CN110217914A - Sewage purifier - Google Patents
Sewage purifier Download PDFInfo
- Publication number
- CN110217914A CN110217914A CN201910589290.0A CN201910589290A CN110217914A CN 110217914 A CN110217914 A CN 110217914A CN 201910589290 A CN201910589290 A CN 201910589290A CN 110217914 A CN110217914 A CN 110217914A
- Authority
- CN
- China
- Prior art keywords
- room
- water
- clarifying chamber
- sewage purifier
- sewage
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 239000010865 sewage Substances 0.000 title claims abstract description 103
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 262
- 230000001376 precipitating effect Effects 0.000 claims abstract description 81
- 239000013049 sediment Substances 0.000 claims abstract description 66
- 238000012384 transportation and delivery Methods 0.000 claims description 32
- 238000005189 flocculation Methods 0.000 claims description 24
- 230000016615 flocculation Effects 0.000 claims description 24
- 238000005352 clarification Methods 0.000 claims description 23
- 239000007788 liquid Substances 0.000 claims description 18
- 230000001965 increasing effect Effects 0.000 claims description 14
- 230000003028 elevating effect Effects 0.000 claims description 9
- 230000007246 mechanism Effects 0.000 claims description 9
- 239000012530 fluid Substances 0.000 claims description 7
- 210000000867 larynx Anatomy 0.000 claims description 3
- 208000034423 Delivery Diseases 0.000 claims 1
- 238000004140 cleaning Methods 0.000 claims 1
- 239000002245 particle Substances 0.000 abstract description 82
- 239000007787 solid Substances 0.000 abstract description 81
- 230000000694 effects Effects 0.000 abstract description 16
- 238000010586 diagram Methods 0.000 description 12
- 238000000034 method Methods 0.000 description 11
- 238000004062 sedimentation Methods 0.000 description 11
- 230000009471 action Effects 0.000 description 9
- 238000000926 separation method Methods 0.000 description 9
- 230000005484 gravity Effects 0.000 description 8
- 230000008569 process Effects 0.000 description 7
- 239000008187 granular material Substances 0.000 description 6
- 239000010802 sludge Substances 0.000 description 6
- 238000010992 reflux Methods 0.000 description 5
- 230000008859 change Effects 0.000 description 4
- 238000001816 cooling Methods 0.000 description 4
- 239000012535 impurity Substances 0.000 description 4
- 239000003818 cinder Substances 0.000 description 3
- 238000009749 continuous casting Methods 0.000 description 3
- 238000009826 distribution Methods 0.000 description 3
- 238000011010 flushing procedure Methods 0.000 description 3
- 238000005098 hot rolling Methods 0.000 description 3
- 239000007921 spray Substances 0.000 description 3
- 238000005507 spraying Methods 0.000 description 3
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 230000003311 flocculating effect Effects 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 244000144985 peep Species 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 238000005086 pumping Methods 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 238000000338 in vitro Methods 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 229910052761 rare earth metal Inorganic materials 0.000 description 1
- 150000002910 rare earth metals Chemical class 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000004088 simulation Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/38—Treatment of water, waste water, or sewage by centrifugal separation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F2001/007—Processes including a sedimentation step
Abstract
The present invention provides a kind of sewage purifiers, comprising: cyclone sediment room, Hydraulic Circulation clarifying chamber, concentrating and precipitating room and the tube settling room being sequentially communicated；Cyclone sediment room is set to the lower section of Hydraulic Circulation clarifying chamber；Concentrating and precipitating room and tube settling room surround Hydraulic Circulation clarifying chamber, also, tube settling room is set to the top of concentrating and precipitating room.Through the invention, the poor technical problem of the effect of the turbid circulating water processing equipment removal solid particle polluter in the presence of the prior art is alleviated.
Description
Technical field
The present invention relates to technical field of sewage more particularly to a kind of sewage purifiers.
Background technique
In the steel industry, the turbid circulating water system of traditional continuous casting and hot rolling line, generallys use following process flow,
Flushing cinder sewage from production line enters primary sedimentation basin or Whirlwind tank by gravity stream, is discharged through level-one booster station, send to change
Dirt separator or rare-earth magnetic disc or secondary sedimentation tank are learned, is discharged again through two-stage pressurizing pumping plant, through filter or is fed directly to cooling tower
Cooling, then through three times' lifting pumping plant, give to continuous casting or hot rolling line, to clean product surface or product cooling, generation
Flushing cinder sewage constantly so recycles.The flushing cinder sewage constantly so recycled is also known as turbid circulating water.In cyclic process, in turbid circulating water
Solid particle polluter be removed so that be back to the turbid circulating water of continuous casting or hot rolling line water quality keep stablize.
Generally using sewage purification process such as coagulation, precipitating and clarifications, to remove the solid particle polluter in turbid circulating water.But
It is the turbid circulating water processing equipment in the prior art technical problem poor in the presence of the effect of removal solid particle polluter.
Summary of the invention
The object of the present invention is to provide a kind of sewage purifiers, to alleviate the turbid circulating water processing in the presence of the prior art
The poor technical problem of the effect of equipment removal solid particle polluter.
Following technical proposal can be used to realize in above-mentioned purpose of the invention:
The present invention provides a kind of sewage purifier, comprising: the cyclone sediment room that is sequentially communicated, Hydraulic Circulation clarifying chamber,
Concentrating and precipitating room and tube settling room；Cyclone sediment room is set to the lower section of Hydraulic Circulation clarifying chamber；Concentrating and precipitating room and inclined tube are heavy
Shallow lake room surrounds Hydraulic Circulation clarifying chamber, also, tube settling room is set to the top of concentrating and precipitating room.
In a preferred embodiment, the bottom wall of Hydraulic Circulation clarifying chamber is equipped with clarification chamber inlet, Hydraulic Circulation clarifying chamber
Side wall equipped with clarifying chamber export；The annulus of extension and upper and lower opening along the vertical direction is equipped in Hydraulic Circulation clarifying chamber,
Backflow gap, and the opening of the lower end of annulus are equipped between the lower end of annulus and the bottom wall of Hydraulic Circulation clarifying chamber
Direction and covering clarification chamber inlet.
In a preferred embodiment, clarifying chamber outlet is set to the bottom of the side wall of Hydraulic Circulation clarifying chamber.
In a preferred embodiment, the internal diameter of the opening of the lower end of annulus gradually increases along direction from the top down
Greatly.
In a preferred embodiment, the upper end of annulus is connected with expansion pipe, expands the internal diameter of pipe along from bottom to top
Direction be gradually increased.
In a preferred embodiment, the upper end for expanding pipe is connected with guide shell, and the internal diameter of guide shell is from upper end to lower end
It is consistent.
In a preferred embodiment, comprising: the lower end of water sprayer trunnion, water sprayer trunnion is connected to clarification chamber inlet,
Upper end is equipped with opening upward, and annulus surrounds the upper end of water sprayer trunnion, and the fluid into clarification chamber inlet can pass through
Water sprayer trunnion flows upwardly into annulus, also, reflux is equipped between the inner wall of annulus and the outer wall of water sprayer trunnion
Channel.
In a preferred embodiment, including being set to water sprayer trunnion and clarifying the water sprayer nozzle between chamber inlet, water
The lower end of injector nozzles is connected to clarification chamber inlet, and the lower end of water sprayer trunnion is connected to the upper end of water sprayer nozzle, water sprayer
The internal diameter of nozzle is gradually reduced from lower end to upper end.
In a preferred embodiment, sewage purifier provided by the invention includes moving down on annulus for driving
Dynamic annulus elevating mechanism.
In a preferred embodiment, annulus elevating mechanism includes shaft, the gear for being installed on shaft and is installed on
The annulus and rack gear being arranged along the vertical direction, wheel and rack are meshed.
In a preferred embodiment, comprising: be set to Hydraulic Circulation and clarify indoor annular deflector, annular deflector
Outer profile be connected to the inner wall of Hydraulic Circulation clarifying chamber；Clarifying chamber outlet is set to annular deflector and Hydraulic Circulation clarifying chamber
Between bottom wall.
In a preferred embodiment, annular deflector is tilted down from outer profile to Internal periphery.
In a preferred embodiment, the bottom wall of Hydraulic Circulation clarifying chamber includes bottom wall rake, bottom wall rake it is outer
Profile is connect with the side wall of Hydraulic Circulation clarifying chamber, the central axis of the Internal periphery of bottom wall rake close to Hydraulic Circulation clarifying chamber
Line；Bottom wall rake is tilted down from outer profile to Internal periphery.
In a preferred embodiment, the angle that the angle and bottom wall rake that annular deflector tilts down tilt down
It is equal.
In a preferred embodiment, clarifying chamber outlet includes multiple water delivery through-holes, and the both ends of each water delivery through-hole are distinguished
It is connected to Hydraulic Circulation clarifying chamber and concentrating and precipitating room.
In a preferred embodiment, the axis of each water delivery through-hole deviates in the same direction in Hydraulic Circulation clarifying chamber
Mandrel line.
In a preferred embodiment, the axis of each water delivery through-hole tilts down.
In a preferred embodiment, comprising: multiple water-supply-pipes for being connected to water delivery through-hole, water-supply-pipe is to concentrating and precipitating room
Interior extension.
In a preferred embodiment, the side wall of Hydraulic Circulation clarifying chamber includes sidewall slope portion, and sidewall slope portion is located at
In concentrating and precipitating room, and sidewall slope portion slopes inwardly from bottom to up.
In a preferred embodiment, sewage purifier provided by the invention includes clear above tube settling room
The upper end liquid outlet of water collecting region, tube settling room is connected to clear water collecting region.
In a preferred embodiment, comprising: the receipts water drum set on the top of clear water collecting region, the side wall for receiving water drum are equipped with
The receipts water through-hole being connected to clear water collecting region；The outlet pipe being connected to the inner cavity for receiving water drum.
In a preferred embodiment, the roof of cyclone sediment room is equipped with the eddy flow being connected to clarification chamber inlet and exports；Rotation
Stream precipitates indoor top and is equipped with spiral deflector, the axis that deflector is exported around eddy flow, and the foreign steamer of deflector
Wide to shrink along direction ecto-entad from top to bottom, the center of deflector is equipped with up and down and the water conservancy diversion with eddy flow outlet
Channel；The top side wall of cyclone sediment room is equipped with the eddy flow entrance towards deflector.
In a preferred embodiment, deflector is the cone spiral vane that outer diameter is gradually reduced from upper end to lower end.
In a preferred embodiment, deflector extends along the vertical direction and coils in the horizontal plane along helix, also,
The depth that deflector extends vertically downwards, is gradually increased from outside to inside.
In a preferred embodiment, including the water conservancy diversion top plate being set to above deflector, deflector is upward along the vertical direction
Extend to water conservancy diversion top plate.
In a preferred embodiment, multiple wave grooves are provided in the plate face of deflector, multiple wave grooves are along vertical side
To being spaced apart.
In a preferred embodiment, sewage purifier provided by the invention includes the water flow being connected to cyclone sediment room
Injector, aqueous stream injectors are for spraying sewage to be clean into cyclone sediment room.
In a preferred embodiment, sewage purifier provided by the invention includes the first sewage pipe, the first sewage pipe
Lower section positioned at Hydraulic Circulation clarifying chamber and the lower section positioned at concentrating and precipitating room；The bottom wall of Hydraulic Circulation clarifying chamber is equipped with and first
First sewage draining exit of sewage pipe connection；The bottom wall of concentrating and precipitating room is equipped with the second sewage draining exit being connected to the first sewage pipe.
In a preferred embodiment, the first sewage pipe is connected to the entrance of aqueous stream injectors.
In a preferred embodiment, sewage purifier provided by the invention includes flocculation reaction room, flocculation reaction room
Set on flow-guiding channel, the top opening and eddy flow outlet of flocculation reaction room, bottom wall of the bottom opening towards cyclone sediment room.
The features of the present invention and advantage are: sewage purifier provided by the invention, are integrated with cyclone sediment room, waterpower is followed
Ring clarifying chamber, concentrating and precipitating room and tube settling room have the characteristics that compact-sized and occupied area is small.Turbid circulating water is after the pressurizing
It enters in cyclone sediment room, can use the overbottom pressure head of itself to subsequent chamber movement, reduce pressurization number and move
Power consumption.Turbid circulating water first isolates the solid particle polluter of larger particles in cyclone sediment room, then sequentially enters
In Hydraulic Circulation clarifying chamber and concentrating and precipitating room, increases the partial size of remaining solid particle polluter in turbid circulating water, realize into one
Step separation enters tube settling room, the solid particle polluter of separation removal smaller particle later.At above-mentioned separation step by step
The technique of reason first removes the biggish solid particle polluter of partial size, then removes the lesser solid particle polluter of partial size, improves purification
The stability of effect ensures the water quality of purified turbid circulating water.
Detailed description of the invention
To describe the technical solutions in the embodiments of the present invention more clearly, make required in being described below to embodiment
Attached drawing is briefly described, it should be apparent that, drawings in the following description are only some embodiments of the invention, for
For those of ordinary skill in the art, without creative efforts, it can also be obtained according to these attached drawings other
Attached drawing.
Fig. 1 is the structural schematic diagram of the first embodiment of sewage purifier provided in an embodiment of the present invention；
Fig. 2 is the structural schematic diagram of second of embodiment of sewage purifier provided in an embodiment of the present invention；
Fig. 3 is the structural schematic diagram of the Hydraulic Circulation clarifying chamber in sewage purifier provided in an embodiment of the present invention；
Fig. 4 is that water delivery through-hole is projected in the distribution schematic diagram in the plane perpendicular to concentrating and precipitating room central axis；
Fig. 5 is the partial enlarged view in Fig. 4 at A；
Fig. 6 is structural schematic diagram of the water delivery through-hole in Hydraulic Circulation clarifying chamber shown in Fig. 4 in vertical direction；
Fig. 7 is the structural schematic diagram of the cyclone sediment room in sewage purifier shown in FIG. 1；
Fig. 8 is that the deflector in cyclone sediment room shown in Fig. 7 is projected in the plane perpendicular to the axis of eddy flow outlet
Structural schematic diagram；
Fig. 9 is the structural schematic diagram of the cyclone sediment room in sewage purifier shown in Fig. 2；
Figure 10 is that the deflector in cyclone sediment room shown in Fig. 9 is projected in the plane perpendicular to the axis of eddy flow outlet
Structural schematic diagram；
Figure 11 is the structural schematic diagram of the another embodiment of the deflector in cyclone sediment room shown in Fig. 9.
Drawing reference numeral explanation:
01, Hydraulic Circulation clarifying chamber；011, chamber inlet is clarified；012, clarifying chamber exports；0121, water delivery through-hole；0122, defeated
Water pipe；013, annular deflector；014, bottom wall rake；015, sidewall slope portion；
02, annulus；021, backflow gap；022, expansion pipe；023, guide shell；024, conical flow guiding pipe；025, it returns
Circulation road；025 ', return flow line；
031, water sprayer trunnion；032, water sprayer nozzle；
04, annulus elevating mechanism；
05, concentrating and precipitating room；06, tube settling room；
07, clear water collecting region；071, water drum is received；0711, water through-hole is received；072, outlet pipe；073, exhaust valve；
08, cyclone sediment room；081, eddy flow entrance；082, eddy flow exports；083, inclined plate；
09, deflector；091, flow-guiding channel；
10, cone spiral vane；
111, spiral channel；112, water conservancy diversion top plate；113, wave groove；
12, the first sewage pipe；121, first annular pipe；122, the second ring pipe；123, flow back branch pipe；131, the first blowdown
Mouthful；132, the second sewage draining exit；
14, aqueous stream injectors；141, sludge inlet；
15, flocculation reaction room；151, upper cylinder；152, slower conical tube；
16, third ring pipe；161, wash tub pipe；171, the second sewage pipe；172, evacuated tube；
181, manhole；182, peep hole is overhauled；183, safety valve.
Specific embodiment
Following will be combined with the drawings in the embodiments of the present invention, and technical solution in the embodiment of the present invention carries out clear, complete
Site preparation description, it is clear that described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.It is based on
Embodiment in the present invention, it is obtained by those of ordinary skill in the art without making creative efforts every other
Embodiment shall fall within the protection scope of the present invention.
As depicted in figs. 1 and 2, the present invention provides a kind of sewage purifiers, comprising: the cyclone sediment room being sequentially communicated
08, Hydraulic Circulation clarifying chamber 01, concentrating and precipitating room 05 and tube settling room 06；Cyclone sediment room 08 is set to Hydraulic Circulation clarifying chamber
01 lower section；Concentrating and precipitating room 05 and tube settling room 06 surround Hydraulic Circulation clarifying chamber 01, also, tube settling room 06 is set
In the top of concentrating and precipitating room 05.
Turbid circulating water enters in cyclone sediment room 08, and eddy flow is formed in cyclone sediment room 08, and solid particle therein is miscellaneous
Matter under the action of the centrifugal, is separated with liquid portion.Then, enter in Hydraulic Circulation clarifying chamber 01 from the bottom up, wherein residual
The lesser solid particle polluter of the partial size stayed flocculates, and granular size incrementally increases；In this process, consolidating after flocculation
Body granule foreign is affected by gravity, and is separated with liquid, is deposited on the bottom wall of Hydraulic Circulation clarifying chamber 01.Due to dense
Contracting mud chamber 05 surrounds Hydraulic Circulation clarifying chamber 01, and turbid circulating water enters concentrating and precipitating room from the side wall of Hydraulic Circulation clarifying chamber 01
In 05, during turbid circulating water moves in concentrating and precipitating room 05, wherein remaining solid particle polluter continues to occur with liquid
Separation, and settled to the bottom of concentrating and precipitating room 05.Turbid circulating water is upwardly into inclined tube from concentrating and precipitating room 05, solid particle
The separation of impurity further progress and sedimentation, and the solid particle polluter settled is fallen in concentrating and precipitating room 05 along inclined tube, and
It is deposited to the bottom of concentrating and precipitating room 05, the solid particle polluter of sedimentation can be collected in the bottom of concentrating and precipitating room 05
Processing.
Sewage purifier provided by the invention is integrated with cyclone sediment room 08, Hydraulic Circulation clarifying chamber 01, concentrating and precipitating
Room 05 and tube settling room 06 have the characteristics that compact-sized and occupied area is small.Turbid circulating water is pressurizeed laggard by booster station
Enter into cyclone sediment room 08, using the overbottom pressure head of itself to subsequent chamber, reduces pressurization number and power disappears
Consumption.Turbid circulating water first isolates the solid particle polluter of larger particles in cyclone sediment room 08, then sequentially enters water
In power circular clarifying room 01 and concentrating and precipitating room 05, increase the partial size of remaining solid particle polluter in turbid circulating water, further
Solid particle polluter is separated, enters tube settling room 06, the solid particle polluter of separation removal smaller particle later.Using upper
The technique for stating separating treatment step by step first removes the biggish solid particle polluter of partial size, then to remove the lesser solid particle of partial size miscellaneous
The stability of clean-up effect can be improved in matter, ensures the water quality of purified turbid circulating water.
In order to make it easy to understand, next each chamber in the sewage purifier is introduced respectively.
The structure of Hydraulic Circulation clarifying chamber is introduced first.
As shown in figure 3, the bottom wall of Hydraulic Circulation clarifying chamber 01 is equipped with clarification chamber inlet 011, Hydraulic Circulation clarifying chamber 01
Side wall is equipped with clarifying chamber outlet 012；The annular sleeve of extension and upper and lower opening along the vertical direction is equipped in Hydraulic Circulation clarifying chamber 01
Cylinder 02 is equipped with backflow gap 021, and annulus between the lower end of annulus 02 and the bottom wall of Hydraulic Circulation clarifying chamber 01
The opening direction and covering clarification chamber inlet 011 of 02 lower end.
Turbid circulating water enters the annulus 02 in Hydraulic Circulation clarifying chamber 01 by clarification chamber inlet 011 from the bottom up, and
Continue to flow up in annulus 02.During turbid circulating water flows up in annulus 02, solid therein
Grain impurity flocculates, and granular size incrementally increases.
Turbid circulating water is flowed out from the upper opening of annulus 02, is collided with the roof of Hydraulic Circulation clarifying chamber 01, is turned
It is flowed to the clarifying chamber outlet 012 for being located at surrounding.In this process, shadow of the solid particle polluter after flocculation by gravity
It rings, separates, be deposited on the bottom wall of Hydraulic Circulation clarifying chamber 01 with liquid.
Due to there is the water flow that flows up with larger speed in annulus 02 so that pressure in annulus 02 compared with
It is small.So a part of turbid circulating water and a part are deposited to the solid particle polluter on the bottom wall of Hydraulic Circulation clarifying chamber 01, pressing
It is strong it is poor under the action of, can be re-introduced into annulus 02 by backflow gap 021.In this way, turbid circulating water can be made to be recycled
Multiple flocculation and sedimentation is conducive to isolate solid particle polluter therein.And it is re-introduced into annulus 02
Solid particle polluter can play the role of the nuclei of condensation, and turbid circulating water is promoted to flocculate in annulus 02, further improve
Remove the effect of solid particle polluter.
Clarifying chamber outlet 012 is set on the side wall of Hydraulic Circulation clarifying chamber 01, turbid circulating water can be made from annulus 02
Upper end opening outflow after, liquid portion moves around from center, and flocculate after solid particle polluter due to self gravity
It is larger, then can falls downward, separated convenient for solid particle polluter with liquid portion.Preferably, clarifying chamber outlet 012 is set to
The bottom of 01 side wall of Hydraulic Circulation clarifying chamber further improves separating effect to extend the flow path of turbid circulating water.
In one embodiment of the present invention, the upper end of annulus 02 is connected with expansion pipe 022, expands the interior of pipe 022
Diameter is gradually increased along direction from bottom to top.Turbid circulating water in annulus 02 from flowing upwardly into expansion pipe 022, since expansion is managed
022 cross section is gradually increased, and is gradually reduced flow velocity of the turbid circulating water in expansion pipe 022, is conducive to turbid circulating water and flocculates.
Further, the upper end for expanding pipe 022 is connected with guide shell 023, and the internal diameter of guide shell 023 is protected from upper end to lower end
It holds consistent.When turbid circulating water flows in expanding pipe 022, spread outward from center；By guide shell 023, turbid circulating water is received
Hold together, spray turbid circulating water from guide shell 023 along direction straight up, after reducing the solid particle polluter ejection in turbid circulating water
In Hydraulic Circulation clarifying chamber 01 flowing water square to component velocity, be conducive to solid particle polluter and settle downwards.
As shown in figure 3, in one embodiment of the present invention, comprising: water sprayer nozzle 032 and water sprayer trunnion 031, water
The inner wall of Hydraulic Circulation clarifying chamber 01 is fixed in the lower end of injector nozzles 032, and is connected to clarification chamber inlet 011；Water sprayer larynx
The lower end of pipe 031 is connected to water sprayer nozzle 032, and upper end is equipped with opening upward, and the upper end of water sprayer trunnion 031 is protruded into
Into annulus 02.Turbid circulating water into clarification chamber inlet 011 enters in water sprayer trunnion 031 by water sprayer nozzle 032,
And annulus 02 is flowed upwardly by the upper end opening of water sprayer trunnion 031；Also, the internal diameter of annulus 02 is greater than water-jet
The outer diameter of device trunnion 031, so that forming return flow line between the inner wall of annulus 02 and the outer wall of water sprayer trunnion 031
025.Turbid circulating water is sprayed by water sprayer trunnion 031 into annulus 02, is conducive to increase turbid circulating water and is entered annulus
Flow velocity when 02 passes through back to reduce the pressure in annulus 02 convenient for turbid circulating water and its solid particle polluter of sedimentation
Ebb interval 021 and return flow line 025 are back in annulus 02.Preferably, the internal diameter of water sprayer nozzle 032 is supreme from lower end
End is gradually reduced, so that flow velocity of the turbid circulating water in water sprayer nozzle 032 is gradually increased.
Further, the piping connection of flocculation aid will be added in water sprayer nozzle 032, flocculation aid flows into water by the pipeline
In injector nozzles 032, and when being flowed in water sprayer nozzle 032 and water sprayer trunnion 031 with turbid circulating water, carried out with turbid circulating water
Mixing.
In one embodiment of the present invention, the lower end of annulus 02 is equipped with conical flow guiding pipe 024, conical flow guiding pipe
024 internal diameter is gradually increased along direction from the top down, so that the internal diameter of the opening of 02 lower end of annulus is along from the top down
Direction is gradually increased, in order to which turbid circulating water and the solid particle polluter being deposited on 01 bottom wall of Hydraulic Circulation clarifying chamber enter ring
In shape sleeve 02.Moreover, when the outer diameter of water sprayer nozzle 032 is gradually reduced from lower end to upper end, conical flow guiding pipe 024 it is interior
The outer wall of wall and water sprayer nozzle 032 cooperates, and is formed from the surrounding inclined return flow line 025 ' in center upwards, the turbid ring of reflux
Water and solid particle polluter enter in annulus 02 along return flow line 025 ', can with spray from water sprayer trunnion 031
Convergence and collision occur for turbid circulating water, are conducive to be mixed.
In one embodiment of the present invention, referring to figure 3., which includes annulus elevating mechanism
04, annulus elevating mechanism 04 is for driving annulus 02 to move up and down, to control lower end surface and the water of annulus 02
The distance between the bottom wall of power circular clarifying room 01 L adjusts the size of backflow gap 021, thus to turbid circulating water and solid particle
The regurgitant volume that impurity is flowed back into annulus 02 by backflow gap 021 is adjusted, change the turbid circulating water of reflux with from water
Ratio between the new water of the turbid circulating water sprayed in emitter trunnion 031.When the water of the turbid circulating water entered in Hydraulic Circulation clarifying chamber 01
It, can be by the way that adjust should when matter changes, or when the flow velocity that turbid circulating water enters in Hydraulic Circulation clarifying chamber 01 changes
Ratio, clean-up effect to be adjusted, so that the water quality from the turbid circulating water of 012 discharge of clarifying chamber outlet is more stable.
In order to keep annulus 02 more steadily mobile relative to Hydraulic Circulation clarifying chamber 01, Hydraulic Circulation clarifying chamber
Roof is fixed with the guide rod extended straight down；The side wall of annulus 02 is fixed with guide sleeve, and guide rod is arranged in guide sleeve.
By guide rod, pessum sleeve 02 moves along the vertical direction.The structure of annulus elevating mechanism 04 is not limited to one kind, one
In a little embodiments, annulus elevating mechanism 04 includes shaft, be installed on the gear of shaft and be installed on annulus 02 and
The rack gear being arranged along the vertical direction, wheel and rack are meshed.The horizontally extending shell to the sewage purifier of shaft
In vitro, for operator's manual actuation；Sealing cooperation between shaft and the shell of sewage purifier.
Further, 04 outside installation site sensor of annulus elevating mechanism monitors annulus using sensor
02 position can determine the turbid circulating water of reflux and the turbid circulating water sprayed from water sprayer trunnion 031 according to 02 position of annulus
Ratio between new water.Specifically, position sensor is mounted on the outside of annulus 02, detects under conical flow guiding pipe 024
The distance between end and the bottom wall of Hydraulic Circulation clarifying chamber 01 L；Using finite simulation element analysis software, calculates distance L and take difference
The volume ratio value of flow when height value determines the corresponding different flow-rate ratio of different height.
Flow proportional value when different distance L value is analyzed using finite element fluid software, determination is for inquiry and distance L
It is worth the table of corresponding flow proportional value, different distance L corresponds to different flow proportional values.When actual motion, distance is determined
L can determine flow ratio.When volume ratio value is greater than 2:1, there can be preferable flocculating setting effect.Preferably, it returns
The turbid circulating water of stream and from the volume ratio range between the new water of turbid circulating water sprayed in water sprayer trunnion 031 be 2:1-8:1.
In one embodiment of the present invention, annular deflector 013, annular deflector are equipped in Hydraulic Circulation clarifying chamber 01
013 outer profile is connected to the inner wall of Hydraulic Circulation clarifying chamber 01；Clarifying chamber outlet 012 is set to annular deflector 013 and waterpower
Between the bottom wall of circular clarifying room 01.Turbid circulating water enters in Hydraulic Circulation clarifying chamber 01 downwards after flowing out in annulus 02
Movement, the solid particle polluter after on the one hand flocculating collides annular deflector 013, and can be attached on annular deflector 013,
It may advantageously facilitate solid particle polluter to separate from turbid circulating water；On the other hand, clarifying chamber outlet 012 is located at annular deflector
013 lower section, annular deflector 013 can make flow path of the turbid circulating water in Hydraulic Circulation clarifying chamber 01 change, due to
The gravity of solid particle polluter is larger, is influenced in motion process by biggish self gravity, therefore is conducive to promote solid
Granule foreign is separated with liquid portion.
Further, annular deflector 013 is tilted down from outer profile to Internal periphery, in order to be deposited to annular steering
Solid particle polluter slides downwards to the bottom of Hydraulic Circulation clarifying chamber 01 on plate 013.In addition, solid particle polluter can also adhere to
Onto the outer wall of conical flow guiding pipe 024, the outer wall of conical flow guiding pipe 024 inclined downward outward, bootable solid particle polluter
It is slid to the bottom wall of Hydraulic Circulation clarifying chamber 01.
Further.Referring to figure 3., the bottom wall of Hydraulic Circulation clarifying chamber 01 includes bottom wall rake 014, bottom wall rake
014 outer profile is connect with the side wall of Hydraulic Circulation clarifying chamber 01, and the Internal periphery of bottom wall rake 014 is clarified close to Hydraulic Circulation
The central axis of room；Bottom wall rake 014 is tilted down from outer profile to Internal periphery.Bottom wall rake 014 and annular turn to
Plate 013 cooperate, form inclined water stream channel, by turbid circulating water introduce clarifying chamber outlet 012, turbid circulating water along the water stream channel to
Upper flowing is conducive to solid particle polluter separation and sedimentation.Preferably, the angle and bottom wall that annular deflector 013 tilts down
The angle that rake 014 tilts down is equal.
Next introduce the structure of concentrating and precipitating room, and, concentrating and precipitating room and Hydraulic Circulation clarifying chamber how the company of realization
It connects.
As depicted in figs. 1 and 2, concentrating and precipitating room 05 surrounds Hydraulic Circulation clarifying chamber 01, and clarifying chamber outlet 012 and concentration are heavy
Shallow lake room 05 is connected to；The bottom wall of concentrating and precipitating room 05 and the bottom wall of Hydraulic Circulation clarifying chamber 01 link together；Pass through Hydraulic Circulation
The side wall of clarifying chamber 01 separates concentrating and precipitating room 05.Close to the bottom of concentrating and precipitating room 05, concentration is heavy for clarifying chamber outlet 012
The top of shallow lake room 05 is equipped with outlet.It is heavy to enter concentration by clarifying chamber outlet 012 for turbid circulating water in Hydraulic Circulation clarifying chamber 01
In shallow lake room 05, and to the exit movement at top.During turbid circulating water moves in concentrating and precipitating room 05, solid particle polluter with
Liquid portion separation, settles to the bottom of concentrating and precipitating room 05.
In one embodiment of the present invention, as shown in Figure 5 and Figure 6, clarifying chamber outlet 012 is set to waterpower including multiple
The water delivery through-hole 0121 of the side wall of circular clarifying room 01, the both ends of each water delivery through-hole 0121 respectively with Hydraulic Circulation clarifying chamber 01
It is connected to concentrating and precipitating room 05.By water delivery through-hole 0121, enter turbid circulating water in a manner of spraying in concentrating and precipitating room 05,
Be conducive to make the solid particle polluter collision in turbid circulating water and be adsorbed on the inner wall of concentrating and precipitating room 05.Specifically, multiple
Axis of the water delivery through-hole 0121 along Hydraulic Circulation clarifying chamber 01 is at least scattered in two layers；Within the same layer, each water delivery through-hole
0121 around Hydraulic Circulation clarifying chamber 01 central axis circle distribution.
Further, the axis of water delivery through-hole 0121 deviates the central axis of Hydraulic Circulation clarifying chamber 01 in the same direction.
When turbid circulating water is sprayed along the axis of water delivery through-hole 0121 into concentrating and precipitating room 05, turbid circulating water has circumferential point speed
Degree, to make center axis thereof of the turbid circulating water in concentrating and precipitating room 05 around Hydraulic Circulation clarifying chamber 01, and from each
The rotation direction for the turbid circulating water that water delivery through-hole ejects is identical, so that turbid circulating water forms eddy flow in concentrating and precipitating room 05.Solid
Granule foreign under the action of the centrifugal, can be separated with liquid portion, and a part of solid particle polluter can be heavy while rotation
The bottom of concentrating and precipitating room 05 is dropped to, a part of solid particle polluter can collide and be adsorbed onto the inner wall in 05 outside of concentrating and precipitating room
On, and gradually land.
In the present embodiment, the central axis weight of the central axis of concentrating and precipitating room 05 and Hydraulic Circulation clarifying chamber 01
It closes.Referring to figure 4. and Fig. 5, Fig. 4 are that water delivery through-hole is projected in the distribution in the plane perpendicular to 05 central axis of concentrating and precipitating room
Schematic diagram, in Fig. 4, the inner wall of Hydraulic Circulation clarifying chamber 01 is circle, and the axis of water delivery through-hole 0121 intersects with the circle, mistake
Angle β between the radius and the axis of water delivery through-hole 0121 of the intersection point is the angle of inclination beta of water delivery through-hole 0121.It is preferred that
The angle of inclination beta on ground, each water delivery through-hole 0121 is equal, also, -55 °≤β≤55 °.
Further, the axis of each water delivery through-hole 0121 tilts down.As shown in fig. 6, the axis of water delivery through-hole 0121
Angle between line and horizontal plane is α.Since the opening of concentrating and precipitating room 05 is disposed over, turbid circulating water is from water delivery through-hole 0121
Middle ejection can be moved downward first into after concentrating and precipitating room 05, then turn to move upwards.Solid particle polluter self gravity
It is larger, it is not easy to obtain upward motion energy, bottom wall of the meeting in this process with concentrating and precipitating room 05 collides, and is inhaled
It is attached.Preferably, 15 °≤α≤45 °.
Further, water-supply-pipe 0122 is connected on water delivery through-hole 0121, water-supply-pipe 0122 prolongs into concentrating and precipitating room 05
It stretches, the axis of water-supply-pipe 0122 is overlapped with the axis of water delivery through-hole 0121, and water-supply-pipe 0122 plays guiding to the movement of turbid circulating water
Effect, promotes turbid circulating water to enter concentrating and precipitating room 05 along the axis of water delivery through-hole 0121.
Next the structure of tube settling room is introduced, and, tube settling room, concentrating and precipitating room and Hydraulic Circulation clarifying chamber
How connection is realized.
As depicted in figs. 1 and 2, tube settling room 06 is set to the top of concentrating and precipitating room 05, in tube settling room 06 side by side
More inclined tubes are tiltedly installed with, the lower ending opening of each inclined tube is connected to the lower end inlet of tube settling room 06, each inclined tube
Upper end opening be connected to the upper end liquid outlet of tube settling room 06.The lower end inlet of tube settling room 06 and concentrating and precipitating room
05 top connection.
The cross section of the vertical inclined tube axis of inclined tube can be round or ellipse.Preferably, the vertical inclined tube of inclined tube
The cross section of axis is oval, is conducive to the contact area for increasing tube wall, more conducively arrested particles.
Inclined tube can use hollow tube；Inclined tube tube bank is used as filler inclined tube.The top of concentrating and precipitating room 05 is welded and connected with
Inclined tube bracket, inclined tube bracket are supported inclined tube.
In some embodiments, inclined tube is formed by connecting by several sectorial blocks by tongue-and-groove.The connection of inclined tube bracket lower part is more
A guide fluid grating, guide fluid grating are in vertical plate-like, positioned at the lower part of tube settling room 06, and are installed on the side of concentrating and precipitating room 05
Wall；Multiple guide fluid gratings are arranged along horizontal circumference.Guide fluid grating can support inclined tube bracket, while guide fluid grating is located at concentration and sinks
The top of shallow lake room 05 can carry out water conservancy diversion to the water flow in concentrating and precipitating room 05, so that 05 internal upper part region shape of concentrating and precipitating room
At stable upper up-flow, cyclonic effect is eliminated, the uniformity of oblique in-pipe flow is improved, is conducive to the water flow in inclined tube and keep stablizing
Uniformly.
Turbid circulating water is upwardly into inclined tube from concentrating and precipitating room 05, and solid particle polluter further progress is separated and sunk
Drop, and the solid particle polluter settled is fallen in concentrating and precipitating room 05 along inclined tube.In order to make tube settling room 06 have compared with
Good sedimentation effect, the angular range between the axis and horizontal line of each inclined tube are 55 °~65 °；Preferably, each inclined tube
Angle between axis and horizontal line is 60 °.
In one embodiment of the present invention, the side wall of Hydraulic Circulation clarifying chamber 01 includes sidewall slope portion 015, and side wall inclines
Inclined portion 015 is located in concentrating and precipitating room 05, and sidewall slope portion 015 slopes inwardly from bottom to up, so that concentrating and precipitating room 05
The area of section of horizontal direction be gradually increased along direction from the bottom up, to reduce turbid circulating water in concentrating and precipitating room 05
Flow velocity is settled convenient for solid particle polluter, and enters turbid circulating water in inclined tube with lower speed, can be improved turbid
The utilization rate of ring water residence time and inclined tube in inclined tube enhances sedimentation effect.
Tube settling room 06 is annular, and surrounds Hydraulic Circulation clarifying chamber 01, and tube settling room 06 and Hydraulic Circulation are clarified
It is separated between room 01 by the side wall of Hydraulic Circulation clarifying chamber 01, in this way, being conducive to save space, reduces the sewage purifier
The size of vertical direction.
Further, sewage purifier provided by the invention further includes clear water collecting region 07, and clear water collecting region 07 is set to
The upper end liquid outlet of the top of tube settling room 06, tube settling room 06 is connected to clear water collecting region 07.Turbid circulating water passes through inclined tube
It travels up in clear water collecting region 07, and is stored in clear water collecting region 07, recycled in order to discharge.
The top of clear water collecting region 07, which is equipped with, receives water drum 071, and the side wall for receiving water drum 071 is equipped with to be connected to clear water collecting region 07
Receipts water through-hole 0711；It receives water drum 071 and is connected with outlet pipe 072, the turbid circulating water in clear water collecting region 07, which reaches, receives water through-hole
After 0711 height, entered in receipts water drum 071 by receiving water through-hole 0711, and through outlet pipe 072, it is direct using hydraulic pressure more than needed
It send to pressure filter or cooling tower.Preferably, receiving water drum 071 is funnel-shaped structure, and multiple receipts water through-holes 0711 are distributed in
On the tapered sidewalls of funnel-shaped structure, to increase the uniformity coefficient of water flow.In some embodiments, water drum 071 is received to be connected with
Exhaust valve 073 reduces the air pressure received in water drum 071 by exhaust valve 073, receives in water drum 071 in order to which turbid circulating water enters.
Next structure and cyclone sediment room, the concentrating and precipitating room and Hydraulic Circulation clarifying chamber of cyclone sediment room are introduced
How connection is realized.
Cyclone sediment room 08 is set to the lower section of Hydraulic Circulation clarifying chamber 01, and by the bottom wall of Hydraulic Circulation clarifying chamber 01 with
Hydraulic Circulation clarifying chamber 01 is spaced, and is spaced by the bottom wall and concentrating and precipitating room 05 of concentrating and precipitating room 05.Cyclone sediment room
08 roof is equipped with the eddy flow outlet 082 being connected to clarification chamber inlet 011；Top in cyclone sediment room 08 is equipped with spiral
Deflector 09, deflector 09 around eddy flow outlet 082 axis, and deflector 09 outer profile along from top to bottom direction by
Export-oriented contract, the center of deflector 09 are equipped with up and down and export 082 flow-guiding channel 091 being connected to eddy flow；Eddy flow is heavy
The top side wall of shallow lake room 08 is equipped with the eddy flow entrance 081 towards deflector 09.
Turbid circulating water is entered in cyclone sediment room 08 by eddy flow entrance 081, and is flowed to deflector 09；In itself initial velocity
Under the action of degree, self gravity and deflector 09, turbid circulating water is along deflector 09, from top to bottom around the axis of eddy flow outlet 082
Rotation, lower ending opening of the cocurrent to flow-guiding channel 091；Moved upwards after into flow-guiding channel 091, by eddy flow outlet 082 into
Enter into clarification chamber inlet 011.During turbid circulating water rotates in cyclone sediment room 08, solid particle polluter therein from
Under heart effect, separated with liquid portion.
In one embodiment of the present invention, as shown in Figure 7 and Figure 8, deflector 09 be outer diameter from upper end to lower end gradually
Reduced cone spiral vane 10.The turbid circulating water that eddy flow entrance 081 ejects has to leading positioned at 08 center of cyclone sediment room
The trend of the lower ending opening flowing of circulation road 091, cone spiral vane 10 play guiding function to the flow path of turbid circulating water, make
Turbid circulating water is formed in cyclone sediment room 08 stablizes eddy flow.Solid particle polluter in turbid circulating water under the action of the centrifugal, with liquid
Part separates, and collides and is adsorbed on the side wall of cyclone sediment room 08, and gradually falls to the bottom of cyclone sediment room 08
Portion.
The eddy flow formed under the guidance of cone spiral vane 10, the outer diameter of eddy flow gradually reduce, and solid particle polluter
Own wt is larger, it is easier to separate under the action of the centrifugal with liquid portion.
Alternatively, Fig. 9-Figure 11 is please referred to, deflector 09 extends along the vertical direction and edge in the horizontal plane
Helix coiling, also, the depth that deflector 09 extends vertically downwards, are gradually increased from outside to inside.Deflector 09
Lower edge constitutes the outer profile of deflector 09, and shrinks along direction ecto-entad from top to bottom.Figure 10 is projected in for deflector
Spiral channel is formed in deflector 09 in Figure 10 perpendicular to the structural schematic diagram in the plane of the axis of eddy flow outlet
111.Turbid circulating water enters in the spiral channel 111 from upper end, can be in spiral channel under the action of deflector 09
Axis rotation in 111 around eddy flow outlet 082 forms rotation and at the same time moving down to the lower ending opening of flow-guiding channel 091
Stream；Under the induced effect of the eddy flow in the spiral channel 111, the turbid circulating water in cyclone sediment room 08 also forms eddy flow.
When carrying out eddy flow, solid particle polluter is separated with liquid portion turbid circulating water under the action of the centrifugal, is collided and is adsorbed onto and leads
On the side wall of flowing plate 09 and on the inner wall of cyclone sediment room 08, and gradually fall to the bottom of cyclone sediment room 08.
Further, as shown in figure 11, above deflector 09 be equipped with water conservancy diversion top plate 112, deflector 09 along the vertical direction to
On extend to water conservancy diversion top plate 112, water conservancy diversion top plate 112 is top closed by above-mentioned spiral channel 111, avoids above-mentioned spiral shape
Channel 111 in turbid circulating water overflow upwards, promote turbid circulating water to flow down along above-mentioned spiral channel 111, be conducive to solid
Body granule foreign is separated.
It when in order to collide solid particle polluter on deflector 09, is preferably adsorbed by deflector 09, inventor is to leading
Flowing plate 09 advanced optimizes, and as shown in figure 11, multiple wave grooves 113, multiple ripples is provided in the plate face of deflector 09
Slot 113 is spaced apart along the vertical direction, on the one hand by setting wave groove 113, is increased and is contacted on deflector 09 with turbid circulating water
Area, solid particle polluter of being on the other hand more convenient for stops and assembles on deflector 09.
The specific embodiment of deflector 09 is described above, next 08 other structures of cyclone sediment room are changed
Into being described.
As shown in figures 7 and 9, the bottom of cyclone sediment room 08 is set as taper, and horizontal cross-section is gradually reduced from top to bottom, with
It is moved along inner wall to bottom centre convenient for the solid particle polluter of sedimentation, convenient for discharge.Deflector 09 and cyclone sediment room 08
Gap is equipped between inner wall, in order to solid particle polluter sedimentation.
Further, which includes the aqueous stream injectors 14 for being set to eddy flow entrance 081, aqueous stream injectors
14 for spraying sewage to be clean to deflector 09.By aqueous stream injectors 14, turbid circulating water can be made with biggish speed
It enters in cyclone sediment room 08, solid particle polluter is promoted to separate under the action of the centrifugal with liquid portion.
For the ease of by the solid of 01 bottom of the solid particle polluter of 05 bottom of concentrating and precipitating room and Hydraulic Circulation clarifying chamber
Granule foreign discharge, sewage purifier include the first sewage pipe 12, and the first sewage pipe 12 is located at Hydraulic Circulation clarifying chamber 01
Lower section and the lower section for being located at concentrating and precipitating room 05；The bottom wall of Hydraulic Circulation clarifying chamber 01 is equipped with the be connected to the first sewage pipe 12
One sewage draining exit 131；The bottom wall of concentrating and precipitating room 05 is equipped with the second sewage draining exit 132 being connected to the first sewage pipe 12.Specifically,
One sewage pipe 12 includes blow-off line, positioned at the first annular pipe 121 of 01 lower section of Hydraulic Circulation clarifying chamber and positioned at concentrating and precipitating
Second ring pipe 122 of 05 lower section of room, blow-off line are connected to first annular pipe 121 and are connected to the second ring pipe 122, first
Ring pipe 121 is connected to by blow down branch with the first sewage draining exit 131, and the second ring pipe 122 passes through blow down branch and the second blowdown
Mouth 132 is connected to.Blow-off line is equipped with valve, by periodically turning on the valve, solid particle polluter is discharged.
Preferably, 2 the first sewage draining exits 131 are at least symmetrically arranged in Hydraulic Circulation clarifying chamber 01, on concentrating and precipitating room 05
At least it is symmetrically arranged with 2 the second sewage draining exits 132.
Preferably, the axis of the first sewage draining exit 131 opens up along the vertical direction, and the axis of the first sewage draining exit 131 is followed with waterpower
The distance between the central axis of ring clarifying chamber 01 K is not less than 200mm, to guarantee the bottom centre in Hydraulic Circulation clarifying chamber 01
Gathering has solid particle polluter, is flowed back with providing solid particle polluter into annulus 02.
In some embodiments, the first sewage pipe 12 is connected to the entrance of aqueous stream injectors 14.Specifically, water flow jet
The arrival end of device 14 is equipped with sludge inlet 141, and the first sewage pipe 12 is connected to by the branch pipe 123 that flows back with the sludge inlet 141.The
Solid particle polluter in one sewage pipe 12 can be entered directly into aqueous stream injectors 14 by the branch pipe 123 that flows back, and be improved solid
The efficiency that body granule foreign flows back, can be to avoid adding external pressurized equipment.Turbid circulating water in aqueous stream injectors 14
Under drive, solid particle polluter is admixed together with turbid circulating water, and is crushed under the impact of water flow, and particle becomes smaller.Pass through
Aqueous stream injectors 14 back flow into the solid particle polluter in cyclone sediment room 08, can play the role of the nuclei of condensation, promote
Solid particle polluter in turbid circulating water agglomerates to together, is convenient for separating clarifying, to reduce the addition of the chemical reagent such as flocculation aid
Amount.Preferably, the axis of reflux branch pipe 123, from one end of close first sewage pipe 12 to one end close to aqueous stream injectors 14,
To be tilted along the injection direction of aqueous stream injectors 14, in order to which the solid particle polluter in the first sewage pipe 12 enters water flow spray
In emitter 14, and preferably crushed.
For the ease of the sludge in cyclone sediment room 08 to be discharged, the bottom of cyclone sediment room 08 is equipped with the second sewage pipe
171.Second sewage pipe 171 is equipped with valve, periodically the sludge of deposition can be discharged by valve.Preferably, such as Fig. 7 institute
Show, the bottom of 08 inner cavity of cyclone sediment room is equipped with inclined plate 083, and for carrying sludge, the mud inlet of the second sewage pipe 171 is set to oblique
The top of plate 083.In some embodiments, the bottom of cyclone sediment room 08 is additionally provided with evacuated tube 172, sets in evacuated tube 172
There is emptying valve.
Further, which includes flocculation reaction room 15, and flocculation reaction room 15 is set to flow-guiding channel 091,
The top opening of flocculation reaction room 15 is connected to eddy flow outlet 082, bottom wall of the bottom opening towards cyclone sediment room 08.Such as Fig. 7
With shown in Fig. 9, flocculation reaction room 15 includes upper cylinder 151 and slower conical tube 152, and cyclone sediment is fixed in the upper end of upper cylinder 151
The roof of room 08, and be connected to eddy flow outlet 082, the upper end of slower conical tube 152 is connected to the lower end of cylinder 151, slower conical tube 152
Internal diameter be gradually increased from top to bottom；The axis of the axis of upper cylinder 151 and the axis of slower conical tube 152 with eddy flow outlet 082
It is overlapped.The lower part of 152 inner cavity of top and slower conical tube of upper 151 inner cavity of cylinder is respectively equipped with sieve plate or orifice plate, in upper and lower sieve
Space between plate or orifice plate is equipped with multiple hollow ball shape flocculation reactors；Sieve plate or orifice plate be it is dismountable, in order to
Replace hollow ball shape flocculation reactor.Deflector 09 is fixedly installed on the outer wall of cylinder and the outer wall of slower conical tube.
Turbid circulating water in cyclone sediment room 08 is moved downward along deflector 09, is entered from the lower ending opening of slower conical tube 152
In slower conical tube 152 and upper cylinder 151, and hollow ball shape flocculation reactor is flowed through, flocculation reaction occurs, makes solid particle polluter
Partial size increase；It is discharged by the upper end opening of upper cylinder 151, and is flowed by eddy flow outlet 082 and clarification chamber inlet 011
In Hydraulic Circulation clarifying chamber 01.
Sewage purifier provided by the invention is integrated with cyclone sediment room 08, flocculation reaction room 15, Hydraulic Circulation clarification
Room 01, concentrating and precipitating room 05, tube settling room 06 and clear water collecting region 07 have the characteristics that compact-sized and occupied area is small.
Turbid circulating water enters in cyclone sediment room 08 after being pressurizeed by booster station, and using the overbottom pressure head of itself to subsequent net
Change process chamber and the flowing of clear water collecting region, reduces pressurization number and power consumption.Turbid circulating water is first in cyclone sediment room 08
The solid particle polluter of larger particles is isolated, then passes through flocculation reaction room 15, makes remaining solid particle in turbid circulating water
The partial size of impurity increases, in order to separate；The turbid circulating water being discharged from flocculation reaction room 15 sequentially enters Hydraulic Circulation clarification
In room 01 and concentrating and precipitating room 05, further separate solid particle polluter, enter tube settling room 06 later, separation removal compared with
Short grained solid particle polluter.Using the technique of above-mentioned separating treatment step by step, the biggish solid particle polluter of partial size is first removed,
The lesser solid particle polluter of partial size is removed again, the stability of clean-up effect can be improved, and ensures the water of purified turbid circulating water
Matter.
Third annular is equipped with for the ease of being rinsed to the internal cavities in cyclone sediment room 08, in cyclone sediment room 08
The tube wall of pipe 16, third ring pipe 16 is equipped with multiple water outlets；Third ring pipe 16 passes through wash tub pipe 161 and external water supply
Piping connection, the water into third ring pipe 16 are sprayed by the water outlet on tube wall into cyclone sediment room 08, are realized and are rinsed.
For the ease of maintenance, and ensure the safe and stable operation of equipment, side wall, Hydraulic Circulation in cyclone sediment room 08
The top side wall of clarifying chamber 01 and the roof of clear water collecting region 07 are respectively equipped with manhole 181, the side wall in concentrating and precipitating room 05
Equipped with maintenance peep hole 182, the roof of clear water collecting region 07 is equipped with the safety valve 183 being connected to clear water collecting region 07.
The foregoing is merely several embodiments of the present invention, and those skilled in the art is according to application documents disclosure
Various changes or modifications can be carried out without departing from the spirit and scope of the present invention to the embodiment of the present invention.
Claims (28)
1. a kind of sewage purifier characterized by comprising the cyclone sediment room that is sequentially communicated, Hydraulic Circulation clarifying chamber, dense
Contracting mud chamber and tube settling room；
The cyclone sediment room is set to the lower section of the Hydraulic Circulation clarifying chamber；
The concentrating and precipitating room and the tube settling room surround the Hydraulic Circulation clarifying chamber, also, the tube settling
Room is set to the top of the concentrating and precipitating room.
2. sewage purifier according to claim 1, which is characterized in that the bottom wall of the Hydraulic Circulation clarifying chamber is equipped with
Chamber inlet is clarified, the side wall of the Hydraulic Circulation clarifying chamber is exported equipped with clarifying chamber；
The annulus of extension and upper and lower opening along the vertical direction is equipped in the Hydraulic Circulation clarifying chamber, the annulus
Backflow gap, and the opening court of the lower end of the annulus are equipped between lower end and the bottom wall of the Hydraulic Circulation clarifying chamber
To and the covering clarification chamber inlet.
3. sewage purifier according to claim 2, which is characterized in that the clarifying chamber outlet is set to the waterpower
The bottom of the side wall of circular clarifying room.
4. sewage purifier according to claim 2, which is characterized in that the upper end of the annulus is connected with expansion
The internal diameter of pipe, the expansion pipe is gradually increased along direction from bottom to top.
5. sewage purifier according to claim 4, which is characterized in that the upper end of the expansion pipe is connected with water conservancy diversion
Cylinder, the internal diameter of the guide shell are consistent from upper end to lower end.
6. sewage purifier according to claim 2 characterized by comprising water sprayer trunnion, the water sprayer larynx
The lower end of pipe is connected to the clarification chamber inlet, and upper end is equipped with opening upward, and the annulus surrounds the water sprayer larynx
The upper end of pipe, the fluid into the clarification chamber inlet can flow upwardly into the annulus by the water sprayer trunnion,
Also, return flow line is equipped between the inner wall of the annulus and the outer wall of the water sprayer trunnion.
7. sewage purifier according to claim 6, which is characterized in that including be set to the water sprayer trunnion with it is described
The water sprayer nozzle between chamber inlet is clarified, the lower end of the water sprayer nozzle is connected to the clarification chamber inlet, the water-jet
The lower end of device trunnion is connected to the upper end of the water sprayer nozzle, and the internal diameter of the water sprayer nozzle gradually subtracts from lower end to upper end
It is small.
8. sewage purifier according to claim 2, which is characterized in that the internal diameter of the opening of the annulus lower end
It is gradually increased along direction from the top down.
9. sewage purifier according to claim 2, which is characterized in that the sewage purifier includes for driving
The annulus elevating mechanism that the annulus moves up and down.
10. sewage purifier according to claim 2 characterized by comprising be set to the Hydraulic Circulation clarification
Indoor annular deflector, the outer profile of the annular deflector are connected to the inner wall of the Hydraulic Circulation clarifying chamber；It is described clear
Clear room outlet is set between the annular deflector and the bottom wall of the Hydraulic Circulation clarifying chamber.
11. sewage purifier according to claim 10, which is characterized in that the annular deflector is from outer profile to interior
Profile is to tilt down.
12. sewage purifier according to claim 11, which is characterized in that the bottom wall packet of the Hydraulic Circulation clarifying chamber
Bottom wall rake is included, the outer profile of the bottom wall rake is connect with the side wall of the Hydraulic Circulation clarifying chamber, and the bottom wall inclines
Central axis of the Internal periphery of inclined portion close to the Hydraulic Circulation clarifying chamber；The bottom wall rake is from outer profile to Internal periphery
It tilts down.
13. sewage purifier according to claim 1, which is characterized in that the clarifying chamber outlet includes multiple water deliverys
The both ends of through-hole, each water delivery through-hole are connected to the Hydraulic Circulation clarifying chamber and the concentrating and precipitating room respectively.
14. sewage purifier according to claim 13, which is characterized in that the axis of each water delivery through-hole is along same
Deviate the central axis of the Hydraulic Circulation clarifying chamber in one direction.
15. sewage purifier according to claim 14, which is characterized in that the axis of each water delivery through-hole to
Lower inclination.
16. sewage purifier described in any one of 3-15 according to claim 1 characterized by comprising multiple to be connected to
The water-supply-pipe of the water delivery through-hole, the water-supply-pipe extend into the concentrating and precipitating room.
17. sewage purifier according to claim 1, which is characterized in that the side wall packet of the Hydraulic Circulation clarifying chamber
Include sidewall slope portion, the sidewall slope portion is located in the concentrating and precipitating room, and the sidewall slope portion from bottom to up to
It is tilted.
18. sewage purifier according to claim 1, which is characterized in that the sewage purifier includes being set to institute
The clear water collecting region above tube settling room is stated, the upper end liquid outlet of the tube settling room is connected to the clear water collecting region.
19. sewage purifier according to claim 18 characterized by comprising
Receipts water drum set on the top of the clear water collecting region, the side wall for receiving water drum is equipped with to be connected to the clear water collecting region
Receipts water through-hole；
The outlet pipe being connected to the inner cavity for receiving water drum.
20. sewage purifier according to claim 1, which is characterized in that the roof of the cyclone sediment room be equipped with
The eddy flow outlet of the clarification chamber inlet connection；
The indoor top of cyclone sediment is equipped with spiral deflector, axis of the deflector around eddy flow outlet
Line, and the outer profile of the deflector is shunk along direction ecto-entad from top to bottom, and the center of the deflector is equipped with upper
Lower perforation and the flow-guiding channel with the eddy flow outlet；
The top side wall of the cyclone sediment room is equipped with the eddy flow entrance towards the deflector.
21. sewage purifier according to claim 20, which is characterized in that the deflector be outer diameter from upper end under
Hold the cone spiral vane being gradually reduced.
22. sewage purifier according to claim 20, which is characterized in that the deflector extend along the vertical direction and
It is coiled in the horizontal plane along helix；Also, the depth that the deflector extends vertically downwards, gradually increases from outside to inside
Greatly.
23. sewage purifier according to claim 22, which is characterized in that including being set to leading above the deflector
Top plate is flowed, the deflector extends upwardly to the water conservancy diversion top plate along the vertical direction.
24. sewage purifier according to claim 22, which is characterized in that be provided in the plate face of the deflector more
A wave groove, multiple wave grooves are spaced apart along the vertical direction.
25. sewage purifier described in any one of -15 or 17-20 according to claim 1, which is characterized in that the sewage
Cleaning equipment includes the aqueous stream injectors being connected to the cyclone sediment room, and the aqueous stream injectors are used for sewage to be clean
It is sprayed into the cyclone sediment room.
26. sewage purifier according to claim 25, which is characterized in that the sewage purifier includes first row
Dirt pipe, first sewage pipe are located at the lower section of the Hydraulic Circulation clarifying chamber and are located at the lower section of the concentrating and precipitating room；
The bottom wall of the Hydraulic Circulation clarifying chamber is equipped with the first sewage draining exit being connected to first sewage pipe；
The bottom wall of the concentrating and precipitating room is equipped with the second sewage draining exit being connected to first sewage pipe.
27. sewage purifier according to claim 26, which is characterized in that first sewage pipe and the water flow are sprayed
The entrance of emitter is connected to.
28. sewage purifier according to claim 20, which is characterized in that the sewage purifier includes that flocculation is anti-
Room is answered, the flocculation reaction room is set to the flow-guiding channel, and the top opening of the flocculation reaction room and eddy flow outlet connect
It is logical, bottom wall of the bottom opening towards the cyclone sediment room.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910589290.0A CN110217914B (en) | 2019-07-02 | 2019-07-02 | Sewage purifying equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910589290.0A CN110217914B (en) | 2019-07-02 | 2019-07-02 | Sewage purifying equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN110217914A true CN110217914A (en) | 2019-09-10 |
| CN110217914B CN110217914B (en) | 2024-02-09 |
Family
ID=67815863
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910589290.0A Active CN110217914B (en) | 2019-07-02 | 2019-07-02 | Sewage purifying equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN110217914B (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111617520A (en) * | 2020-05-12 | 2020-09-04 | 尚铁军 | Turbulent flow sedimentation tank |
| CN111617521A (en) * | 2020-05-12 | 2020-09-04 | 尚铁军 | High-efficient sedimentation tank |
| CN111632409A (en) * | 2020-05-12 | 2020-09-08 | 尚铁军 | Venturi inner member for sedimentation tank |
| JP7055308B1 (en) * | 2021-05-14 | 2022-04-18 | Jms株式会社 | Dental treatment wastewater treatment system and its wastewater treatment method |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102010088A (en) * | 2010-12-23 | 2011-04-13 | 北京京诚科林环保科技有限公司 | Pressure-bearing integral metallurgy sewage purifying treatment device |
| JP2014042860A (en) * | 2012-08-24 | 2014-03-13 | Swing Corp | High-speed coagulation sedimentation equipment |
| CN108622997A (en) * | 2018-06-26 | 2018-10-09 | 秦皇岛德创节能环保科技有限公司 | Pressure-bearing type purifier |
| CN210796005U (en) * | 2019-07-02 | 2020-06-19 | 中冶京诚工程技术有限公司 | Sewage purification equipment |
-
2019
- 2019-07-02 CN CN201910589290.0A patent/CN110217914B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102010088A (en) * | 2010-12-23 | 2011-04-13 | 北京京诚科林环保科技有限公司 | Pressure-bearing integral metallurgy sewage purifying treatment device |
| JP2014042860A (en) * | 2012-08-24 | 2014-03-13 | Swing Corp | High-speed coagulation sedimentation equipment |
| CN108622997A (en) * | 2018-06-26 | 2018-10-09 | 秦皇岛德创节能环保科技有限公司 | Pressure-bearing type purifier |
| CN210796005U (en) * | 2019-07-02 | 2020-06-19 | 中冶京诚工程技术有限公司 | Sewage purification equipment |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111617520A (en) * | 2020-05-12 | 2020-09-04 | 尚铁军 | Turbulent flow sedimentation tank |
| CN111617521A (en) * | 2020-05-12 | 2020-09-04 | 尚铁军 | High-efficient sedimentation tank |
| CN111632409A (en) * | 2020-05-12 | 2020-09-08 | 尚铁军 | Venturi inner member for sedimentation tank |
| CN111617521B (en) * | 2020-05-12 | 2021-08-24 | 四川发展环境科学技术研究院有限公司 | High-efficient sedimentation tank |
| CN111617520B (en) * | 2020-05-12 | 2021-11-30 | 大连大禹水处理技术有限公司 | Turbulent flow sedimentation tank |
| CN111632409B (en) * | 2020-05-12 | 2022-11-08 | 中建三局绿色产业投资有限公司 | Venturi inner member for sedimentation tank |
| JP7055308B1 (en) * | 2021-05-14 | 2022-04-18 | Jms株式会社 | Dental treatment wastewater treatment system and its wastewater treatment method |
Also Published As
| Publication number | Publication date |
|---|---|
| CN110217914B (en) | 2024-02-09 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN110217914A (en) | Sewage purifier | |
| CN110217913A (en) | Eddy flow sewage purifier | |
| CN102010088B (en) | Pressure-bearing integral metallurgy sewage purifying treatment device | |
| CN211521700U (en) | Hydraulic circulation clarification tank | |
| CN203598540U (en) | Vertical flow sedimentation tank | |
| KR960004368B1 (en) | Apparatus for removing grit | |
| CA2609589C (en) | Gravitational separation device for water treatment | |
| CN105366757B (en) | A kind of circulation type adsorption tank and its adsorption method | |
| CN102225304B (en) | Twin exhaust gas purifying tower | |
| CN210796003U (en) | Rotational flow sewage purification equipment | |
| US5124049A (en) | Liquid purification methods | |
| JPS61501135A (en) | Clarification equipment for liquids containing solid substances | |
| CN109665606A (en) | A kind of sewage-treatment plant | |
| CN210698952U (en) | Silt whirl deposits device suitable for sewage purification handles | |
| CN209602177U (en) | A kind of effluent treatment plant | |
| CN206454320U (en) | The efficient clarifying reaction device of fine suspension in a kind of processing sewage | |
| CN108744614A (en) | A kind of vertical sedimentation basin of industrial organic waste water | |
| CN210796005U (en) | Sewage purification equipment | |
| CN206730595U (en) | High-efficient vertical flow sedimentation basin | |
| CN209367977U (en) | Water depth processing unit | |
| US5124034A (en) | Liquid purification systems | |
| RU104082U1 (en) | CENTRIFUGAL OIL AND GAS SEPARATOR | |
| CN207324181U (en) | The high-effect central tube mechanism of perpendicular stream precipitator tower | |
| CN205516881U (en) | Strengthen superposed layer spiral vertical flow settling pond | |
| CN206308168U (en) | Horizontal pressure-bearing type integrated water quality purifying treater |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |