CN205313269U - Water treatment device - Google Patents
Water treatment device Download PDFInfo
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- CN205313269U CN205313269U CN201620046841.0U CN201620046841U CN205313269U CN 205313269 U CN205313269 U CN 205313269U CN 201620046841 U CN201620046841 U CN 201620046841U CN 205313269 U CN205313269 U CN 205313269U
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- water
- well
- treatment facilities
- pipe
- water treatment
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Abstract
(B, ) the utility model relates to a water treatment device, including the source water pipe, with the potassium permanganate dosing system that is linked together of the import department of source water pipe, with the first absorbing well, absorption well that is linked together of the export of source water pipe, with the in -take pump room that is linked together of first absorbing well, absorption well, with the raceway that is linked together of in -take pump room, with the sedimentation tank that is linked together of raceway, with the active carbon dosing system that is linked together of raceway, with (b) (b) V (b) (b) type filtering pond of being linked together of sedimentation tank, with the disinfection contact chamber that is linked together of (b) (b) V (b) (b) type filtering pond, with the clean water basin that is linked together of disinfection contact chamber, with the second absorbing well, absorption well that is linked together of clean water basin, with the second grade pump house that is linked together of second absorbing well, absorption well, with the water supply network that is linked together of second grade pump house. The utility model discloses a water treatment device moves stably, can continuous production, get rid of the effectual of (b) (b) 2 -MIB (b) (b), and the quality of water after the processing is up to standard. (B, )
Description
Technical field
This utility model is specifically related to a kind of water treatment facilities.
Background technology
The biological metabolisms such as algae in summer water, actinomycetes can produce 2-MIB. Owing to 2-MIB belongs to larger molecular organics, conventional water treatment process (coagulation, precipitation, filtration, sterilization) to it almost without removal effect, for ensure effluent water quality, it is necessary to by pre-oxidation and absorption remove.
Conventional pre-oxidation agent has potassium permanganate, ozone, hydrogen peroxide etc., and conventional treatment process water factory does not possess ozone and adds ability, and it is shorter that hydrogen peroxide stores the time.
Utility model content
Technical problem to be solved in the utility model is to provide and a kind of utilizes potassium permanganate to carry out the water treatment facilities of water process for pre-oxidation agent.
For solving above-mentioned technical problem, a kind of technical scheme that this utility model adopts is:
A kind of water treatment facilities, including main water supply tube, the potassium permanganate dosing system being connected with the import department of described main water supply tube, the first absorbing well, absorption well that outlet with described main water supply tube is connected, the water plant being connected with the first described absorbing well, absorption well, the water-supply-pipe being connected with described water plant, the sedimentation tank being connected with described water-supply-pipe, the activated carbon dosing system being connected with described water-supply-pipe, the V-type filter tank being connected with described sedimentation tank, the antisepsis contact tank being connected with described V-type filter tank, the clear water reserviors being connected with described antisepsis contact tank, the second absorbing well, absorption well being connected with described clear water reserviors, the repumping house being connected with the second described absorbing well, absorption well, the water supply network being connected with described repumping house.
Specifically, described potassium permanganate dosing system is also connected for adding potassium permanganate in the first described absorbing well, absorption well with the first described absorbing well, absorption well.
Specifically, described potassium permanganate dosing system is also connected for adding potassium permanganate in described water-supply-pipe with described water-supply-pipe.
Specifically, described activated carbon dosing system is also connected for adding activated carbon in the first described absorbing well, absorption well with the first described absorbing well, absorption well.
Specifically, described activated carbon dosing system is also connected for adding activated carbon in described sedimentation tank with described sedimentation tank.
Specifically, described sedimentation tank is folded plate flocculator and/or horizontal sedimentation tank.
Specifically, described water treatment facilities also includes being connected with described main water supply tube for being connected with described water-supply-pipe for being connected with described antisepsis contact tank for being connected with described clear water reserviors for the benefit chlorine system of chlorination in described clear water reserviors to the rear chlorination feeding system of chlorination in described antisepsis contact tank to the front chlorination feeding system of chlorination in described water-supply-pipe to the heavy chlorine dosing system of chlorination in described main water supply tube.
Specifically, described water treatment facilities also includes the coagulant feeding system being connected for adding coagulant in described water-supply-pipe with described water-supply-pipe.
Specifically, described water treatment facilities also includes being connected for the rinser that described V-type filter tank is carried out with described V-type filter tank.
Specifically, described water treatment facilities also includes being connected with described sedimentation tank for the sludge treating system processing the mud in described sedimentation tank, is connected with described V-type filter tank and described sedimentation tank for the blow-off pipe by the sewage transport in described V-type filter tank to described sedimentation tank respectively.
Scope of the present utility model, however it is not limited to the technical scheme of the particular combination of above-mentioned technical characteristic, also should contain other technical scheme being carried out combination in any by above-mentioned technical characteristic or its equivalent feature and being formed simultaneously. Such as features described above and (but not limited to) disclosed herein have the technical characteristic of similar functions and replace mutually and the technical scheme etc. that formed.
Owing to technique scheme is used, this utility model compared with prior art has the advantage that
Water treatment facilities of the present utility model is stable, it is possible to produce continuously, removes the effective of 2-MIB and water quality reaching standard after treatment.
Accompanying drawing explanation
Fig. 1 is schematic diagram of the present utility model;
Wherein: 1, main water supply tube; 2, potassium permanganate dosing system; 3, weight chlorine dosing system; 4, the first absorbing well, absorption well; 5, water plant; 6, water-supply-pipe; 7, sedimentation tank; 8, activated carbon dosing system; 9, front chlorination feeding system; 10. coagulant feeding system; 11, sludge treating system; 12, V-type filter tank; 13, rinser; 14, blow-off pipe; 15, antisepsis contact tank; 16, rear chlorination feeding system; 17, clear water reserviors; 18, chlorine system is mended; 19, the second absorbing well, absorption well; 20, repumping house; 21, water supply network.
Detailed description of the invention
Below in conjunction with accompanying drawing, this utility model made further detailed complete illustrate.
Potassium permanganate is pre-oxidation agent, and the time of contact of medicament and water need to reach more than 30min and just can tell on, therefore selecting toss area position is main water supply tube 1 road head, adopts centrifugal pump to add, and waterpower mixes. More than 30min time of contact is considered in adding of Powdered Activated Carbon, simultaneously takes account of the dust active carbon abrasion to equipment, for ensureing the continuous of water factory and stable operation, after toss area is arranged on water pump, and sedimentation tank 7 head. Dosing method is that centrifugal pump adds, and waterpower mixes.
As it is shown in figure 1, a kind of water treatment facilities, including main water supply tube 1, the potassium permanganate dosing system 2 being connected with the import department of main water supply tube 1, it is connected for the weight chlorine dosing system 3 of chlorination in main water supply tube 1 with main water supply tube 1, the first absorbing well, absorption well 4 that outlet with main water supply tube 1 is connected, the water plant 5 being connected with the first absorbing well, absorption well 4, the water-supply-pipe 6 being connected with water plant 5, the sedimentation tank 7 being connected with water-supply-pipe 6, the activated carbon dosing system 8 being connected with water-supply-pipe 6, it is connected for the front chlorination feeding system 9 of chlorination in water-supply-pipe 6 with water-supply-pipe 6, be connected the coagulant feeding system 10 for adding coagulant in water-supply-pipe 6 with water-supply-pipe 6, be connected the sludge treating system 11 for processing the mud in sedimentation tank 7 with sedimentation tank 7, the V-type filter tank 12 being connected with sedimentation tank 7, it is connected with V-type filter tank 12 for the rinser 13 that V-type filter tank 12 is carried out, it is connected with V-type filter tank 12 and sedimentation tank 7 for the blow-off pipe 14 by the sewage transport in V-type filter tank 12 to sedimentation tank 7 respectively, the antisepsis contact tank 15 being connected with V-type filter tank 12, it is connected for the rear chlorination feeding system 16 of chlorination in antisepsis contact tank 15 with antisepsis contact tank 15, the clear water reserviors 17 being connected with antisepsis contact tank 15, it is connected for the benefit chlorine system 18 of chlorination in clear water reserviors 17 with clear water reserviors 17, the second absorbing well, absorption well 19 being connected with clear water reserviors 17, the repumping house 20 being connected with the second absorbing well, absorption well 19, the water supply network 21 being connected with repumping house 20.
In this utility model, sedimentation tank 7 is folded plate flocculator and/or horizontal sedimentation tank.
Rinser 13 includes air blast machine room and backwash pump house.
Potassium permanganate of the present utility model is additionally provided with toss area that as follows can be standby, and potassium permanganate dosing system 2 is also connected with the first absorbing well, absorption well 4 for adding potassium permanganate in the first absorbing well, absorption well 4; Potassium permanganate dosing system 2 is also connected for adding potassium permanganate in water-supply-pipe 6 with water-supply-pipe 6.
Activated carbon of the present utility model is additionally provided with toss area that as follows can be standby, and activated carbon dosing system 8 is also connected with the first absorbing well, absorption well 4 for adding activated carbon in the first absorbing well, absorption well 4; Activated carbon dosing system 8 is also connected for adding activated carbon in sedimentation tank 7 with sedimentation tank 7.
During work, after passing sequentially through main water supply tube the 1, first absorbing well, absorption well 4, water plant 5, water-supply-pipe 6, sedimentation tank 7, V-type filter tank 12, antisepsis contact tank 15, clear water reserviors the 17, second absorbing well, absorption well 19, repumping house 20 from the water of water head site, it is delivered to water supply network 21.
As it has been described above, we are illustrated fully according to objective of the present utility model, but this utility model is not limited to above-described embodiment and implementation. The practitioner of correlative technology field can carry out different changes and enforcement in the scope that technological thought of the present utility model is permitted。
Claims (10)
1. a water treatment facilities, it is characterised in that: include main water supply tube (1), the potassium permanganate dosing system (2) being connected with the import department of described main water supply tube (1), the first absorbing well, absorption well (4) that outlet with described main water supply tube (1) is connected, the water plant (5) being connected with described the first absorbing well, absorption well (4), the water-supply-pipe (6) being connected with described water plant (5), the sedimentation tank (7) being connected with described water-supply-pipe (6), the activated carbon dosing system (8) being connected with described water-supply-pipe (6), the V-type filter tank (12) being connected with described sedimentation tank (7), the antisepsis contact tank (15) being connected with described V-type filter tank (12), the clear water reserviors (17) being connected with described antisepsis contact tank (15), the second absorbing well, absorption well (19) being connected with described clear water reserviors (17), the repumping house (20) being connected with described the second absorbing well, absorption well (19), the water supply network (21) being connected with described repumping house (20).
2. water treatment facilities according to claim 1, it is characterised in that: described potassium permanganate dosing system (2) is also connected for adding potassium permanganate in described the first absorbing well, absorption well (4) with described the first absorbing well, absorption well (4).
3. water treatment facilities according to claim 1, it is characterised in that: described potassium permanganate dosing system (2) is also connected for adding potassium permanganate in described water-supply-pipe (6) with described water-supply-pipe (6).
4. water treatment facilities according to claim 1, it is characterised in that: described activated carbon dosing system (8) is also connected for adding activated carbon in described the first absorbing well, absorption well (4) with described the first absorbing well, absorption well (4).
5. water treatment facilities according to claim 1, it is characterised in that: described activated carbon dosing system (8) is also connected for adding activated carbon in described sedimentation tank (7) with described sedimentation tank (7).
6. water treatment facilities according to claim 1, it is characterised in that: described sedimentation tank (7) is folded plate flocculator and/or horizontal sedimentation tank.
7. water treatment facilities according to claim 1, it is characterized in that: described water treatment facilities also includes being connected with described main water supply tube (1) for the heavy chlorine dosing system (3) of chlorination in described main water supply tube (1), it is connected for the front chlorination feeding system (9) of chlorination in described water-supply-pipe (6) with described water-supply-pipe (6), it is connected for the rear chlorination feeding system (16) of chlorination in described antisepsis contact tank (15) with described antisepsis contact tank (15), it is connected with described clear water reserviors (17) for benefit chlorine system (18) of chlorination in described clear water reserviors (17).
8. water treatment facilities according to claim 1, it is characterised in that: described water treatment facilities also includes the coagulant feeding system (10) being connected for adding coagulant in described water-supply-pipe (6) with described water-supply-pipe (6).
9. water treatment facilities according to claim 1, it is characterised in that: described water treatment facilities also includes being connected for the rinser (13) that described V-type filter tank (12) is carried out with described V-type filter tank (12).
10. water treatment facilities according to claim 1, it is characterised in that: described water treatment facilities also includes being connected with described sedimentation tank (7) for the sludge treating system (11) processing the mud in described sedimentation tank (7), is connected with described V-type filter tank (12) and described sedimentation tank (7) for the blow-off pipe (14) by the sewage transport in described V-type filter tank (12) to described sedimentation tank (7) respectively.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620046841.0U CN205313269U (en) | 2016-01-19 | 2016-01-19 | Water treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620046841.0U CN205313269U (en) | 2016-01-19 | 2016-01-19 | Water treatment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205313269U true CN205313269U (en) | 2016-06-15 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620046841.0U Active CN205313269U (en) | 2016-01-19 | 2016-01-19 | Water treatment device |
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| CN (1) | CN205313269U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114314705A (en) * | 2021-11-25 | 2022-04-12 | 合肥供水集团有限公司 | Purification treatment method of overproof raw water |
-
2016
- 2016-01-19 CN CN201620046841.0U patent/CN205313269U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114314705A (en) * | 2021-11-25 | 2022-04-12 | 合肥供水集团有限公司 | Purification treatment method of overproof raw water |
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