CN205398191U - Polyferric sulfate handles device of copper industry waste water - Google Patents
Polyferric sulfate handles device of copper industry waste water Download PDFInfo
- Publication number
- CN205398191U CN205398191U CN201620175918.4U CN201620175918U CN205398191U CN 205398191 U CN205398191 U CN 205398191U CN 201620175918 U CN201620175918 U CN 201620175918U CN 205398191 U CN205398191 U CN 205398191U
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- waste water
- industry waste
- hollow shaft
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Abstract
The utility model belongs to the technical field of waste water treatment, a polyferric sulfate handles device of copper industry waste water, including reactor and the agitating unit of setting at reactor, agitating unit includes hollow mixing shaft and installs a plurality of hollow stirring rake on hollow mixing shaft, the inside hollow structure intercommunication of hollow mixing shaft and hollow stirring rake, the last rotary seal of hollow mixing shaft is provided with reinforced cover, the reinforced charge door that is provided with with hollow mixing shaft's hollow structure intercommunication of putting in, all be provided with a plurality of inlets on hollow mixing shaft and the hollow stirring rake, the bore of the inlet that makes progress bottom the reactor is crescent, reactor upper portion is provided with with the medicine mouth, be provided with the delivery port on the reactor lateral wall, reactor lateral wall lower part is provided with clears up the mouth, and a clearance mouthful outside is provided with the baffle, and the baffle articulates with the reactor lateral wall, and baffle and reactor lateral wall are sealed in reaction sequence sets up, and the delivery port is located above the clearance mouth. The distribution of flocculating agent in waste water has been optimized when adding the flocculating agent.
Description
Technical field
This utility model belongs to technical field of waste water processing, particularly relates to a kind of bodied ferric sulfate and processes the device of copper industry waste water.
Background technology
Flocculant is mainly with just (bearing) some particles or the granule that are electrically difficult to separate in electrical group and some water with negative (just), reduce its electromotive force, it is at labile state, and utilize its aggregation property to make these granules concentrate, and by either physically or chemically separating.Bodied ferric sulfate is conventional flocculant.
Usually flocculant is directly added in waste water, but this addition manner makes reaction substantially concentrate on liquid surface so that flocculant action effect is substantially reduced.In order to overcome the problems referred to above, the adding set of a kind of flocculant disclosed in Chinese patent CN203683189U, it arranges coil pipe bottom reaction tank, being added flocculant by coil pipe in waste water, this mode improves the functioning efficiency of flocculant to a certain extent, but, flocculant concentrates on bottom reaction tank, wherein flocculant is by agitator, itself and waste water fully to be reacted, if flocculant can not well disperse in waste water, then water treatment effect will be substantially reduced.
Utility model content
The purpose of this utility model be overcome prior art to there is flocculant can not good scattered defect in waste water, it is provided that a kind of bodied ferric sulfate processes the device of copper industry waste water.
This utility model solves its technical problem and be the technical scheme is that a kind of bodied ferric sulfate processes the device of copper industry waste water, including reactor and the agitating device being arranged in described reactor;Described agitating device includes hollow shaft and the some hollow stirring paddle being arranged on described hollow shaft, described hollow shaft and hollow stirring paddle boring fabric connectivity;On described hollow shaft, rotary seal is provided with reinforced set, and described reinforced putting is provided with the charge door that the hollow-core construction with described hollow shaft connects;
Described hollow shaft and hollow stirring paddle are provided with some inlets, the bore of reactor bottom upwards described inlet are gradually increased;Described reactor top is provided with dosing mouth;Being provided with outlet in described sidewall of reactor, described outlet is provided with valve;Described sidewall of reactor bottom is provided with clean-up port, it is provided with baffle plate outside described clean-up port, described baffle plate is hinged with described sidewall of reactor, seals setting at baffle plate described in course of reaction with described sidewall of reactor, and described outlet is positioned at above described clean-up port.
As preferably, described outlet is apart from height is total reactor height the 1/2 of described reactor bottom.Clear water is positioned at reactor middle and upper part after precipitation, utilizes outlet effectively clear water can be discharged reactor.
As preferably, described reactor bottom is provided with discharge outlet, is provided with filter membrane in described discharge outlet.When precipitating too much in the reactor, it is possible to open discharge outlet, being discharged by the water after reacted in reactor, precipitation then filtered membrane filtration is stayed in reactor, finally manually precipitation in reactor is removed.
As preferably, for pH value in effective monitoring reactor, in described reactor, it is provided with pH on-line measuring device.
As preferably, described hollow stirring paddle quantity is two, and two described hollow stirring paddles are arranged on the differing heights of hollow shaft.Utilize two hollow stirring paddles to be stirred by waste water in reactor, and on the differing heights that can be distributed in reactor by the flocculant solution in hollow shaft waste water, optimize the distribution of flocculant.
As preferably, being provided with hollow support rails between two described hollow stirring paddles, the hollow-core construction in the hollow stirring paddle described with two of the hollow-core construction in described support bar connects, and described support bar is also equipped with some inlets.Utilize support bar can not only play stirring action, and optimize flocculant distribution in waste water further.
Beneficial effect: utilize the addition flocculant of agitating device in the application, optimizes flocculant distribution in waste water while adding flocculant, stirs while adding so that flocculant is more evenly distributed in waste water;Additionally, add due to flocculant and namely form flocculation sediment after waste water reaction, have a declining tendency under gravity, therefore it is set to upwards be gradually increased by reactor bottom by the bore of inlet, make flocculant that reactor bottom the adds flocculant less than reactor top, and top flocculant is formed and still can play a role in precipitation decline process so that flocculant fully reacts, save flocculant usage.
Accompanying drawing explanation
Below in conjunction with the drawings and specific embodiments, this utility model is described in further detail.
Fig. 1 is the structural representation of preferred embodiment of the present utility model.
Wherein: 1. reactor, 11. dosing mouths, 12. outlets, 13. clean-up ports, 14. discharge outlet, 15. baffle plates, 2. hollow shaft, 3. hollow stirring paddle, 4. reinforced set, 41. charge doors, 5. inlet, 6.pH on-line measuring device, 7. support bar, 8. filter membrane.
Detailed description of the invention
Embodiment 1
As it is shown in figure 1, a kind of bodied ferric sulfate processes the device of copper industry waste water, including reactor 1 and the agitating device being arranged in described reactor 1;Described agitating device includes hollow shaft 2 and two the hollow stirring paddles 3 being arranged on described hollow shaft 2, described hollow shaft 2 and hollow stirring paddle 3 boring fabric connectivity;On described hollow shaft 2, rotary seal is provided with reinforced set 4, and described reinforced set 4 is provided with the charge door 41 that the hollow-core construction with described hollow shaft 2 connects;
Being provided with some inlets 5 on described hollow shaft 2 and hollow stirring paddle 3, described in reactor 1 bottom up, the bore of inlet 5 is gradually increased;Described reactor 1 top is provided with dosing mouth 11;Being provided with outlet 12 on described reactor 1 sidewall, the described outlet 12 height bottom described reactor 1 is the 1/2 of reactor 1 total height, and described outlet 12 is provided with valve;Described reactor 1 lower sidewall is provided with clean-up port 13, described clean-up port 13 is outside is provided with baffle plate 15, described baffle plate 15 is side walls hinged with described reactor 1, setting is sealed with described reactor 1 sidewall at baffle plate 15 described in course of reaction, described outlet 12 is positioned at above described clean-up port 13, it is provided with discharge outlet 14 bottom described reactor 1, in described discharge outlet 14, is provided with filter membrane 8.It is provided with pH on-line measuring device 6 in described reactor 1.
Specifically, described hollow stirring paddle 3 quantity is two, and two described hollow stirring paddles 3 are arranged on the differing heights of hollow shaft 2.Being provided with hollow support rails 7 between two described hollow stirring paddles 3, the hollow-core construction in hollow-core construction hollow stirring paddle 3 described with two in described support bar 7 connects, and described support bar 7 is also equipped with some inlets 5.
Specific works process is as follows, first pass through pH on-line measuring device 6 and detect wastewater pH in reactor 1, and add pH adjusting agent adjustment pH by dosing mouth 11, by pump, polymeric ferrous sulphate solution is passed into by charge door 41 hollow-core construction of hollow shaft 2, hollow stirring paddle 3 and support bar 7, and entered in the waste water within reactor 1 by inlet 5, open stirring to having reacted simultaneously, then turn off reinforced and stirring, and regulate pH and precipitate, after having precipitated, opening outlet 12 valve, namely the water of top clarification discharge;When precipitation reach a certain amount of need clear up time, be first turned on discharge outlet 14, utilize filter membrane 8 by solid-liquid separation, waste water after treatment is discharged through discharge outlet 14, precipitation be trapped within reactor 1, precipitation is cleared up by the baffle plate 15 then opening clean-up port 13.
Should be appreciated that specific embodiment described above is only for explaining this utility model, be not used to limit this utility model.The apparent change extended out by spirit of the present utility model or variation are still among protection domain of the present utility model.
Claims (6)
1. the device of a bodied ferric sulfate process copper industry waste water, it is characterised in that: include reactor (1) and the agitating device being arranged in described reactor (1);Described agitating device includes hollow shaft (2) and the some hollow stirring paddle (3) being arranged on described hollow shaft (2), described hollow shaft (2) and hollow stirring paddle (3) boring fabric connectivity;The upper rotary seal of described hollow shaft (2) is provided with reinforced set (4), and described reinforced set (4) is provided with the charge door (41) that the hollow-core construction with described hollow shaft (2) connects;
Being provided with some inlets (5) on described hollow shaft (2) and hollow stirring paddle (3), described in reactor (1) bottom up, the bore of inlet (5) is gradually increased;Described reactor (1) top is provided with dosing mouth (11);Being provided with outlet (12) on described reactor (1) sidewall, described outlet (12) is provided with valve;Described reactor (1) lower sidewall is provided with clean-up port (13), described clean-up port (13) is outside is provided with baffle plate (15), described baffle plate (15) is side walls hinged with described reactor (1), sealing setting at baffle plate described in course of reaction (15) with described reactor (1) sidewall, described outlet (12) is positioned at top, described clean-up port (13).
2. bodied ferric sulfate according to claim 1 processes the device of copper industry waste water, it is characterised in that: described outlet (12) is apart from height is reactor (1) total height the 1/2 of described reactor (1) bottom.
3. bodied ferric sulfate according to claim 1 processes the device of copper industry waste water, it is characterized in that: described reactor (1) bottom is provided with discharge outlet (14), is provided with filter membrane (8) in described discharge outlet (14).
4. bodied ferric sulfate according to claim 1 processes the device of copper industry waste water, it is characterised in that: it is provided with pH on-line measuring device (6) in described reactor (1).
5. bodied ferric sulfate according to claim 1 processes the device of copper industry waste water, it is characterized in that: described hollow stirring paddle (3) quantity is two, two described hollow stirring paddles (3) are arranged on the differing heights of hollow shaft (2).
6. bodied ferric sulfate according to claim 5 processes the device of copper industry waste water, it is characterized in that: between two described hollow stirring paddles (3), be provided with hollow support rails (7), the hollow-core construction in hollow-core construction hollow stirring paddle (3) described with two in described support bar (7) connects, and described support bar (7) is also equipped with some inlets (5).
Priority Applications (1)
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CN201620175918.4U CN205398191U (en) | 2016-03-08 | 2016-03-08 | Polyferric sulfate handles device of copper industry waste water |
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CN201620175918.4U CN205398191U (en) | 2016-03-08 | 2016-03-08 | Polyferric sulfate handles device of copper industry waste water |
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CN205398191U true CN205398191U (en) | 2016-07-27 |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112209524A (en) * | 2020-12-03 | 2021-01-12 | 芦娜 | Textile sewage treatment equipment |
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2016
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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CN112209524A (en) * | 2020-12-03 | 2021-01-12 | 芦娜 | Textile sewage treatment equipment |
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