CN202089850U - Intelligent integral water treatment device - Google Patents
Intelligent integral water treatment device Download PDFInfo
- Publication number
- CN202089850U CN202089850U CN2011201700756U CN201120170075U CN202089850U CN 202089850 U CN202089850 U CN 202089850U CN 2011201700756 U CN2011201700756 U CN 2011201700756U CN 201120170075 U CN201120170075 U CN 201120170075U CN 202089850 U CN202089850 U CN 202089850U
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- water
- district
- flocculation reaction
- settler
- siphon
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Abstract
The utility model discloses an intelligent integral water treatment device, which combines a flocculation reaction device, a sedimentation device and a filtering device together. By means of an automatic siphon back wash system and by integrating the processes of a coagulation reaction, a sedimentation reaction, gravity type valveless automatic back wash filtering and the like, the efficiency of a device is improved, the occupied area is reduced, the operation cost of specially-assigned persons and the like are saved, and accordingly the effects of energy saving and benefit increasing are achieved.
Description
Technical field
The utility model relates to a kind of water treating equipment, more particularly, relating to can be in wide application field, for comprising that waterworks, hospital, school, mine, machinery, weaving, printing and dyeing, food-processing, electromechanics, power station etc. need carry out the water treating equipment of water purification filter pre-treatment and sewage purification filtration treatment to surface water, river etc.
Background technology
The water treating equipment of the at present common vertical-flow reaction settler of use, are deposited in one at the flocculation of collection conventional water treatment process, adopt eddy flow to add grid reaction and tube settling.Reaction zone flows by control water, makes the colloid in the water collide mutually, adsorb, and is gathered into the bigger particle of particle diameter, then slowly sedimentation.The subject matter that exists is, occupation area of equipment is very big, highly very high, the flocculation reaction time short, effect of settling is poor, is less than 1000 degree to the requirement of raw water turbidity, to former water greater than 1000 degree to no effect.
Traditional water treating equipment generally need be provided with special backwash pump equipment is carried out periodic flushing, remove the expense of purchase of equipment and the cost of labor of arranging the personal management, also will expend a large amount of power costs.And some adopt the water treating equipment of the strainer of waterpower, machinery control, need be provided with to force backwash pump and back flushing water tank, after debugging is finished, need the personal management.The subject matter of its existence is that floor space is big especially, siphon function success ratio low (or not having the siphon function), a large amount of back flushing water body, the easy oxidations of equipment clear water upcast of waste are rotted, and causes short and polluted-water etc. once more in work-ing life.
Summary of the invention
The technical problems to be solved in the utility model is that at the prior art deficiency, providing a kind of can increase work efficiency, and dwindles floor space, saves the water treating equipment of special messenger's process cost with energy efficiency.
For solving the problems of the technologies described above, the technical scheme that the utility model adopted is: a kind of water treating equipment, comprise flocculation reaction device, settler, U type pipe and filtration unit, described flocculation reaction device top is communicated with settler by diversion trench, described filtration unit is positioned at the below of settler, and described settler is communicated with filtration unit.
Described flocculation reaction device comprises the third order reaction district, is respectively flocculation reaction one district, flocculation reaction two districts and reaction precipitation three districts by current through order, connect in the vertical shaft mode and be communicated with by diversion trench in the third order reaction district, the third order reaction district of described flocculation reaction device all is provided with the perforated grill that multilayer is evenly distributed with some identical perforates, and the bottom, third order reaction district of described flocculation reaction device is equipped with blow-off pipe.
Described settler comprises diversion trench, flat flow settling region, honeycomb inclined-tube district, catchment area, distributing trough, mud-collecting slot and blow-off pipe, described diversion trench bottom is communicated with the flat flow settling region, described mud-collecting slot, flat flow settling region, honeycomb inclined-tube district, catchment area, distributing trough are arranged from bottom to top, described mud-collecting slot is many swash plates structure, and described honeycomb inclined-tube district selects for use surface-area to reach the honeycomb inclined-tube of PE material of the Φ 35 * 1200 of 169 ㎡/m3.
Described settler is communicated with by U type pipe with filtration unit, and U type pipe comprises water-in, bend pipe, water outlet, and water-in and water outlet are positioned at the bend pipe two ends, and water-in is higher than water outlet and arranges.
Described filtration unit comprises water distribution baffle plate, filter material layer, water flowing canal, clear water zone, and described filtration unit has also assembled the automatic siphon back-purge system under the hydraulics that comprises siphon upcast, siphon downtake, auxiliary siphon tube, vapor pipe and siphon destroying device.
Compared with prior art, the beneficial effect that the utility model had is: the utility model is by set flocculation reaction device, settler and filtration unit, technologies such as coagulating, precipitin reaction and the filtration of gravity type boat davit valveless automatic backwash are organically combined, make that water treating equipment have that flocculation reaction is effective, sedimentation effect is stable, the anti impulsion load ability is strong, head loss is few, full-automatic back washing, energy efficiency, failure rate is low, stable and operational administrative is easy, need not advantages such as the special messenger keeps an eye on.
Description of drawings
Fig. 1 is the structural representation of the water treating equipment in the utility model;
Fig. 2 is the schema according to the water inlet order of the present utility model;
Fig. 3 is the structural representation of flocculation reaction device;
Fig. 4 is the current service chart in the flocculation reaction device;
Fig. 5 is the structural representation of perforated grill in the flocculation reaction device;
Fig. 6 is the structural representation of settler;
Fig. 7 is the front view of U type pipe;
Fig. 8 is the left view of U type pipe;
Fig. 9 is the filter apparatus configuration synoptic diagram;
Figure 10 is the front view of automatic siphon back-purge system wiring layout;
Figure 11 is the side-view of automatic siphon back-purge system wiring layout;
Figure 12 is the structural representation of automatic siphon back-purge system.
Embodiment
Below in conjunction with accompanying drawing embodiment of the present utility model is described in further detail.
As shown in Figure 1 and Figure 2, water treating equipment of the present utility model comprise water-in 1, flocculation reaction device 2, settler 3, U type pipe 4, filtration unit 5 and water outlet 6.
Former water enters flocculation reaction device 2 through water-in 1 after adding coagulating agent by line mixer.As shown in Figure 3, Figure 4, the reaction tank of flocculation reaction device is in series by first diversion trench 204 and second diversion trench 207 in the vertical shaft mode by flocculation reaction one district 202, flocculation reaction two districts 206 and reaction precipitation three districts 208.In flocculation reaction one district 202, flocculation reaction two districts 206 and reaction precipitation three districts 208, all be equipped with the multilayer perforated grill of structure as shown in Figure 5.
The former water that has added coagulating agent at first enters flocculation reaction one district 202 of flocculation reaction device, current enter first diversion trench, 204 tops by the multi-layer porous grid 213 in flocculation reaction one district from bottom to top and flow downward, current enter flocculation reaction two districts 206 in first diversion trench, 204 bottoms, and enter second diversion trench, 207 tops by the multi-layer porous grid 212 in flocculation reaction two districts from bottom to top, the current direction current downflow enters reaction precipitation three districts 208 through second diversion trench, 207 bottoms, and current continue upwards to flow and enter settler diversion trench 307 by the multi-layer porous grid 211 in reaction precipitation three districts.
Current in flocculation reaction device, flow through successively flocculation reaction one district 202, first diversion trench 204, flocculation reaction two districts 206, second diversion trench 207 and reaction precipitation three districts 208 and constantly change direction, staggered up and down flowing, when multi-layer porous grid that current assemble in by flocculation reaction device, current shrink, current enlarge after crossing mesh, form good flocculating conditions, finish the flocculation reaction process by energy expenditure.The dense water that produces because of flocculation reaction then is settled down to the flocculation reaction device bottom and is regularly discharged by blow-off pipe 203,205,209.
Current after flocculation reaction device 2 is handled enter settler 3.As shown in Figure 6, settler 3 comprises blow-off pipe 301, mud-collecting slot 302, flat flow settling region 303, honeycomb inclined-tube district 304, distributing trough 305, catchment area 306 and diversion trench 307, diversion trench 307 bottoms are communicated with flat flow settling region 303, mud-collecting slot 302, flat flow settling region 303, honeycomb inclined-tube district 304, catchment area 306, distributing trough 305 be arranged from bottom to top, mud-collecting slot 302 is many swash plates structure, and honeycomb inclined-tube district 304 selects for use surface-area to reach the honeycomb inclined-tube of PE material of the Φ 35 * 1200 of 169 ㎡/m3.
The current that enter settler 3 at first enter flat flow settling region 303 and carry out the flat flow precipitation through diversion trench 307 bottoms, current entered honeycomb inclined-tube district 304 after water level constantly raise, current change direction in honeycomb inclined-tube district 304, current further carry out precipitin reaction, last current enter catchment area 306, promptly enter distributing trough 305 and output after water level reach a certain height.The dense water that produces in the precipitin reaction process constantly is settled down to mud-collecting slot 302 and is regularly discharged by blow-off pipe 301.
Current through precipitin reaction enter U type pipe 4 through distributing trough 305.As Fig. 7, shown in Figure 8, U type pipe 4 comprises bend pipe 401, water outlet 402, water-in 403, and water-in 403 and water outlet 402 are positioned at bend pipe 401 two ends, and water-in 403 is higher than water outlet 402 and arranges.Current flow from top to bottom by water-in 403 and enter filtration unit 5 through bend pipe 401 by water outlet 403.
As shown in Figure 9, filtration unit 5 comprises water distribution baffle plate 506, filter material layer 507, water flowing canal 508, clear water zone 509, the current that entered filtration unit 5 by U type pipe 4 at first enter siphon upcast 505, flow down to water distribution baffle plate 506 then and by its water distribution uniformity to filter material layer 507, current enter water flowing canal 508 by filter material layer 507 from top to bottom, enter clear water zone 509 then, and water level constantly rises, when arriving certain altitude, water purification is by water outlet 6 outputs.
As Figure 10, shown in Figure 11, filtration unit 5 is equipped with the automatic siphon back-purge system 500 under the hydraulics.As shown in figure 12, automatic siphon back-purge system 500 comprises siphon upcast 505, siphon downtake 503, auxiliary siphon tube 502, vapor pipe 501 and siphon destroying device 504.Filtration unit 5 is cleaner at the beginning in operation, along with pass working time, filter material layer 507 surface particles impurity increase gradually, head loss also increases thereupon, water level will slowly raise along siphon upcast 505, after head loss is increased to a certain degree, water level in the siphon upcast 505 rises to auxiliary siphon tube mouth 502 and flows down rapidly from the mouth of pipe, rely on hold under the arm the gas and jet action and vapor pipe 501 of current that the air in the siphon upcast 505 is taken away, make siphon upcast 505 form vacuum, water in the siphon upcast 505 is just crossed the pipe top in large quantities and is fallen along siphon downtake 503 under barometric point, promptly begun backwash process.From down and the upper punch filter wash bed of material 507, when the water level of clear water zone 509 drops to siphon destroying device 504 (about about 5min), siphon is destroyed and flushing process finishes through water flowing canal 508 for the water of clear water zone 509, and filtration begins again.
Claims (5)
1. water treating equipment, comprise flocculation reaction device, settler, U type pipe and filtration unit, it is characterized in that: described flocculation reaction device top is communicated with settler by diversion trench, described filtration unit is positioned at the below of settler, and described settler is communicated with filtration unit.
2. water treating equipment according to claim 1, it is characterized in that: described flocculation reaction device comprises the third order reaction district, is respectively flocculation reaction one district, flocculation reaction two districts and reaction precipitation three districts by current through order, connect in the vertical shaft mode and be communicated with by diversion trench in the third order reaction district, the third order reaction district of described flocculation reaction device all is provided with the perforated grill that multilayer is evenly distributed with some identical perforates, and the bottom, third order reaction district of described flocculation reaction device is equipped with blow-off pipe.
3. water treating equipment according to claim 1, it is characterized in that: described settler comprises diversion trench, flat flow settling region, honeycomb inclined-tube district, catchment area, distributing trough, mud-collecting slot and blow-off pipe, described diversion trench bottom is communicated with the flat flow settling region, described mud-collecting slot, flat flow settling region, honeycomb inclined-tube district, catchment area, distributing trough are arranged from bottom to top, described mud-collecting slot is many swash plates structure, and described honeycomb inclined-tube district selects for use surface-area to reach the honeycomb inclined-tube of PE material of the Φ 35 * 1200 of 169 ㎡/m3.
4. water treating equipment according to claim 1, it is characterized in that: described settler is communicated with by U type pipe with filtration unit, U type pipe comprises water-in, bend pipe, water outlet, and water-in and water outlet are positioned at the bend pipe two ends, and water-in is higher than water outlet and arranges.
5. water treating equipment according to claim 1, it is characterized in that: described filtration unit comprises water distribution baffle plate, filter material layer, water flowing canal, clear water zone, and described filtration unit has also assembled the automatic siphon back-purge system under the hydraulics that comprises siphon upcast, siphon downtake, auxiliary siphon tube, vapor pipe and siphon destroying device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201700756U CN202089850U (en) | 2011-05-25 | 2011-05-25 | Intelligent integral water treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201700756U CN202089850U (en) | 2011-05-25 | 2011-05-25 | Intelligent integral water treatment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202089850U true CN202089850U (en) | 2011-12-28 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011201700756U Expired - Fee Related CN202089850U (en) | 2011-05-25 | 2011-05-25 | Intelligent integral water treatment device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202089850U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102328976A (en) * | 2011-05-25 | 2012-01-25 | 湖南泉江环保科技有限公司 | Intelligent integrated water treatment device and water treatment method thereof |
| CN103523911A (en) * | 2013-09-13 | 2014-01-22 | 杭州师范大学 | Self-mixing type anaerobic ammonia oxidation baffle plate reactor |
| CN103539280A (en) * | 2012-07-16 | 2014-01-29 | 杨志江 | Integrated water purification device |
-
2011
- 2011-05-25 CN CN2011201700756U patent/CN202089850U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102328976A (en) * | 2011-05-25 | 2012-01-25 | 湖南泉江环保科技有限公司 | Intelligent integrated water treatment device and water treatment method thereof |
| CN103539280A (en) * | 2012-07-16 | 2014-01-29 | 杨志江 | Integrated water purification device |
| CN103523911A (en) * | 2013-09-13 | 2014-01-22 | 杭州师范大学 | Self-mixing type anaerobic ammonia oxidation baffle plate reactor |
| CN103523911B (en) * | 2013-09-13 | 2015-01-14 | 杭州师范大学 | Self-mixing type anaerobic ammonia oxidation baffle plate reactor |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20111228 Termination date: 20140525 |