CN206308168U - Horizontal pressure-bearing type integrated water quality purification treatment device - Google Patents
Horizontal pressure-bearing type integrated water quality purification treatment device Download PDFInfo
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- CN206308168U CN206308168U CN201621407721.5U CN201621407721U CN206308168U CN 206308168 U CN206308168 U CN 206308168U CN 201621407721 U CN201621407721 U CN 201621407721U CN 206308168 U CN206308168 U CN 206308168U
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 139
- 238000000746 purification Methods 0.000 title abstract description 6
- 238000009826 distribution Methods 0.000 claims abstract description 40
- 238000012545 processing Methods 0.000 claims abstract description 10
- 239000000945 filler Substances 0.000 claims abstract description 8
- 239000000463 material Substances 0.000 claims description 15
- 239000000706 filtrate Substances 0.000 claims description 14
- 238000005192 partition Methods 0.000 claims description 11
- 239000000126 substance Substances 0.000 claims description 10
- 239000000725 suspension Substances 0.000 claims description 10
- 239000007788 liquid Substances 0.000 claims description 7
- 230000000740 bleeding effect Effects 0.000 claims description 3
- 238000004891 communication Methods 0.000 claims description 3
- 239000008398 formation water Substances 0.000 claims 1
- 230000000694 effects Effects 0.000 abstract description 18
- 238000001914 filtration Methods 0.000 abstract description 18
- 239000010802 sludge Substances 0.000 abstract description 8
- 238000000034 method Methods 0.000 description 13
- 238000001556 precipitation Methods 0.000 description 10
- 230000008569 process Effects 0.000 description 8
- 239000013049 sediment Substances 0.000 description 8
- 238000005345 coagulation Methods 0.000 description 7
- 230000015271 coagulation Effects 0.000 description 7
- 229910000831 Steel Inorganic materials 0.000 description 6
- 230000008901 benefit Effects 0.000 description 6
- 239000010959 steel Substances 0.000 description 6
- 238000005352 clarification Methods 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 5
- 230000001112 coagulating effect Effects 0.000 description 4
- 238000010992 reflux Methods 0.000 description 4
- 238000004062 sedimentation Methods 0.000 description 4
- 239000002131 composite material Substances 0.000 description 3
- 238000005189 flocculation Methods 0.000 description 3
- 230000016615 flocculation Effects 0.000 description 3
- 238000005086 pumping Methods 0.000 description 3
- 230000006641 stabilisation Effects 0.000 description 3
- 238000011105 stabilization Methods 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000003814 drug Substances 0.000 description 2
- 238000004134 energy conservation Methods 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 2
- 238000010907 mechanical stirring Methods 0.000 description 2
- 238000012544 monitoring process Methods 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- 229920002472 Starch Polymers 0.000 description 1
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- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
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- 238000001514 detection method Methods 0.000 description 1
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Abstract
The utility model provides a horizontal pressure-bearing type integrated water purification treatment device, which comprises a horizontal closed pressure-bearing shell, wherein a settling chamber, a clarifying chamber and a filter chamber are sequentially arranged in the horizontal closed pressure-bearing shell along the axis direction, the bottoms of the settling chamber and the clarifying chamber are respectively provided with a sludge discharge pipe communicated with the outside, the lower part of the clarifying chamber is communicated with a clarifying area at the upper part of the settling chamber through a vertical water distribution groove, the middle part of the clarifying chamber is provided with a filler inclined pipe with two open ends, and the top surface of the clarifying chamber is provided with a primary water outlet pipe communicated with the outside; the horizontal water distribution tank arranged at the upper part of the filtering chamber is communicated with the primary water outlet pipe through a connecting pipe, a filtering layer combined component is arranged below the horizontal water distribution tank, and a secondary water outlet pipe communicated with the outside is arranged in the filtering layer combined component. The utility model provides a quality of water purification unit can guarantee that stable purifying effect, water resistance impact performance are strong, and difficult jam goes out water and need not the pressurization moreover and can deliver to follow-up processing facility.
Description
Technical field
The utility model is related to purifier technical field, at more particularly to a kind of horizontal pressure-bearing type integrated purification of water quality
Reason device.
Background technology
In municipal administration, industrial discharge water treatment system, conventional coagulation, precipitate, filter each treatment facility and be generally independence
, open treatment facility, its long flow path, floor space are big, civilwork engineering quantity is big, the construction period is long, suitable big-and-middle-sized water quality
Purified treatment engineering.But for small-sized water quality purified treatment engineering, using the multi-functional collection in one such as coagulation, precipitation, filtering
Forming apparatus have absolute predominance, the advantage is that small compact arrangement of equipment, floor space, short time limit, automatic control level are high, positive because such as
This, multifunctional all, integrated form purifier arise at the historic moment, and make a general survey of this class existing equipment, generally existing problems with:
1st, coagulation, precipitation, filtering middle part turnout science and engineering skill are simply integrated with, fail to be made for each facility functional characteristics
System optimization is combined;
2nd, the design feature of Highgrade integration causes that the functions such as coagulation, precipitation, filtering are influenceed by certain each other, because
And the impact resistance of equipment dies down, cause producing water water quality unstable;
3rd, fail the solid particle polluter of different-grain diameter scope in classification removal turbid circulating water, easily cause equipment regional area
Blocking;
4th, part integrated equipment is intolerant to pressure, it is impossible to make full use of the overbottom pressure head of one-level booster station, device to produce water and still need to
Enter subsequent treatment facility through two-stage pressurizing, cause unnecessary power consumption.
Utility model content
The purpose of this utility model is to provide a kind of horizontal pressure-bearing type integrated purification of water quality that can overcome drawbacks described above
Processing unit, and the horizontal pressure-bearing type integrated water quality purifying treater has, and height is low, overhaul convenient, can be arranged at underground
The advantages of in space.
To reach above-mentioned purpose, the utility model provides a kind of horizontal pressure-bearing type integrated water quality purifying treater,
It includes Horizontal closed formula pressure-bearing shell, is sequentially provided with along its axis direction in the Horizontal closed formula pressure-bearing shell:Precipitation
Room, is provided with back taper dividing plate in the middle part of the mud chamber, the mud chamber is separated to form into top by the back taper dividing plate
Settling section and bottom eddy flow Chu Chen areas, the settling section and the eddy flow Chu Chen areas are by being arranged at the back taper dividing plate
The nozzle of bottom is connected, and the side surface upper part in the eddy flow Chu Chen areas is sunk at the beginning of being provided with the water inlet pipe with ft connection, the eddy flow
The bottom surface in area is provided with the one-level discharge pipeline with ft connection, and the bottom surface of the settling section is provided with two grades of spoil disposals with ft connection
Pipe;Clarifying chamber, the bottom of the clarifying chamber is connected by vertical distribution channel with the settling section, and the bottom surface of the clarifying chamber sets
There is back taper spoil disposal guiding gutter, the bottom of the back taper spoil disposal guiding gutter is provided with the three-level discharge pipeline with ft connection, described
The filler inclined tube of both ends open is provided with the middle part of clarifying chamber, the top surface of the clarifying chamber is provided with the primary effluent with ft connection
Pipe;Filter chamber, the top of the filter chamber is provided with horizontal distribution channel, and the horizontal distribution channel is gone out by connecting tube with the one-level
Water pipe is connected, and filter layer combiner is provided with below the horizontal distribution channel, be provided with the filter layer combiner with
The secondary effluent pipe of ft connection.
Horizontal pressure-bearing type integrated water quality purifying treater as described above, wherein, contraposition is provided with the settling section
The bell shape deflector and infundibulate deflector of setting, the week of the periphery of the bell shape deflector and the infundibulate deflector
Side is connected by multiple spaced support members, and the lower end of multiple support members is connected to the upper table of the back taper dividing plate
Flow-guiding channel is formed between face, and the infundibulate deflector and the back taper dividing plate, the flow-guiding channel is vertical with described
Distribution channel is connected, and suspension has a trunnion from top to bottom in necking down shape in the bell shape deflector, and the trunnion upper end
Having and the inner surface of the bell shape deflector between allows the runner of liquid communication, and the leakage is run through in the lower end of the trunnion
Bucket shape deflector simultaneously extends to the outside of the nozzle, and have annular space, institute between the trunnion and the infundibulate deflector
Stating has backflow gap between trunnion and the nozzle, the annular space, the backflow gap and the flow-guiding channel are mutually interconnected
It is logical.
Horizontal pressure-bearing type integrated water quality purifying treater as described above, wherein, chemical feed pipe is provided with the nozzle,
The chemical feed pipe extends to the outside of the Horizontal closed formula pressure-bearing shell.
Horizontal pressure-bearing type integrated water quality purifying treater as described above, wherein, the bottom surface of the back taper dividing plate
The cylindrical shape guide shell of open bottom end is connected with, the lower end of the nozzle is located in the cylindrical shape guide shell.
Horizontal pressure-bearing type integrated water quality purifying treater as described above, wherein, the bottom of the cylindrical shape guide shell
Portion is provided with filter screen, and multiple vortex balls are provided with the cylindrical shape guide shell.
Horizontal pressure-bearing type integrated water quality purifying treater as described above, wherein, connected on the primary effluent pipe
There are check-valves and transmissometer, be connected with backwash outlet pipe in the connecting tube, it is the backwash outlet pipe, the connecting tube, described
Horizontal distribution channel and the secondary effluent pipe are sequentially communicated to form backwash path.
Horizontal pressure-bearing type integrated water quality purifying treater as described above, wherein, it is provided with the top of the connecting tube
Air bleeding valve.
Horizontal pressure-bearing type integrated water quality purifying treater as described above, wherein, the filter layer combiner bag
Filtrate supporting plate and the multimedium filter material layer being arranged in the filtrate supporting plate are included, the filtrate supporting plate is located at the filtering
The bottom of room, the secondary effluent pipe is located at the bottom of the multimedium filter material layer, and the secondary effluent pipe is provided with water outlet receipts
Acquisition means, the effluent collection device is connected with the multimedium filter material layer.
Horizontal pressure-bearing type integrated water quality purifying treater as described above, wherein, the effluent collection device includes
The many radial directions along the secondary effluent pipe side by side and spaced screen pipe, one end of each screen pipe with described two grades
Outlet pipe is connected, the other end closing of each screen pipe, and each screen pipe is provided with multiple spaced for intaking
Filter cap.
Horizontal pressure-bearing type integrated water quality purifying treater as described above, wherein, the mud chamber, the clarifying chamber
With the filter chamber by along the Horizontal closed formula pressure-bearing shell is radial parallel and spaced first dividing plate and second partition
It is separated;The 3rd dividing plate being be arranged in parallel with first dividing plate, described are provided with the Horizontal closed formula pressure-bearing shell
Three dividing plates are located between first dividing plate and the second partition, first dividing plate, the 3rd dividing plate and horizontal envelope
The side wall of enclosed pressure-bearing shell encloses to form the vertical distribution channel, and the top of first dividing plate is provided with breach and forms described
The inlet of vertical distribution channel, the bottom of the 3rd dividing plate is provided with the liquid outlet that lower breach forms the vertical distribution channel.
Compared with prior art, advantage of the present utility model is as follows:
The utility model provide horizontal pressure-bearing type integrated water quality purifying treater, with precipitation, coagulation, clarification,
Filtering staggeredly processes composite technology, and turbid circulating water is utilized through cyclone sediment, flocculation sediment, hydraulic sludge backflow successively, tube settling
With multi-medium filtering PROCESS FOR TREATMENT, the clean-up effect of stabilization, and the horizontal pressure-bearing type integrated purification of water quality treatment are ensure that
Device, resistance to waterpower impact property is strong, structure is relatively easy, be not easily blocked, safeguard and operational control is simple and convenient, and whole process closing is held
Pressure so that the pressure loss of the turbid circulating water discharged via primary effluent pipe, backwash outlet pipe or secondary effluent pipe is smaller, Neng Gouyou
Effect utilizes overbottom pressure head so that water outlet can deliver to subsequent treatment facility without two-stage pressurizing pumping plant, so as to simplify operation, section
About use cost;Additionally, compared with existing this kind equipment, tube settling is set into independent a processing region, Neng Gougen
The area of tube settling is determined according to water quality situation, so as to reach optimal sedimentation effect;
The horizontal pressure-bearing type integrated water quality purifying treater that the utility model is provided, takes full advantage of nozzle in trunnion
The negative pressure that lower end produces carries out sludge reflux treatment, without mechanical stirring equipment, has saved power input, is conducive to energy-conservation to drop
Consumption;
The horizontal pressure-bearing type integrated water quality purifying treater that the utility model is provided, using filter chamber as last water quality
Processing unit, using the transmissometer monitoring water treatment data being connected on primary effluent pipe, comes at any time according to water quality situation
Regulate whether for turbid circulating water to be passed through filter chamber, to improve the treatment effeciency of horizontal pressure-bearing type integrated water quality purifying treater.
Brief description of the drawings
The following drawings is only intended to, in the utility model is done schematic illustration and explanation, not limit model of the present utility model
Enclose.Wherein:
Fig. 1 is the knot of the horizontal pressure-bearing type integrated water quality purifying treater provided according to the embodiment of the utility model one
Structure schematic diagram;
Fig. 2 is the side structure schematic view of the horizontal pressure-bearing type integrated water quality purifying treater shown in Fig. 1;
Fig. 3 be in Fig. 1 along cross section structure diagram from A-A to section.
Drawing reference numeral explanation:
1- Horizontal closed formula pressure-bearing shells;The dividing plates of 11- first;The upper breach of 111-;12- second partitions;The dividing plates of 13- the 3rd;
Breach under 131-;2- mud chambers;21- back taper dividing plates;22- eddy flow Chu Chen areas;221- water inlet pipes;222- one-level discharge pipelines;23-
Settling section;Bis- grades of discharge pipelines of 231-;232- bell shape deflectors;233- infundibulate deflectors;234- support members;235- water conservancy diversion leads to
Road;236- trunnions;24- nozzles;25- chemical feed pipes;26- cylindrical shape guide shells;27- is vortexed ball;3- clarifying chambers;The vertical water distributions of 31-
Groove;32- back taper spoil disposal guiding gutters;33- three-level discharge pipelines;34- filler inclined tubes;35- primary effluent pipes;36- check-valves;37-
Transmissometer;4- filter chambers;The horizontal distribution channels of 41-;42- filter layer combiners;421- filtrate supporting plates;422- multimedium filtrates
Layer;43- secondary effluent pipes;44- effluent collection devices;441- screen pipes;442- filter caps;5- connecting tubes;6- backwash outlet pipes;
7- air bleeding valves.
Specific embodiment
In order to have clearer understanding to the technical solution of the utility model, purpose and effect, in conjunction with brief description of the drawings originally
The specific embodiment of utility model.
In Fig. 1, the direction of arrow is turbid circulating water flow direction.
As shown in figure 1, the horizontal pressure-bearing type integrated water quality purifying treater that the utility model is provided, it includes horizontal
Closed pressure-bearing shell 1, mud chamber 2, the and of clarifying chamber 3 are sequentially provided with Horizontal closed formula pressure-bearing shell 1 along its axis direction
Filter chamber 4, wherein, the middle part of mud chamber 2 is provided with back taper dividing plate 21, is separated to form mud chamber 2 by back taper dividing plate 21
The settling section 23 on top and the eddy flow Chu Chen areas 22 of bottom, the bottom of back taper dividing plate 21 are provided with nozzle 24, settling section 23 and rotation
Liu Chuchen areas 22 are connected by nozzle 24, and the inlet of nozzle 24 is located in eddy flow Chu Chen areas 22, the liquid outlet position of nozzle 24
In in settling section 23, the side surface upper part in eddy flow Chu Chen areas 22 is provided with the water inlet pipe 221 with ft connection, and water inlet pipe 221 is along cutting
Line enters heavy interior at the beginning of eddy flow, and the bottom surface in eddy flow Chu Chen areas 22 is provided with the one-level discharge pipeline 222 with ft connection, by water inlet pipe
221 prolong tangential direction into the turbid circulating water in eddy flow Chu Chen areas 22, and eddy flow is formed under the guide effect of back taper dividing plate 21, by
In subject to centrifugal forces, the suspension of the larger granularity in part is got rid of to the side wall in eddy flow Chu Chen areas 22 in turbid circulating water, and
Slide under gravity to the bottom surface in eddy flow Chu Chen areas 22, when a certain amount of mud is gathered in the bottom surface in eddy flow Chu Chen areas 22
When, the one-level discharge pipeline 222 set by bottom surface is discharged, in order that mud is more smoothly discharged, at the bottom in eddy flow Chu Chen areas 22
The face method of heap building concrete, makes the bottom surface in eddy flow Chu Chen areas 22 form funnel-form beneficial to deslagging, and by one-level discharge pipeline
222 import is arranged on the bottom of funnel, and so, mud can be in the guide functions of the bottom surface in funnelform eddy flow Chu Chen areas 22
Lower smoothly to be discharged into one-level discharge pipeline 222, removing the turbid circulating water after the suspension of larger granularity can enter clear by nozzle 24
Clear area 23 is clarified, and is discharged for the ease of sediment in settling section 23, and the bottom surface in settling section 23 is provided with and ft connection
Two grades of discharge pipelines 231, two grades of discharge pipelines 231 extend to the outside of Horizontal closed formula pressure-bearing shell 1 through eddy flow Chu Chen areas 22, clear
Sediment can periodically be discharged via two grades of discharge pipelines 231 in clear area 23;
The bottom of clarifying chamber 3 is connected by vertical distribution channel 31 with settling section 23, the turbid ring after being processed via mud chamber 2
Water enters the bottom of clarifying chamber 3 by vertical distribution channel 31, and the bottom surface of clarifying chamber 3 is provided with back taper mud diversion trench 32, back taper
The bottom of shape spoil disposal guiding gutter 32 is provided with the three-level discharge pipeline 33 with ft connection, and the sediment in clarifying chamber 3 is in back taper mud
Starch under the guide effect of guiding gutter 32, three-level discharge pipeline 33 can be passed through and discharged, the middle part of clarifying chamber 3 is provided with both ends open
Filler inclined tube 34, the bottom of inclined tube 34 supported by the steelframe that channel-section steel and round steel are constituted, and inclined tube 34 is arranged in clarifying chamber 3
Portion, the turbid circulating water of the bottom of clarifying chamber 3 reaches the effect of water quality clarification even into inclined tube 34, and in the presence of inclined tube 34, and
The part mud can be slided and be finally collected to back taper spoil disposal guiding gutter 32 by inclined tube 34 is interior, and in back taper spoil disposal water conservancy diversion
Under the guide effect of groove 32, periodically discharged from three-level discharge pipeline 33, the top surface of clarifying chamber 3 is provided with the primary effluent with ft connection
Pipe 35, if clarity meets requirement after the clarified room treatment of turbid circulating water with pressure, can be discharged by primary effluent pipe 35, directly be entered
Enter subsequent treatment facility, it is turbid after clarified room treatment if water quality is unsatisfactory for requiring after the clarified room treatment of turbid circulating water with pressure
Ring water, passes sequentially through primary effluent pipe 35, the inflow of connecting tube 5 and is arranged in the horizontal distribution channel 41 on the top of filter chamber 4;
The lower section of horizontal distribution channel 41 is provided with filter layer combiner 42, and turbid circulating water is uniformly entered by horizontal distribution channel 41
Enter in filter layer combiner 42, the secondary effluent pipe 43 with ft connection, turbid circulating water warp are provided with filter layer combiner 42
Discharged by secondary effluent pipe 43 after being filtered by filter layer combiner 42, and directly enter people's subsequent treatment facility without pressurization.
It should be noted that the pressure value into the turbid circulating water of water inlet pipe 221 is greater than 0.15MPa.
The horizontal pressure-bearing type integrated water quality purifying treater that the utility model is provided, with precipitation, clarification, fine mistake
The treatment composite technology such as filter, turbid circulating water is processed through cyclone sediment, clarification, tube settling and multi-medium filtering, ensure that successively
The clean-up effect of stabilization, and the horizontal pressure-bearing type integrated water quality purifying treater, resistance to waterpower impact property is strong, structure is relative
Simply, it is not easily blocked, safeguards and operational control is simple and convenient, whole process closing pressure-bearing, and overbottom pressure head can be effectively utilized, go out
Water can deliver to subsequent treatment facility without two-stage pressurizing pumping plant, so as to simplify operation, save use cost;Additionally, with
Existing this kind equipment is compared, and tube settling is set into an independent processing region, can determine that inclined tube sinks according to water quality situation
The area in shallow lake, so as to reach optimal sedimentation effect.
Further, bell shape deflector 232 and infundibulate deflector 233 that contraposition is set, bell jar are provided with settling section 23
The periphery of shape deflector 232 is connected with the periphery of infundibulate deflector 233 by multiple spaced support members 234, support
Part 234 is angle steel, and the periphery of bell shape deflector 232 is connected to the top of multiple support members 234, infundibulate deflector 233
Periphery is connected to the middle part of multiple support members 234, and infundibulate deflector 233 be arranged in parallel with back taper dividing plate 21, Duo Gezhi
The bottom of support member 234 is connected to the upper surface of back taper dividing plate 21, and makes between infundibulate deflector 233 and back taper dividing plate 21
Flow-guiding channel 235 is formed, flow-guiding channel 235 is connected by the space on the top of bell shape deflector 232 with vertical distribution channel 31,
Hanged by channel-section steel in bell shape deflector 232 and connect one from top to bottom in the trunnion 236 of necking down shape, and trunnion 236 upper end and clock
Be separated the runner for being formed and allowing liquid communication between the inner surface of cover shape deflector 232, and turbid circulating water with pressure is by the upper end of trunnion 236
During ejection, play a part of to expand stream by trunnion 236, the lower end of trunnion 236 runs through infundibulate deflector 233 and extends to nozzle
There is annular space, between there is backflow between trunnion 236 and nozzle 24 between 24 outside, and trunnion 236 and infundibulate deflector 233
Gap, annular space, backflow gap and flow-guiding channel 235 are interconnected, and the turbid circulating water sprayed via nozzle 24 passes through trunnion 236,
Under the guide effect of bell shape deflector 232, it is flow in vertical distribution channel 31 via flow-guiding channel 235, it is straight due to nozzle 24
Footpath is less than the diameter of the lower end of trunnion 236, so that nozzle 24 produces negative pressure in the lower end of trunnion 236, inside flow-guiding channel 235
Dividing mud to be flow in the presence of negative pressure carries out sludge reflux utilization at backflow gap, the processing procedure sets without mechanical agitation
It is standby, be effectively saved power input so that horizontal pressure-bearing type integrated water quality purifying treater have it is energy-saving
Advantage, remaining mud is periodically discharged via two grades of discharge pipelines 231.
Further, as depicted in figs. 1 and 2, chemical feed pipe 25 is provided with nozzle 24, chemical feed pipe 25 extends to the outside of housing,
Can be to flocculant be added in clarifying chamber, so that the small suspension that precipitation is difficult in turbid circulating water is condensed into and is easy to by chemical feed pipe 25
The big floccule of precipitation, so as to reach optimal sedimentation effect, and is located at trunnion 236 effect for producing negative pressure in nozzle 24
Under, carry out sludge reflux so that turbid circulating water obtains sufficient coagulation stirring.
Further, as shown in figure 1, the bottom surface of back taper dividing plate 21 is connected with the cylindrical shape guide shell 26 of open bottom end, circle
The top of tubular guide shell 26 is welded on the bottom surface of back taper dividing plate 21, and the lower end of nozzle 24 is located in cylindrical shape guide shell 26,
Cylindrical shape guide shell 26 forms coagulating room in eddy flow Chu Chen areas 22, adds the turbid circulating water of coagulated agent to be led via cylindrical shape
The bottom of flow cartridge 26 enters cylindrical shape guide shell 26, is sufficiently mixed, and settling section 23, the mud after sedimentation are entered by nozzle 24
Slurry can be discharged periodically via two grades of discharge pipelines 231 of the bottom surface of back taper dividing plate 21.
Further, the bottom of cylindrical shape guide shell 26 is provided with filter screen, cylindrical shape guide shell 26 and is provided with multiple vortex balls
27, multiple vortex ball 27 is hollow sphere structure, and its surface is provided with circular hole, when turbid circulating water passes through circular hole, because of the work of spheroid
With making turbid circulating water sufficiently be mixed with medicament, therefore enhance flocculation reaction effect.
In a kind of implementation method of the present utility model, as shown in figure 1, being connected with the He of check-valves 36 on primary effluent pipe 35
Transmissometer 37, the water quality of the turbid circulating water with pressure after the real-time detection of transmissometer 37 is processed via mud chamber 2 and clarifying chamber 3, with
Judge whether turbid circulating water needs to carry out filtration treatment into filter chamber 4, so, turbid circulating water water quality after treatment meets requirement
When, so that it may after only being processed by mud chamber 2 and clarifying chamber 3, and successively via primary effluent pipe 35, connecting tube 5 and backwash outlet pipe 6
Discharge outside horizontal pressure-bearing integrated water purifying processing unit, subsequent treatment facility can be entered without pressurization;
Backwash outlet pipe 6, connecting tube 5, horizontal distribution channel 41 and secondary effluent pipe 43 are sequentially communicated to form backwash path, when
After filter layer combiner 42 is filtered through certain hour, a certain amount of suspension can be intercepted thereon, so that under its filter capacity
Drop, now needs to close the water inlet pipe 221 of the present apparatus, and backwash water enters filter chamber 4 by secondary effluent pipe 43, and backwash water is by filtering
Outside layer combiner 42, horizontal distribution channel 41, connecting tube 5, backwash outlet pipe 6, the discharge present apparatus, due on primary effluent pipe 35
Equipped with check-valves 36, therefore backwash water will not flow back to clarifying chamber 3.
In a kind of implementation method of the present utility model, as shown in figures 1 and 3, filter layer combiner 42 includes filtrate
Supporting plate 421 and the multimedium filter material layer 422 being arranged in filtrate supporting plate 421, filtrate supporting plate 421 are located at filter chamber 4
Bottom, secondary effluent pipe 43 is located at the bottom of multimedium filter material layer 422, and secondary effluent pipe 43 is supported by channel steel support in filtrate
The top of plate 421 so that there is certain distance to form ponding space between secondary effluent pipe 43 and filtrate supporting plate 421, so as to
Smoothly enter in secondary effluent pipe 43 in the turbid circulating water after filtering, in order to further increase the inflow of secondary effluent pipe 43,
Secondary effluent pipe 43 is provided with effluent collection device 44, and effluent collection device 44 is placed in multimedium filter material layer 422, after filtering
Turbid circulating water is entered in secondary effluent pipe 43 by effluent collection device 44, and is held via the discharge of secondary effluent pipe 43 Horizontal closed formula
Pressure shell body 1 is directly entered subsequent treatment facility.
Further, as shown in figure 3, effluent collection device 44 includes many radial directions along secondary effluent pipe 43 side by side and interval
The screen pipe 441 of setting, one end of each screen pipe 441 is provided with the filtering pipe flange being connected with secondary effluent pipe 43, each screen pipe
441 other end closing, secondary effluent pipe 43 be radially provided with it is multiple side by side and be interval with adpting flange, by bolt by one
Adpting flange connects with a filtering pipe flange, and one end of screen pipe 441 connects with secondary effluent pipe 43, and each screen pipe is provided with many
The individual spaced filter cap 442 for intaking, the quantity of filter cap 442 can be set according to actual needs, by many Jie
Turbid circulating water after the filtering of matter filter layer, by the entrance screen pipe 441 of filter cap 442, after converging to secondary effluent pipe 43, passing through
Horizontal closed formula pressure-bearing shell 1 is discharged by secondary effluent pipe 43 and is directly entered subsequent treatment facility.
In a kind of implementation method of the present utility model, as shown in figure 1, mud chamber 2, clarifying chamber 3 and filter chamber 4 are by along sleeping
The closed pressure-bearing shell 1 of formula is radial parallel and spaced first dividing plate 11 and second partition 12 are separated, Horizontal closed
The radial section of formula pressure-bearing shell 1 is rounded, and the first dividing plate 11 and second partition 12 are circular bulkheads, support filler inclined tube 34
The two ends of channel-section steel welded with the first dividing plate 11 and second partition 12 respectively, one end and the second partition 12 of horizontal distribution channel 41 are welded
Connect, one end and the second partition 12 of filtrate supporting plate are welded, the sidewall weld of other part and Horizontal closed formula pressure-bearing shell 1;
The 3rd dividing plate 13 being be arranged in parallel with the first dividing plate 11, the 3rd dividing plate 13 are provided with Horizontal closed formula pressure-bearing shell 1
Also it is circular bulkheads.3rd dividing plate 13 is located between the first dividing plate 11 and second partition 12, and the 3rd dividing plate 13 adjacent to first every
Plate 11 is set, and the side wall of the first dividing plate 11, the 3rd dividing plate 13 and Horizontal closed formula pressure-bearing shell 1 encloses to form vertical distribution channel
31, the top of the first dividing plate 11 is provided with the inlet that breach 111 forms vertical distribution channel 31, and the bottom of the 3rd dividing plate 13 is provided with
Lower breach 131 forms liquid outlet, specifically, cutting next bow-shaped structural on the top of the first dividing plate 11 forms breach 111,
And the both sides of breach 111 is connected with the 3rd dividing plate 13 by upper junction plate respectively, ensure upper breach by two upper junction plates
111 will not fit with the 3rd dividing plate 13, and cutting next bow-shaped structural in the bottom of the 3rd dividing plate 13 forms lower breach 131, makes
The both sides of lower breach 131 are connected by lower connecting plate with the first dividing plate 11 respectively, and lower breach 131 is ensured not by two lower connecting plates
Can be fitted with the first dividing plate 11, ensure that turbid circulating water can enter clarifying chamber 3 through by vertical distribution channel 31.
The horizontal pressure-bearing type integrated water quality purifying treater of the utility model offer is provided below in conjunction with the accompanying drawings
Concrete technology flow process:
As shown in figure 1, need to process and add the sewage of coagulant medicament to prolong tangent line into mud chamber 2 by water inlet pipe 221
Eddy flow Chu Chen areas 22 in, wherein, the pressure value from water inlet pipe 221 into the sewage of device is greater than 0.15MPa, in back taper
Eddy flow is formed under the guide functions of dividing plate 21, because suffered centrifugal force is different, the suspension quilt of the larger granularity in part in turbid circulating water
Get rid of to the side wall in eddy flow Chu Chen areas 22, and slide under gravity to the bottom surface in eddy flow Chu Chen areas 22, these suspensions
Mud is periodically discharged through one-level discharge pipeline 222, and the turbid circulating water of the suspension of the removal larger granularity in part is acted on by rotational flow settlement
Into being arranged in the cylindrical shape guide shell 26 of the bottom of back taper dividing plate 21, coagulating is carried out in cylindrical shape guide shell 26,
In order that coagulating is more abundant, multiple vortex balls 27 are provided with cylindrical shape guide shell 26, strengthen mixed by being vortexed ball 27
Solidifying reaction effect, settling section 23 is entered by the turbid circulating water after coagulating by nozzle 24, due to being provided with and outside in nozzle 24
The chemical feed pipe 25 of connection, nozzle is passed through by chemical feed pipe 25 to flocculant, turbid circulating water is added in nozzle 24 together with flocculant
24 carry out clarifying treatment into settling section 23, are reacted at the backflow gap that turbid circulating water can be between trunnion 236 and nozzle 24,
Big floccule body, reacted turbid circulating water is produced to pass through trunnion 236, and under the guide functions of bell shape deflector 232, via
Flow-guiding channel 235 is flow in vertical distribution channel 31, and is produced a floccule body part to be located at the lower end of trunnion 236 in nozzle 24 and produced
Reacted again by being back at backflow gap under raw suction function, another part is periodically via two grades of discharge pipelines 231
Discharge;
The turbid circulating water of clarifying chamber 3 is flow to by vertical distribution channel 31 uniformly to enter in the presence of back taper spoil disposal guiding gutter 32
Enter in filler inclined tube 34, via being discharged into primary effluent pipe 35 after the clarifying treatment of filler inclined tube 34, the sludge of precipitation is then regular
Discharged by three-level discharge pipeline 33, the transmissometer into the turbid circulating water in primary effluent pipe 35 through being connected on primary effluent pipe 35
37 detections, if its testing result meets the requirements, turbid circulating water is directly via primary effluent pipe 35, connecting tube 5 and backwash outlet pipe 6
Discharge, if its testing result is undesirable, turbid circulating water is entered in the horizontal distribution channel 41 of filter chamber 4 by connecting tube 5;
Turbid circulating water is uniformly flowed into multimedium filter material layer 422 by horizontal distribution channel 41, via the mistake of multimedium filter material layer 422
After filter treatment, entered in screen pipe 441 by filter cap 442, discharged finally by secondary effluent pipe 43.
Multimedium filter material layer 422, after being filtered through certain hour, can intercept a certain amount of suspension above filter material layer, make filter
Bed of material filter capacity declines, and now needs to close the water inlet pipe 221 of the present apparatus, and backwash water enters filter chamber 4 by secondary effluent pipe 43,
And by effluent collection device 44, multimedium filter material layer 422, horizontal distribution channel 41, connecting tube 5, backwash outlet pipe 6, discharge originally
Outside device.Because being equipped with check-valves 36 on primary effluent pipe 35, therefore backwash water will not flow back to clarifying chamber 3.
In sum, the horizontal pressure-bearing type integrated water quality purifying treater that the utility model is provided is heavy with multistage
Shallow lake, the clarification of one-level coagulation, one-level, single filter interlock treatment composite technology, turbid circulating water successively through cyclone sediment, flocculation sediment,
Hydraulic sludge backflow utilization, tube settling and multi-medium filtering PROCESS FOR TREATMENT, ensure that the clean-up effect of stabilization, and this is horizontal
Pressure-bearing type integrated water quality purifying treater, resistance to waterpower impact property is strong, structure is relatively easy, be not easily blocked, safeguard and grasp
Make control simple and convenient, whole process closing pressure-bearing so that discharged via primary effluent pipe or secondary effluent pipe or backwash outlet pipe
Turbid circulating water the pressure loss it is smaller, can effectively utilize overbottom pressure head so that producing water can deliver to without two-stage pressurizing pumping plant
Subsequent treatment facility, so as to simplify operation, has saved use cost;Additionally, compared with existing this kind equipment, inclined tube is sunk
Shallow lake is set to an independent processing region, the area of tube settling can be determined according to water quality situation, so as to reach optimal precipitation
Effect;
The horizontal pressure-bearing type integrated water quality purifying treater that the utility model is provided, takes full advantage of nozzle in trunnion
The negative pressure that lower end produces carries out sludge reflux utilization, without mechanical stirring equipment, has saved power input, is conducive to energy-conservation to drop
Consumption;
The horizontal pressure-bearing type integrated water quality purifying treater that the utility model is provided, using filter chamber as last water quality
Processing unit, using the transmissometer monitoring water treatment data being connected on primary effluent pipe, comes at any time according to water quality situation
Regulate whether for turbid circulating water to be passed through filter chamber, to improve the treatment effeciency of horizontal pressure-bearing type integrated water quality purifying treater.
The schematical specific embodiment of the utility model is the foregoing is only, model of the present utility model is not limited to
Enclose.Any those skilled in the art, the equivalent variations made on the premise of design of the present utility model and principle is not departed from
With modification, the scope of the utility model protection all should be belonged to.And it should be noted that each part of the present utility model simultaneously
It is not limited only to above-mentioned overall applicability, each technical characteristic described in specification of the present utility model can be selected according to actual needs
One individually uses or selects multinomial combining to use, therefore, the utility model is covered in the nature of things to be invented with this case
Other relevant combinations of point and concrete application.
Claims (10)
1. a kind of horizontal pressure-bearing type integrated water quality purifying treater, it is characterised in that the horizontal pressure-bearing type integrated water
Matter purifying processing device include Horizontal closed formula pressure-bearing shell, in the Horizontal closed formula pressure-bearing shell along its axis direction according to
It is secondary to be provided with:
Mud chamber, is provided with back taper dividing plate in the middle part of the mud chamber, separated the mud chamber by the back taper dividing plate
Form the settling section on top and the eddy flow Chu Chen areas of bottom, the settling section and the eddy flow Chu Chen areas by be arranged at it is described fall
The nozzle of conical baffle bottom is connected, and the side surface upper part in the eddy flow Chu Chen areas is provided with the water inlet pipe with ft connection, described
The bottom surface in eddy flow Chu Chen areas is provided with the one-level discharge pipeline with ft connection, and the bottom surface of the settling section is provided with ft connection two
Level discharge pipeline;
Clarifying chamber, the bottom of the clarifying chamber is connected by vertical distribution channel with the settling section, the bottom surface of the clarifying chamber
Back taper spoil disposal guiding gutter is provided with, the bottom of the back taper spoil disposal guiding gutter is provided with the three-level discharge pipeline with ft connection, institute
The filler inclined tube that both ends open is provided with the middle part of clarifying chamber is stated, the top surface of the clarifying chamber is provided with the primary effluent with ft connection
Pipe;
Filter chamber, the top of the filter chamber is provided with horizontal distribution channel, and the horizontal distribution channel passes through connecting tube and the one-level
Outlet pipe is connected, and filter layer combiner is provided with below the horizontal distribution channel, is provided with the filter layer combiner
With the secondary effluent pipe of ft connection.
2. horizontal pressure-bearing type integrated water quality purifying treater according to claim 1, it is characterised in that
Bell shape deflector and infundibulate deflector that contraposition is set, the week of the bell shape deflector are provided with the settling section
While being connected by multiple spaced support members with the periphery of the infundibulate deflector, the lower end of multiple support members connects
Formation water conservancy diversion between the upper surface of the back taper dividing plate, and the infundibulate deflector and the back taper dividing plate is connected to lead to
Road, the flow-guiding channel is connected with the vertical distribution channel, and it be in from top to bottom necking down there to be suspension in the bell shape deflector
Having between the trunnion of shape, and the inner surface of the upper end of the trunnion and the bell shape deflector allows the stream of liquid communication
Road, the lower end of the trunnion is through the infundibulate deflector and extends to the outside of the nozzle, and the trunnion with it is described
There is annular space between infundibulate deflector, there is backflow gap, the annular space, the backflow between the trunnion and the nozzle
Gap and the flow-guiding channel are interconnected.
3. horizontal pressure-bearing type integrated water quality purifying treater according to claim 2, it is characterised in that
Chemical feed pipe is provided with the nozzle, the chemical feed pipe extends to the outside of the Horizontal closed formula pressure-bearing shell.
4. horizontal pressure-bearing type integrated water quality purifying treater according to claim 1, it is characterised in that
The bottom surface of the back taper dividing plate is connected with the cylindrical shape guide shell of open bottom end, and the lower end of the nozzle is located at the circle
In tubular guide shell.
5. horizontal pressure-bearing type integrated water quality purifying treater according to claim 4, it is characterised in that
The bottom of the cylindrical shape guide shell is provided with filter screen, and multiple vortex balls are provided with the cylindrical shape guide shell.
6. horizontal pressure-bearing type integrated water quality purifying treater according to claim 1, it is characterised in that
Check-valves and transmissometer are connected with the primary effluent pipe, backwash outlet pipe is connected with the connecting tube, it is described anti-
Water pipe, the connecting tube, the horizontal distribution channel and the secondary effluent pipe is washed out to be sequentially communicated to form backwash path.
7. horizontal pressure-bearing type integrated water quality purifying treater according to claim 1, it is characterised in that
Air bleeding valve is provided with the top of the connecting tube.
8. horizontal pressure-bearing type integrated water quality purifying treater according to claim 1, it is characterised in that
The filter layer combiner includes filtrate supporting plate and the multimedium filter material layer being arranged in the filtrate supporting plate, institute
Bottom of the filtrate supporting plate positioned at the filter chamber is stated, the secondary effluent pipe is located at the bottom of the multimedium filter material layer, institute
State secondary effluent pipe and be provided with effluent collection device, the effluent collection device is connected with the multimedium filter material layer.
9. horizontal pressure-bearing type integrated water quality purifying treater according to claim 8, it is characterised in that
The effluent collection device includes many radial directions along the secondary effluent pipe side by side and spaced screen pipe, each institute
The one end for stating screen pipe connects with the secondary effluent pipe, the other end closing of each screen pipe, is set on each screen pipe
There are multiple spaced filter caps for intaking.
10. horizontal pressure-bearing type integrated water quality purifying treater according to any one of claim 1 to 9, its feature
It is,
The mud chamber, the clarifying chamber and the filter chamber by along the Horizontal closed formula pressure-bearing shell it is radial parallel and interval
The first dividing plate and second partition for setting are separated;
The 3rd dividing plate being be arranged in parallel with first dividing plate, the 3rd dividing plate are provided with the Horizontal closed formula pressure-bearing shell
Between first dividing plate and the second partition, first dividing plate, the 3rd dividing plate and Horizontal closed formula are held
The side wall of pressure shell body encloses to form the vertical distribution channel, and the top of first dividing plate is provided with breach and is formed described matches somebody with somebody vertically
The inlet of tank, the bottom of the 3rd dividing plate is provided with the liquid outlet that lower breach forms the vertical distribution channel.
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110790404A (en) * | 2019-12-09 | 2020-02-14 | 中冶京诚工程技术有限公司 | River channel aeration device and aeration method |
CN110921738A (en) * | 2019-12-09 | 2020-03-27 | 中冶京诚工程技术有限公司 | River course dosing device and dosing method |
-
2016
- 2016-12-21 CN CN201621407721.5U patent/CN206308168U/en active Active
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110790404A (en) * | 2019-12-09 | 2020-02-14 | 中冶京诚工程技术有限公司 | River channel aeration device and aeration method |
CN110921738A (en) * | 2019-12-09 | 2020-03-27 | 中冶京诚工程技术有限公司 | River course dosing device and dosing method |
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