CN203196398U - Efficient micro-resistance pulsation vortex sedimentation device - Google Patents
Efficient micro-resistance pulsation vortex sedimentation device Download PDFInfo
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- CN203196398U CN203196398U CN 201320222019 CN201320222019U CN203196398U CN 203196398 U CN203196398 U CN 203196398U CN 201320222019 CN201320222019 CN 201320222019 CN 201320222019 U CN201320222019 U CN 201320222019U CN 203196398 U CN203196398 U CN 203196398U
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- whirlpool
- baffle plate
- sedimentation
- pulsation
- water
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- 238000004062 sedimentation Methods 0.000 title claims abstract description 33
- 230000010349 pulsation Effects 0.000 title claims abstract description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 55
- 238000007599 discharging Methods 0.000 claims abstract description 18
- 239000010802 sludge Substances 0.000 claims abstract description 17
- 238000006243 chemical reaction Methods 0.000 claims abstract description 11
- 238000005192 partition Methods 0.000 claims abstract description 3
- 239000004744 fabric Substances 0.000 claims description 8
- 230000003139 buffering effect Effects 0.000 claims description 6
- 230000000630 rising effect Effects 0.000 claims description 5
- 230000004888 barrier function Effects 0.000 claims description 2
- 230000015572 biosynthetic process Effects 0.000 claims description 2
- 238000011282 treatment Methods 0.000 abstract description 11
- 238000009826 distribution Methods 0.000 abstract description 7
- 230000001174 ascending effect Effects 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 abstract 1
- 230000000694 effects Effects 0.000 description 7
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- 239000008187 granular material Substances 0.000 description 6
- 238000005265 energy consumption Methods 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 230000008859 change Effects 0.000 description 3
- 238000010276 construction Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 230000006872 improvement Effects 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- 239000010865 sewage Substances 0.000 description 3
- 230000015271 coagulation Effects 0.000 description 2
- 238000005345 coagulation Methods 0.000 description 2
- 230000007812 deficiency Effects 0.000 description 2
- 238000000151 deposition Methods 0.000 description 2
- 230000008021 deposition Effects 0.000 description 2
- 239000000945 filler Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 229910000975 Carbon steel Inorganic materials 0.000 description 1
- 206010037544 Purging Diseases 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 239000010962 carbon steel Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000000701 coagulant Substances 0.000 description 1
- 230000001112 coagulating effect Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 238000005189 flocculation Methods 0.000 description 1
- 230000016615 flocculation Effects 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 230000002706 hydrostatic effect Effects 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
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Abstract
The utility model belongs to the field of water treatment equipment designing and manufacturing, and particularly relates to an efficient micro-resistance pulsation vortex sedimentation device. The efficient micro-resistance pulsation vortex sedimentation device comprises a shell. A water inlet and a water outlet are sequentially formed in the left side shell wall and the right side shell wall of the upper portion of the shell. A sludge discharging area is arranged at the bottom end of the shell. Sludge discharging ports are formed in the sludge discharging area. The interior of the shell is divided by a middle partition plate into a water distribution area on the water inlet side, a sedimentation area on the water outlet side and the sludge discharging area at the bottom. A pulsation vortex sedimentation layer formed by a plurality of micro-resistance vortex sedimentation devices is arranged inside the sedimentation area. The micro-resistance vortex sedimentation devices are inclined pipes. A plurality of inclined baffles are arranged in the center of an inner cavity of each pipe at intervals along the axis of each pipe. The inclining directions of the inclined baffles are opposite to the inclining directions of the pipes. The 30-60-degree included angles are formed by the baffles and the pipe walls of the pipes. The two ends of the baffles and the pipe walls form water flow ascending channels and sludge downwards gliding channels. Vortex reaction areas are formed between the adjacent baffles.
Description
Technical field
The utility model relates to water treatment facilities and manufactures and designs the field, relates in particular to a kind of settler.
Background technology
Settler is in the water treatment system engineering, no matter as pretreatment system or the auxiliary equipment of two stage treatment has indispensable effect, the tradition settler mainly contains inclined tube (plate) settler of vertical-flow, flat flow, radial-flow, tube settling and modified form etc., the pond type of each quasi-tradition or improvement version all exists some shortcomings, larger such as the pond degree of depth, the practice of construction difficulty, cost is relatively costly; Precipitation water inlet water distribution is difficult for evenly, the sludge drainage system relative complex, and the operation workload is very large, spoil disposal machinery is located at that water-bed easy-to-rust damages or spoil disposal facility material quality requirements is higher, one-time investment is more expensive, and inconvenient maintenance in the reality, and some pond type floor spaces are very large; Part pond type water velocity is unstable, is advanced the influence of fluctuations of water flow velocity larger; It is complicated that mud, soil discharging facility are scraped in the bottom, to unit in charge of construction require high; The ability of anti-various unfavorable factors a little less than, streamflow regime is unstable, water distribution is complicated, being difficult to evenly directly affects the facility treatment effect.Relevant deposition facility dosing stirring reaction energy consumption is larger in the past simultaneously, and especially the big yield system is more obvious; It is different that the different sewage classification is equipped with demand to related agents, and different classes of assistant medicament reaction dissolving requires to be not quite similar, the flowability of precipitum is to some extent difference also, control requires complicated relatively, operational management is larger, and part sedimentation material easily gathers dirty stifled, causes local accumulation to affect whole structure.The related application of existing sedimentation facilities exists many limitation factors on the whole, though respectively there is the characteristics problem also relatively obvious, can not adapt to day by day complicated all kinds of water treatment systems.
One kind of Chinese patent CN2542311 is used for the tube settler that coagulant sedimentation is disposed of sewage, the pool wall top that pond body two is relative, have water inlet and delivery port, have sludge outlet with the pool wall bottom of delivery port homonymy, progressively tilt from high to low from water inlet one side to sludge outlet one side at the bottom of the pond, the pond body is separated into two-layer up and down by baffle plate in the pond, the upper strata is clear water zone, lower floor is cloth pool and settling zone, water inlet communicates with the settling zone by a vertical passage, settle one group of inclined tube on the baffle plate, the lower end import of inclined tube is with the cloth pool and the settling zone communicates and nearly sludge outlet one side, the upper end outlet is in the middle and upper part of clear water zone and a side of nearly water inlet, it is characterized in that the horizontal level of described delivery port is higher than water inlet 5～25cm.Compared with prior art, the utility model has suitably improved the delivery port level height, the side knock effect of current in the clear water zone is obviously reduced, thereby the remaining floccule content of water outlet significantly reduces.
Multi-layered and variable-angle swash plate or the tube settler of Chinese patent CN101002993 intensifying treatment effect, it relates to a kind of water treatment facilities.The problem that the turbidity removal rate that the utility model has solved existing swash plate/tube settler is low, operating cost is high.Placing 2～5 layers of total height in the sedimentation basin of the present utility model is 1.0～1.8m settler, and every layer of settler is swash plate or inclined tube, and every layer of settler angle of inclination is 15～80 °, and the angle of inclination of the relative settler of water (flow) direction is for forward or reverse.The utlity model has the advantage that investment operating cost is low, turbidity removal rate is high.
Chinese patent CN2075534 high efficient coagulating sedimentation basin.By the series-type circular pipe primary reactor, fine mesh grid reaction pond narrow space inclined plate settling basin three parts consist of.The pipe primary reactor is by plural serial stage, and side direction has a plurality of water inlets and delivery port, and this device is raised the efficiency one times, but the decrease construction costs also can reduce the day-to-day operation expense significantly.Also can make as required simultaneously the small water supplying treatment facility of different size, enlarge range of application.
Although above-mentioned patent is improved traditional tank type and water inlet water distribution mode or inclined tube (plate); Or increased the number of plies and the angle of inclined tube (plate), and change the flow direction switching, thereby improved the whole structure of facility, or changed dosing coagulation mode, improve the polluter cohesion effect of uniting, thereby strengthen disposal ability; Eliminating thoroughly its original deficiency but be, only is that the part facility is improved optimization, even has brought some new defectives, and the too little or number of plies easily causes local mud to pile up too much such as the filler inclination angle, causes water outlet uneven, moves for a long time even damage filler; The waterpower flow process is oversize, causes facility to take up an area excessive and spoil disposal is inconvenient, needs to increase the supplementary means such as flushing purgings, and relative energy consumption is higher.
Summary of the invention
The utility model is for the deficiencies in the prior art, provide a kind of can effectively reduce the plant area area and structural shape flexible, the treatment effect of increasing water quality greatly, substantially need not simultaneously other energy consumptions, pressure water inlet or gravity flow water inlet all can, whole facility can carry out the little resistance pulsation of the multiple flow passages super low energy consumption whirlpool sedimentation device of extensive use without power consumption equipment in various water treatments.
The utility model one key problem in technology is to be provided with the pulsation whirlpool settled layer that several little resistance whirlpool sedimentation devices form side by side in the settling zone, form the reaction of pulsation whirlpool, the further flocculation of flco is united after making dosing, has suppressed the floating of tiny alumen ustum, improves effluent quality.Its concrete technical scheme is: a kind of efficient little resistance pulsation whirlpool sedimentation device, comprise housing, be disposed with water inlet and delivery port on the shell wall of the left and right sides, housing top, the housing bottom is sludge discharging area, be provided with mud discharging mouth, barrier partitions becomes the cloth pool of water inlet side in using in the housing, the settling zone of delivery port side and the sludge discharging area of bottom, it is characterized in that being provided with in the described settling zone pulsation whirlpool settled layer that several little resistance whirlpool sedimentation devices form side by side, described little resistance whirlpool sedimentation device is tilted tube, the inner cavity of pipe center arranges some sloping baffles along the axis interval, described baffle plate incline direction is opposite with the pipeline incline direction, form 30 ~ 60 angles of spending with tube wall, the gap of baffle plate two ends and tube wall consists of current rising passway and mud sliding channel, consists of the whirlpool reaction zone between adjacent screen.
Described pulsation whirlpool settled layer is divided into three different functional blocks substantially: be divided into the different current rising passway of quantity, whirlpool reaction zone and mud sliding channel according to processing water yield difference.The current that contain all kinds of granule foreigns enter after this settled layer, march forward along the current rising passway, in the way of advancing, enter the whirlpool reaction zone through all kinds of granule foreigns of coagulation in the water, whenever, after stopping, collision slides to the mud sliding channel through a whirlpool reaction zone agglomerate mud granule, enter the bottom mud collection area, simultaneously tiny alumen ustum is after hydraulic action enters pulsation whirlpool district, collision is formed a team and is embraced knot mutually, form larger mud granule, also enter the bottom sludge discharging area through the mud sliding channel, so current are in uphill process, all kinds of granule foreigns constantly repeat above-mentioned motion, and collision is glided, and has improved greatly the settling zone load, be the 10--30 of in the past conventional method doubly, even higher.
Another key problem in technology of the present utility model is that intake tunnel adopts a kind of new water distribution manner; pending water source enters after the system; by little resistance water distribution mechanism; adjust slowly flow rate of water flow and water (flow) direction at fine suspension or colloidal particles when absorption is combined into larger particles mutually; make water water source flow speed stability; under low flow rate regime, enter the settling zone; reduce the system shock load; guarantee decanting zone water inlet even water distribution; also have simultaneously certain preliminary sedimentation function, alleviate post precipitation district sedimentation load.Its concrete technical scheme is: described cloth pool is divided into vertical intake tunnel from top to bottom, buffering is adjusted the district, two baffle plates that tilt clockwise are set in the described buffering adjustment district one on the other, baffle plate middle part during the overhead gage upper end connects, the lower end is downward-sloping, and consist of buffer runner between housing sidewall, described lower baffle plate is arranged at middle baffle plate below, consist of variable flow channel between upper lower baffle plate, the lower baffle plate upper end consists of the data feedback channel that flows into the settling zone with gap, middle plate washer lower end, and the gap of lower baffle plate lower end and housing sidewall consists of the drain outlet.
As further improvement, described housing sidewall and overhead gage with overhead gage formation buffer runner be arranged in parallel.Flow and the stationarity of buffer runner have been improved by this kind setting, more effective adjusting flow rate of water flow.
As further improvement, described bottom sludge discharging area is set at least one taper bucket, and mud discharging mouth is arranged at taper bucket bottom.The bucket inclination angle arranges rationally, and smooth surface is smooth and easy, guarantees that all kinds of sludgd depositions are quick, and can not adhere to the bucket side and cause mud to gather, thus the permanent operation of the system of assurance.Spoil disposal is arranged on the bucket bottom, utilizes liquid level difference pressure spoil disposal, and unpowered can consumption is so that spoil disposal is more thorough and energy saving economy.
The beneficial effects of the utility model: the utility model can be effectively so that in the water all kinds of granule foreign sedimentations thorough fast; And unpowered supporting, energy saving economy; The high load capacity design is saved the area; And effluent quality is good, and the part situation can reduce or cancel follow-up filtration system, cost saving.Be applicable to various feedwater and sewage disposal system, and all can reach satisfied result of use.As reasonable in design, the delivery turbidity in processing procedure can reach about 1, can greatly reduce the filtration system of subsequent configuration, even can save follow-up filtration system, reaches energy savings, occupation of land, reduces the purpose of operating cost.
Description of drawings
Fig. 1 is the structural representation of the utility model settler.
Fig. 2 is the top view of Fig. 1.
Fig. 3 is the structural representation of the little resistance whirlpool of the utility model sedimentation device.
The specific embodiment
Below in conjunction with test and specific embodiment; the utility model is further understood in exemplary illustration and help; but the embodiment detail only is for the utility model is described; do not represent the lower whole technical schemes of the utility model design; therefore should not be construed as the total technical scheme of the utility model is limited; some are In the view of the technical staff; the unsubstantiality that does not depart from the utility model design increases and/or change; for example simple the change or replacement of technical characterictic to have same or similar technique effect all belongs to the utility model protection domain.
A kind of efficient little resistance pulsation whirlpool sedimentation device, comprise housing 001, be disposed with water inlet 011 and delivery port 012 on the shell wall of the left and right sides, housing 001 top, housing 001 bottom is set to two taper buckets 013 that are arranged side by side, mud discharging mouth 014 is arranged at taper bucket 013 bottom, baffle plate 015 is separated into the cloth pool 002 of water inlet 011 side in the housing 001 interior usefulness, the settling zone 003 of delivery port 012 side and the sludge discharging area 004 of bottom, be provided with the pulsation whirlpool settled layer 031 that several little resistance whirlpool sedimentation devices 311 form side by side in the described settling zone 003, described little resistance whirlpool sedimentation device 311 is tilted tube, the inner cavity of pipe center arranges some sloping baffles 312 along the axis interval, described baffle plate 312 incline directions are opposite with the pipeline incline direction, form 30 ~ 60 angles of spending with tube wall, the gap of baffle plate 312 two ends and tube wall consists of current rising passway 313 and mud sliding channel 314, and 312 of adjacent screen consist of whirlpool reaction zone 315.Described cloth pool 002 is divided into vertical intake tunnel 021 from top to bottom, buffering is adjusted district 022, two baffle plates (221,222) that tilt clockwise are set in the described buffering adjustment district 022 one on the other, baffle plate 015 middle part during overhead gage 221 upper ends connect, the lower end is downward-sloping, and consist of buffer runner 223 between housing 001 sidewall, described housing 001 sidewall and overhead gage 221 be arranged in parallel.Described lower baffle plate 222 is arranged at middle baffle plate 015 below, consist of variable flow channel 224 between upper lower baffle plate (221,222), 015 time splaying of lower baffle plate 222 upper ends and middle plate washer consists of the data feedback channel 225 that flows into settling zone 003, and the gap of lower baffle plate 222 lower ends and housing 001 sidewall consists of drain outlet 226.
Be equipped with the hydrostatic wave suppression arrangement in the utility model, to eliminate flow-disturbing to the impact of the water velocity on convergence weir, water outlet is catchmented uniform and stable, and water outlet is fast smooth.
Little resistance whirlpool sedimentation device of the present utility model is made simple, and is extensive with material, needs to select the multiple materials such as carbon steel, PVC, PP, FPR and stainless steel to make according to different processing requirements, and mounted angle needs according to design can be 45
0-80
0Rationally adopt; Individual layer arranges, and compares with the multilayer settler of prior art, and sliding channel is more smooth and easy, can not produce the situation that cleaning is piled up and be difficult to wash to mud, moves more simple and convenient.
Claims (4)
1. efficient little resistance pulsation whirlpool sedimentation device, comprise housing, be disposed with water inlet and delivery port on the shell wall of the left and right sides, housing top, the housing bottom is sludge discharging area, be provided with mud discharging mouth, barrier partitions becomes the cloth pool of water inlet side in using in the housing, the settling zone of delivery port side and the sludge discharging area of bottom, it is characterized in that being provided with in the described settling zone pulsation whirlpool settled layer that several little resistance whirlpool sedimentation devices form side by side, described little resistance whirlpool sedimentation device is tilted tube, the inner cavity of pipe center arranges some sloping baffles along the axis interval, described baffle plate incline direction is opposite with the pipeline incline direction, form 30 ~ 60 angles of spending with tube wall, the gap of baffle plate two ends and tube wall consists of current rising passway and mud sliding channel, consists of the whirlpool reaction zone between adjacent screen.
2. a kind of efficient little resistance pulsation whirlpool sedimentation device according to claim 1, it is characterized in that described cloth pool is divided into vertical intake tunnel from top to bottom, buffering is adjusted the district, two baffle plates that tilt clockwise are set in the described buffering adjustment district one on the other, baffle plate middle part during the overhead gage upper end connects, the lower end is downward-sloping, and consist of buffer runner between housing sidewall, described lower baffle plate is arranged at middle baffle plate below, consist of variable flow channel between upper lower baffle plate, the lower baffle plate upper end consists of the data feedback channel that flows into the settling zone with gap, middle plate washer lower end, and the gap of lower baffle plate lower end and housing sidewall consists of the drain outlet.
3. a kind of efficient little resistance pulsation whirlpool sedimentation device according to claim 2 is characterized in that described housing sidewall and overhead gage with overhead gage formation buffer runner be arranged in parallel.
4. a kind of efficient little resistance pulsation whirlpool sedimentation device according to claim 1 is characterized in that described bottom sludge discharging area is set at least one taper bucket, and mud discharging mouth is arranged at taper bucket bottom.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320222019 CN203196398U (en) | 2013-04-27 | 2013-04-27 | Efficient micro-resistance pulsation vortex sedimentation device |
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| CN 201320222019 CN203196398U (en) | 2013-04-27 | 2013-04-27 | Efficient micro-resistance pulsation vortex sedimentation device |
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| CN203196398U true CN203196398U (en) | 2013-09-18 |
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| CN 201320222019 Expired - Fee Related CN203196398U (en) | 2013-04-27 | 2013-04-27 | Efficient micro-resistance pulsation vortex sedimentation device |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103301658A (en) * | 2013-04-27 | 2013-09-18 | 江苏中超环保有限公司 | Efficient micro-resistance pulsating vortex sedimentation device |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103301658A (en) * | 2013-04-27 | 2013-09-18 | 江苏中超环保有限公司 | Efficient micro-resistance pulsating vortex sedimentation device |
| CN103301658B (en) * | 2013-04-27 | 2015-07-22 | 江苏中超环保有限公司 | Efficient micro-resistance pulsating vortex sedimentation device |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 214205, Baihe Road, Yixing, Jiangsu, Wuxi Province, No. 3 Patentee after: JIANGSU ZHONGCHAO ENVIRONMENTAL PROTECTION CO., LTD. Address before: 214205, Baihe Road, Yixing, Jiangsu, Wuxi Province, No. 3 Patentee before: Jiangsu Zhongchao Environmental Protection Co., Ltd. |
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| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130918 Termination date: 20190427 |
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| CF01 | Termination of patent right due to non-payment of annual fee |