CN205328786U - Pit water separation processor - Google Patents
Pit water separation processor Download PDFInfo
- Publication number
- CN205328786U CN205328786U CN201620006171.XU CN201620006171U CN205328786U CN 205328786 U CN205328786 U CN 205328786U CN 201620006171 U CN201620006171 U CN 201620006171U CN 205328786 U CN205328786 U CN 205328786U
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- water separation
- separation processor
- tank
- jar
- coagulating sedimentation
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Abstract
The utility model provides a pit water separation processor, the pressure atomizing device comprises a water inlet pipe, advance water piping connection to coagulating sedimentation jar, and coagulating sedimentation jar, filter the jar, the chemical reaction jar, the evaporation crystallizer communicates in proper order, this evaporation crystallizer reconnection outlet pipe, wherein, coagulating sedimentation jar upper end is equipped with the drain hole, the lower extreme is equipped with the evacuation pipe, be equipped with the filter layer in the filtration jar, chemical reaction jar upper end is equipped with the feed inlet, the lower extreme is equipped with the discharge opening, the inside heater that is equipped with of evaporation crystallizer, the lower end of the stocker is provided with a discharging cylinder, abandonment water passes through the inlet tube and gets into the coagulating sedimentation jar, add the formation of medicament promotion flocculating constituent, the stirring post -precipitation, the precipitate is through the play of the evacuation bank of tubes, upper strata waste water gets into and filters the jar, filter impurity, the waste liquid gets into the chemical reaction jar, add the chemicals neutralization, the part result draws off through the discharge opening, liquid gets into the evaporation crystallizer, the evaporation crystallization, after the crystal is discharged, liquid behind the separation processing is discharged by the outlet pipe, therefore, the utility model discloses simple structure, effective whole treatment effeciency of abandonment water that improves.
Description
Technical field
This utility model relates to the technical field of wastewater treatment, particularly relates to a kind of mine water separation processor。
Background technology
In order to environmental protection needs, no matter discharge or the mining water of reuse, it is required for through going purified treatment in various degree, treatment technology conventional at present mainly has precipitation, coagulating sedimentation, precipitation to filter, the modes such as shunting, chemical method of removing contamination, but the equipment supporting with these modes is reaching to have in intended theoretical value bigger error, each mode all only has good effect on a kind of direction of process, when processing different material at the same time, such as float, acid solution etc., the effect of these modes is poor, and the equipment adopted is also excessively complicated, relatively costly, complicated operation。
For this, designer of the present utility model is because drawbacks described above, and by concentrating on studies and designing, comprehensive experience and the achievement being engaged in related industry for a long time for many years, research design goes out a kind of mine water separation processor, to overcome drawbacks described above。
Utility model content
The purpose of this utility model is in that to provide a kind of mine water separation processor, and its simple in construction is easy to operate, can efficiently separate process mine waste water。
For solving the problems referred to above, the utility model discloses a kind of mine water separation processor, including water inlet pipe and outlet pipe, it is characterised in that:
Separating treatment assembly it is provided with between described water inlet pipe and outlet pipe, described separating treatment assembly comprises the coagulating sedimentation tank, filtering tank, chemical reaction pot and the evaporative crystallization tank that are sequentially communicated, described water inlet pipe connects coagulating sedimentation tank, and described outlet pipe is connected to evaporative crystallization tank。
Wherein: docking successively respectively through pipe flange between described coagulating sedimentation tank, filtering tank, chemical reaction pot, evaporative crystallization tank, each pipe flange is equipped with an overflow valve。
Wherein: be equipped with a NF membrane at each pipe flange joint。
Wherein: being provided with agitator in described coagulating sedimentation tank, the upper end of described coagulating sedimentation tank is provided with drain hole, and lower end is provided with evacuated tube。
Wherein: described agitator comprises driver element, shaft and stirring vane, described driver element is connected to shaft to realize Stirring, and the periphery of described shaft is provided with at least one stirring vane。
Wherein: dismountable in described filtering tank at least one filter course is installed。
Wherein: described filter course is multilamellar, and multiple layers of filters set gradually from big to little filter densities。
Wherein: the upper end of described chemical reaction pot is provided with charging aperture, and lower end is provided with discharge port。
Wherein: being provided with heater inside described evaporative crystallization tank, lower end is provided with discharging opening。
Wherein: described heater is electric heater, and the tank body of described evaporative crystallization tank be additionally provided with vacuum heat-insulating layer or asbestos heat-insulation layer。
By said structure it can be seen that mine water separation processor of the present utility model has the effect that
1, simple in construction, easy to operate, less costly；
2, waste water is easily separated process by the mode being layered by it, and realizes processing the recyclable recycling of thing, improves waste water overall treatment efficiency。
Detailed content of the present utility model can be obtained by explanation described later and institute's accompanying drawing。
Accompanying drawing explanation
Fig. 1 shows the structural representation of mine water separation processor of the present utility model。
Accompanying drawing labelling:
1 is water inlet pipe；2 is coagulating sedimentation tank；3 is filtering tank；4 is chemical reaction pot；5 is evaporative crystallization tank；6 is outlet pipe；7 is drain hole；8 is evacuated tube；9 is charging aperture；10 is discharge port；11 is heater；12 is discharging opening；13 is pipe flange；14 is overflow valve；15 is NF membrane；16 is agitator。
Detailed description of the invention
Referring to Fig. 1, it is shown that mine water separation processor of the present utility model。
Described mine water separation processor includes water inlet pipe 1 and outlet pipe 6, it is provided with separating treatment assembly between described water inlet pipe 1 and outlet pipe 6, described separating treatment assembly comprises the coagulating sedimentation tank 2, filtering tank 3, chemical reaction pot 4 and the evaporative crystallization tank 5 that are sequentially communicated, described water inlet pipe 1 connects coagulating sedimentation tank 2, and described outlet pipe 6 is connected to evaporative crystallization tank 5。
Docking successively respectively through pipe flange 13 between described coagulating sedimentation tank 2, filtering tank 3, chemical reaction pot 4, evaporative crystallization tank 5, each pipe flange 13 all can be provided with an overflow valve 14, all can be provided with a NF membrane 15 at each pipe flange 13 joint。
Wherein, it is provided with agitator 16 in described coagulating sedimentation tank 2, described agitator 16 can comprise driver element, shaft and stirring vane, described driver element is connected to shaft to realize Stirring, the periphery of described shaft is provided with at least one stirring vane, the upper end of described coagulating sedimentation tank 2 is provided with drain hole 7, lower end is provided with evacuated tube 8, thus, when liquid enters coagulating sedimentation tank 2, agitator 16 can be passed through be sufficiently stirred for, put into suitable coagulated agent by drain hole 7, to carry out sufficient coagulating sedimentation in whipping process simultaneously。
It is provided with at least one filter course in described filtering tank 3, the liquid flow through is filtered by described filter course, wherein, described filter course can be multilamellar, and multiple layers of filters sets gradually from big to little filter densities, to carry out layered filtration, and described filter course is detachable be installed in filtering tank 3, to facilitate taking-up cleaning。
The upper end of described chemical reaction pot 4 is provided with charging aperture 9, and lower end is provided with discharge port 10, to realize liquid carries out the operation such as chemical reaction, neutralization。
Described evaporative crystallization tank 5 is internal is provided with heater 11, and lower end is provided with discharging opening 12, and described heater can be electric heater, and the tank body of described evaporative crystallization tank 5 also can be provided with heat-insulation layer, and described heat-insulation layer can be vacuum heat-insulating layer or asbestos heat-insulation layer。
In specific works, operation principle of the present utility model is:
Waste water enters coagulating sedimentation tank 2 by water inlet pipe 1, add medicament by drain hole 7 to coagulating sedimentation tank 2 and promote the formation of floccule body, postprecipitation is stirred through agitator 16, precipitate is discharged through evacuated tube 8, upper strata waste water enters filtering tank 3, after filtering and the impurity of precipitation cohesion tentatively filtered, waste liquid enters chemical reaction pot 4, add chemicals from charging aperture 9 and pH value, portion of product draws off through discharge port 10, liquid enters evaporative crystallization tank 5, heater 11 heating evaporation crystallization, crystal is after discharging opening 12 is discharged, final liquid is discharged by outlet pipe 6, wherein each tank body junction is filtered through row by NF membrane 15, and by overflow valve 14 coutroi velocity。
As can be seen here, the utility model has the advantage of:
1, simple in construction, easy to operate, less costly；
2, waste water is easily separated process by the mode being layered by it, and realizes processing the recyclable recycling of thing, improves waste water overall treatment efficiency。
It is readily apparent that above description and record are only illustrate rather than in order to limit disclosure of the present utility model, application or use。Although describing in an embodiment and being described in the drawings embodiment, but this utility model be not intended to by accompanying drawing example and be described as in an embodiment it is now recognized that optimal mode to implement the specific examples of instruction of the present utility model, scope of the present utility model will include any embodiment falling into description and appended claims above。
Claims (10)
1. a mine water separation processor, including water inlet pipe and outlet pipe, it is characterised in that:
Separating treatment assembly it is provided with between described water inlet pipe and outlet pipe, described separating treatment assembly comprises the coagulating sedimentation tank, filtering tank, chemical reaction pot and the evaporative crystallization tank that are sequentially communicated, described water inlet pipe connects coagulating sedimentation tank, and described outlet pipe is connected to evaporative crystallization tank。
2. mine water separation processor as claimed in claim 1, it is characterised in that: docking successively respectively through pipe flange between described coagulating sedimentation tank, filtering tank, chemical reaction pot, evaporative crystallization tank, each pipe flange is equipped with an overflow valve。
3. mine water separation processor as claimed in claim 2, it is characterised in that: it is equipped with a NF membrane at each pipe flange joint。
4. the mine water separation processor as described in arbitrary in claim 1-3, it is characterised in that: being provided with agitator in described coagulating sedimentation tank, the upper end of described coagulating sedimentation tank is provided with drain hole, and lower end is provided with evacuated tube。
5. mine water separation processor as claimed in claim 4, it is characterized in that: described agitator comprises driver element, shaft and stirring vane, described driver element is connected to shaft to realize Stirring, and the periphery of described shaft is provided with at least one stirring vane。
6. the mine water separation processor as described in arbitrary in claim 1-3, it is characterised in that: dismountable in described filtering tank at least one filter course is installed。
7. mine water separation processor as claimed in claim 6, it is characterised in that: described filter course is multilamellar, and multiple layers of filters sets gradually from big to little filter densities。
8. the mine water separation processor as described in arbitrary in claim 1-3, it is characterised in that: the upper end of described chemical reaction pot is provided with charging aperture, and lower end is provided with discharge port。
9. the mine water separation processor as described in arbitrary in claim 1-3, it is characterised in that: being provided with heater inside described evaporative crystallization tank, lower end is provided with discharging opening。
10. mine water separation processor as claimed in claim 9, it is characterised in that: described heater is electric heater, and the tank body of described evaporative crystallization tank is additionally provided with vacuum heat-insulating layer or asbestos heat-insulation layer。
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620006171.XU CN205328786U (en) | 2016-01-04 | 2016-01-04 | Pit water separation processor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620006171.XU CN205328786U (en) | 2016-01-04 | 2016-01-04 | Pit water separation processor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205328786U true CN205328786U (en) | 2016-06-22 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620006171.XU Active CN205328786U (en) | 2016-01-04 | 2016-01-04 | Pit water separation processor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205328786U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110078283A (en) * | 2019-04-24 | 2019-08-02 | 中国神华能源股份有限公司 | Saliferous equipment for treating water from mine |
| CN112321049A (en) * | 2020-10-22 | 2021-02-05 | 河北工程大学 | Underground mine water treatment device for coal mine |
-
2016
- 2016-01-04 CN CN201620006171.XU patent/CN205328786U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110078283A (en) * | 2019-04-24 | 2019-08-02 | 中国神华能源股份有限公司 | Saliferous equipment for treating water from mine |
| CN112321049A (en) * | 2020-10-22 | 2021-02-05 | 河北工程大学 | Underground mine water treatment device for coal mine |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |