outwardly discharge are installed at No. three underflow openings 16.
By No. two blowdown valves 17, the particle of deposition can be periodically discharged to the sewage-treatment plant in the present embodiment.
No. two overflow pipes 11 are connected to the inside of third level purification device shell 14.
In addition, being equipped with cricoid inclined plate 18 in the inside middle and upper part of third level purification device shell 14, as shown in Figure 5.
Inclined plate 18 in the present embodiment for example can be using existing inclined plate (plastics material in inclined-plate clarifying basin in the prior art
Matter), for filtering sedimented particle.In addition, the present embodiment middle swash plate 18 also has following connection structure:
The medial support of inclined plate 18 is on second level purification device shell 7, and outside-supporting is in third level purification device shell
On 14.
18 one side of inclined plate functions similarly to the effect of cone disk 9, that is, plays the role of filtering sedimentation, on the other hand, tiltedly
The structure design of plate 18 determines that it can play the supporting role to second level purification device simultaneously.
When inclined plate 18 is installed, mounting height is lower than the mounting height of clear water output 15.
Since Venturi tube 2 needs to suck clear water in the present embodiment, the mounting height needs of clear water output 15 are higher than
The height of Venturi tube 2 just can guarantee the continuous water suction of Venturi tube 2, to guarantee the normal operation of whole device.
Rapids rotation reactor 8 is preferably placed at the outer upper side of third level purification device shell.In third level purification device shell
14 top is equipped with the through-hole (not shown) passed through for No.1 overflow pipe 4 and No. two feed pipes 10.
No.1 overflow pipe 4 and No. two feed pipes 10 are pierced by outward by the through-hole respectively and revolve reactor phase with rapids
Even.
In addition, upper diameter of the present embodiment also to cyclone 1, bores the maximum gauge and second level purification device of disk 9
The relationship of the upper diameter of shell 7 has carried out a series of experiments, and conclusion is as follows:
The upper diameter for defining cyclone is D, then:
The maximum gauge for boring disk is preferably 1.5D-2.5D, and the maximum gauge of preferably cone disk is 2D；And second level purification device shell
The diameter on body top is preferably 3D-3.5D, and the diameter of second stage preferably purification device upper part of the housing is 3.25D.
Wherein, the maximum gauge of cone disk 9 refers to, outer diameter possessed by the maximum cone disk 9 of outer diameter in all cone disks 9.
Certainly, all cone disks 9 in the present embodiment also can have identical outer diameter.
It was proved that then adsorption area is too small, reduces coarse granule when the maximum gauge for boring disk 9 is less than 1.5D
Effect of settling, when bore disk 9 maximum gauge be greater than 2.5D when, then reduce tangential velocity, influence settling efficiency.
Therefore, the range that the maximum gauge of the cone disk in the present embodiment is 1.5D-2.5D.
In addition, reducing purification effect when the diameter of the second level purification device upper part of the housing in the present embodiment is less than 3D
Rate, and be higher than 3.5D when, then coarse granule can be made to run out of from No. two overflow pipes, influence clean-up effect.
Therefore, the diameter of the second level purification device upper part of the housing in the present embodiment is the range of 3D-3.5D.
Certainly, the size of the tilt angle and filter hole 19 of boring disk 9 in the present embodiment also requires, such as bores inclining for disk 9
Rake angle can be 50-65 degree, most preferably 60 degree, and the size of filter hole 19 is advisable in 2-3mm.
By above-mentioned design, so that small floc sedimentation is when encountering cone disk 9, the effect that can be detached from cyclonic action rapidly is more preferable.
As shown in Fig. 2, the substantially treatment process of the present embodiment middle and high concentration sewage quick treatment device are as follows:
The sewage of high concentration squeezes into No.1 feed pipe 3 by high-concentration sewage feed pipe 6 by pump (not shown), in interior external pressure
Under the action of difference, Venturi tube 2 sucks clear water from external clear water zone (i.e. the top clear water zone 26 of third level purification device), by it
It is diluted to sewage of low concentration, reaches the isolated optimum concentration range of cyclone 1.
After sewage tangentially enters cyclone 1 at a high speed, under effect of centrifugal force, the fraction of coarse granule and its carrying
Water enters the bottom of second level purification device shell 7 as 20 rapid subsidence of first class purification contour stealth is from the discharge of No.1 underflow opening 5
It (is accumulated i.e. at No. two underflow openings 12) in portion.Still the sewage containing a small amount of particle follows first class purification inward eddy 21 from No.1 overflow
Pipe 4 is discharged, and revolves reactor 8 into rapids, and inside rapids rotation reactor 8, subparticle quick agglomerate under the action of medicament is formed
Big floc sedimentation.Level-one overflow is further processed after rapids revolves 8 flocculation of reactor into second level purification device.
Since second level purification device size is greater than first order purification device, under the effect of same treatment amount, second
Charging speed of the charging rate of No. two feed pipes 10 of grade purification device much smaller than the No.1 feed pipe 3 of first order purification device
Degree.Under tangential inlet effect, second level eddy flow 22 (micro- eddy flow) is formed inside the purification device of the second level, floc sedimentation can not only be kept
Integrality, and capable of quickly settling downwards, to side wall, and with the coarse granule product mixed-stacking that is discharged from No.1 underflow opening 5, two
Number underflow opening 12 is equipped with No.1 blowdown valve 13, and after bottom section concentration reaches certain value, No.1 blowdown valve 13 opens automatic row
Material.
Due to being equipped with multiple cone disks 9 arranged along the vertical direction in the outside of cyclone 1, so that second level eddy flow ascending current
During 23 overflows, after small floc sedimentation encounters cone disk 9, it can be detached from cyclonic action rapidly, deposited on cone disk 9, when depositing to
After forming big floc sedimentation to a certain degree, big floc sedimentation overcomes the resistance of cone disk 9, and landing is settled down to No. two underflow openings 12.The present embodiment exists
Under the action of boring disk 9, it can guarantee the water quality of high throughput underflow outflow water (being discharged through No. two overflow pipes 11).
No.1 blowdown valve 13 is installed at No. two underflow openings 12, and periodically net to the third level by the No.1 blowdown valve 13
Disguise the bottom discharging set, the further Compression Settlement at No. three underflow openings 16 of third level purification device.
Compressional zone gradually rises in third level purification device, and lower layer compressional zone 24 is gradually formed in third level purification device
(high concentration coarse granule), middle layer settling zone 25 (solution of suspended coarse particles) and upper layer clear water zone 26 are (containing thin few
Grain), the filtering of inclined plate 18 is penetrated progressively through to upper layer clear water zone 26 in transition region ascending current 27, and water quality is reachable after the filtering of inclined plate 18
To index request.Inclined plate 18 is not only similar with cone disk 9 to play the role of filtering sedimentation, while playing branch to second level purification device
Support effect.It is used inside third level purification device in the clear water zone of upper layer for the Absorb Water of Venturi tube 2, and third level purification dress
The middle and upper part set is equipped with clear water output 15, and clear water zone supernatant after precipitation is discharged from clear water output 15, as qualified production
Product.
Quickly locate in addition, the utility model also proposed a kind of high-concentration sewage based on above-mentioned sewage quick treatment device
Reason method.
As shown in Fig. 1,2 and 6, a kind of high-concentration sewage immediate processing method includes the following steps:
S1. high-concentration sewage is transported to cyclone 1, coarse granule by high-concentration sewage feed pipe 6 and Venturi tube 2
It is discharged in second level purification device shell 7 downwards, fine grained is upwardly into rapid rotation reactor 8；
S2. it is revolved to rapids and PAC (flocculation aid) is added at the dosing mouth 1 (import A1) of reactor 8, at dosing mouth 2 (import A2)
It is added PAM (flocculant), generates small floc sedimentation and enter in second level purification device shell 7；
S3. under the action of 7 inward eddy of second level purification device shell and cone disk 9, coarse granule and the sedimentation of small floc sedimentation,
And (bottom) compressional zone of third level purification device shell 14 is discharged to from No.1 blowdown valve 13 or is adsorbed by cone disk 9, clear water
(top) clear water zone of third level purification device shell 14 is then discharged to by No. two overflow pipes 11；
S4. remainder particulate is pressed back into (bottom) compressional zone of third level purification device shell 14 by resistance by inclined plate 18,
Clear water is by inclined plate 18 up to (top) clear water zone of third level purification device shell 14；
S5. clear water zone as purifies the water body finished, flows out from clear water output 15, and precipitating, particle etc. are from No. two blowdown valves
Discharge.
The utility model is high with separative efficiency, treating capacity is big, low power consumption and other advantages, makes a concrete analysis of as follows:
1. separative efficiency is high
In first order purification device and second level purification device, eddy flow centrifugal force can accelerate the sedimentation of wadding body, and cone disk is effective
Increase settling area；In third level purification device, the resistance of inclined plate is more advantageous to sedimentation, and can adsorb wadding body, improves and divides
From efficiency.
2. treating capacity is big
The utility model mainly utilizes eddy flow principle and suction-operated, and first order purification device, second level purification dress
The cycle operation between third level purification device is set, and at No. two underflow openings 12 of second level purification device and third
It is respectively equipped with blowdown valve at No. three underflow openings 16 of grade purification device, the continuous processing to sewage may be implemented.
3. low energy consumption
What first order purification device and second level purification device mainly utilized in the utility model is eddy flow and cone disk absorption
Principle greatly reduce dosing and energy consumption compared to traditional simple agent-feeding treatment method.
Third level purification device does not need additional power source using inclined plate sedimentation, the principle of absorption.
Certainly, the preferred embodiment of only the utility model described above, the utility model is not limited to enumerate above-mentioned
Embodiment, it should be noted that for anyone skilled in the art under the introduction of this specification, that is made is all etc.
With substitution, obvious variant, all fall within the essential scope of this specification, it ought to be by the protection of the utility model.
Claims (6)
1. a kind of high-concentration sewage quick treatment device characterized by comprising
First order purification device, second level purification device and the third level purification device set gradually from inside to outside；
First order purification device includes cyclone and Venturi tube；
No.1 feed pipe, No.1 overflow pipe and No.1 underflow opening are equipped on cyclone；No.1 feed pipe, No.1 overflow pipe and one
Number underflow opening is located at the middle and upper part of cyclone, top and bottom；
One end of Venturi tube is connect with No.1 feed pipe, and the other end is connect with high-concentration sewage feed pipe；
Second level purification device includes second level purification device shell, rapid rotation reactor and several cone disks with filter hole；
Wherein, the top of second level purification device shell is in the form of a column, and lower part is tapered；
Cyclone is located at the inside of second level purification device shell；And
The No.1 underflow opening of the cyclone is stretched down to the lower part of second level purification device shell；
No. two feed pipes, No. two overflow pipes and No. two underflow openings are equipped on the purification device shell of the second level；No. two feed pipes, two
Number overflow pipe and No. two underflow openings are located at the middle and upper part of second level purification device shell, top and bottom；
Rapids rotation reactor includes three imports and one outlet；Wherein:
No.1 overflow pipe is connected up to an import of rapid rotation reactor, remaining import of rapids rotation reactor is dosing mouth；
The outlet of rapids rotation reactor is connected to downwards No. two feed pipes；
All cone disks are mounted on the outside of cyclone, and each cone disk is arranged successively from top to bottom；
It is equipped at No. two underflow openings for the No.1 blowdown valve to the third level purification device discharge；
Third level purification device includes third level purification device shell；
The top of third level purification device shell is in the form of a column, and lower part is tapered；
Second level purification device shell is located at the inside of third level purification device shell；And the cyclone, the second level are net
Change device housing, the third level purification device shell coaxial line in the vertical direction；
Clear water output and No. three underflow openings are equipped on third level purification device shell；Clear water output and No. three underflow openings distinguish position
In the middle and upper part and bottom of third level purification device shell；
No. two blowdown valves for outwardly discharge are installed at No. three underflow openings；
No. two overflow pipes are connected to the inside of the third level purification device shell；
It is equipped in the inside middle and upper part of third level purification device shell cricoid for filtering the inclined plate of sedimented particle；
The mounting height of inclined plate is lower than the mounting height of clear water output；
The medial support of inclined plate is on the purification device shell of the second level, and outside-supporting is on third level purification device shell.
2. high-concentration sewage quick treatment device according to claim 1, which is characterized in that
The cone disk is welded to connect in the outside of cyclone.
3. high-concentration sewage quick treatment device according to claim 1, which is characterized in that
The mounting height of the clear water output is higher than the height of Venturi tube.
4. high-concentration sewage quick treatment device according to claim 1, which is characterized in that
The rapid rotation reactor is located at the outer upper side of third level purification device shell；
The through-hole passed through for the No.1 overflow pipe and No. two feed pipes is equipped at the top of the third level purification device shell.
5. high-concentration sewage quick treatment device according to claim 1, which is characterized in that
The Venturi tube is located at the inside of third level purification device shell and is located at the top of the inclined plate.
6. high-concentration sewage quick treatment device according to claim 1, which is characterized in that
The top of the cyclone is in the form of a column, and lower part is tapered；And the cyclone upper diameter, bore disk maximum gauge with
And the size of second level purification device upper part of the housing has following relationship:
The upper diameter for defining cyclone is D, then:
The maximum gauge for boring disk is 1.5D-2.5D, and the diameter of second level purification device upper part of the housing is 3D-3.5D.
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| CN201821885205.2U CN209226738U (en) | 2018-11-15 | 2018-11-15 | A kind of high-concentration sewage quick treatment device |
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| CN201821885205.2U CN209226738U (en) | 2018-11-15 | 2018-11-15 | A kind of high-concentration sewage quick treatment device |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109354246A (en) * | 2018-11-15 | 2019-02-19 | 山东科技大学 | A kind of high-concentration sewage quick treatment device and its processing method |
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2018
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109354246A (en) * | 2018-11-15 | 2019-02-19 | 山东科技大学 | A kind of high-concentration sewage quick treatment device and its processing method |
| CN109354246B (en) * | 2018-11-15 | 2023-09-26 | 山东科技大学 | High-concentration sewage rapid treatment device and treatment method thereof |
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