CN210505892U - Catalytic device for accelerating oxidation of lead-zinc beneficiation wastewater - Google Patents
Catalytic device for accelerating oxidation of lead-zinc beneficiation wastewater Download PDFInfo
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- CN210505892U CN210505892U CN201921263506.6U CN201921263506U CN210505892U CN 210505892 U CN210505892 U CN 210505892U CN 201921263506 U CN201921263506 U CN 201921263506U CN 210505892 U CN210505892 U CN 210505892U
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Abstract
The utility model discloses a catalytic unit that is used for lead zinc ore dressing waste water oxidation with higher speed relates to ore dressing waste water recycle field, the device comprises a device main part, the device main part is including stirring the cabin and filtering the cabin, the motor is installed at the top in stirring the cabin, the output of motor is provided with the cylinder, the both sides of cylinder evenly are provided with the multiunit (mixing) shaft, one side at stirring cabin top is provided with the water inlet, one side of device main part is provided with the connecting pipe, the one end of connecting pipe runs through to the inside in stirring the cabin. The utility model discloses a (mixing) shaft of the cylinder and the cylinder both sides that set up can make lead zinc ore dressing waste water and the iron carbon filler in the cylinder carry out abundant reaction, and then make lead zinc ore dressing waste water can generate the precipitate, and the precipitate subsides in the bottom of stirred tank, and the waste water after the processing passes through the active carbon filter screen along the connecting pipe, and the active carbon can adsorb the heavy metal ion in the waste water, and the water pump can be with the water after handling in the water tank of taking out.
Description
Technical Field
The utility model relates to a beneficiation wastewater recycle field specifically is a catalytic unit that is used for lead zinc beneficiation wastewater to accelerate oxidation.
Background
The lead-zinc beneficiation wastewater comprises lead-zinc beneficiation process drainage, tailing pond overflow water and mine field drainage. The lead and zinc beneficiation process drainage is generally conveyed to a tailing pond together with tailing slurry, and is collectively called tailing water. The beneficiation wastewater treatment is also called tailing water treatment, and a catalytic device for accelerating the oxidation of the lead-zinc beneficiation wastewater is needed for treating the lead-zinc beneficiation wastewater.
However, the existing catalytic device has poor treatment effect on lead-zinc beneficiation wastewater, causes serious influence on human beings and the environment after being discharged, cannot treat precipitates after oxidation of the lead-zinc beneficiation wastewater, also can remain moisture in the precipitates, can waste resources by direct discharge, can pollute the environment and reduce the working efficiency.
SUMMERY OF THE UTILITY MODEL
The utility model aims to provide a: in order to solve the problems that the treatment effect of the conventional catalytic device on the lead-zinc beneficiation wastewater is poor, the discharged lead-zinc beneficiation wastewater has serious influence on human beings and the environment, and the conventional catalytic device cannot dry the residual precipitate after the lead-zinc beneficiation wastewater, so that the resources are wasted, and the working efficiency is reduced, the catalytic device for the accelerated oxidation of the lead-zinc beneficiation wastewater is provided.
In order to achieve the above object, the utility model provides a following technical scheme: a catalytic device for accelerating oxidation of lead-zinc beneficiation wastewater comprises a device main body, wherein the device main body comprises a stirring cabin and a filtering cabin, a motor is installed at the top of the stirring cabin, a roller is arranged at the output end of the motor, a plurality of groups of stirring shafts are uniformly arranged on two sides of the roller, a water inlet is arranged on one side of the top of the stirring cabin, a connecting pipe is arranged on one side of the device main body, one end of the connecting pipe penetrates into the stirring cabin, the other end of the connecting pipe penetrates into the filtering cabin, a sludge suction pump is installed on one side of the device main body, away from the connecting pipe, a sludge suction pipe penetrating into the stirring cabin is arranged at the sludge suction end of the sludge suction pump, a drying box is arranged on one side of the sludge suction pump, a sludge outlet pipe penetrating into the drying box is arranged at the sludge outlet end of the sludge suction pump, and a heater, the inside in filtration cabin is provided with the active carbon filter screen, device main part one side is provided with the water tank, the water tank leads to pipe and is connected with the filtration cabin, the water pump is installed to the centre of water pipe.
Preferably, a door is hinge-connected to one side of the device body.
Preferably, one end of the connecting pipe is provided with a filter cloth.
Preferably, the top ends of the connecting pipe, the sludge suction pipe and the water pipe are all provided with valves.
Preferably, the outer wall of the roller is uniformly provided with a plurality of groups of through holes.
Preferably, the outer wall of the drum is provided with a hatch.
Compared with the prior art, the beneficial effects of the utility model are that: the utility model discloses a (mixing) shaft of the cylinder that sets up and cylinder both sides can make lead zinc ore dressing waste water and the iron carbon filler in the cylinder carry out abundant reaction, and then make lead zinc ore dressing waste water can generate the precipitate, the precipitate subsides in the bottom of stirred tank, waste water after the processing passes through the active carbon filter screen along the connecting pipe, the heavy metal ion in the waste water can be adsorbed to the active carbon, make cleaner that waste water can handle, the water pump can be with in the water suction water tank after handling, the suction dredge pump can be with subsiding in the precipitate suction stoving incasement of stirred tank bottom portion simultaneously, the heater can be dried to the precipitate, make the evaporation of water in the precipitate, the last precipitate solid that remains, catalytic efficiency is improved.
Drawings
Fig. 1 is a front view of the present invention;
FIG. 2 is a schematic structural view of the drum of the present invention;
fig. 3 is a schematic structural diagram of the activated carbon filter screen of the present invention.
In the figure: 1. a device main body; 2. a motor; 3. a drum; 4. a stirring shaft; 5. a through hole; 6. a cabin door; 7. a box door; 8. a water inlet; 9. a connecting pipe; 10. a filter cloth; 11. a dredge pump; 12. a drying box; 13. a heater; 14. an active carbon filter screen; 15. a water pump; 16. a water pipe; 17. a water tank; 18. a stirring chamber; 19. a filtration compartment; 20. a mud suction pipe; 21. and (4) a mud outlet pipe.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
The motor (model is YS 80), the water pump (model is G-JET JET pump), the heater (model is QL-KQ-80) and the dredge pump (model is ML 150-16) mentioned in the utility model can be ordered and obtained in the market or private.
Referring to fig. 1-3, a catalytic device for accelerating oxidation of lead-zinc beneficiation wastewater comprises a device main body 1, the device main body 1 comprises a stirring cabin 18 and a filtering cabin 19, a motor 2 is installed at the top of the stirring cabin 18, a roller 3 is arranged at the output end of the motor 2, a plurality of groups of stirring shafts 4 are uniformly arranged on two sides of the roller 3, a water inlet 8 is arranged on one side of the top of the stirring cabin 18, a connecting pipe 9 is arranged on one side of the device main body 1, one end of the connecting pipe 9 penetrates into the stirring cabin 18, the other end of the connecting pipe 9 penetrates into the filtering cabin 19, a sludge suction pump 11 is installed on one side of the device main body 1 away from the connecting pipe 9, a sludge suction pipe 20 penetrating into the stirring cabin 18 is arranged at the sludge suction end of the sludge suction pump 11, a drying box 12 is arranged at one side of the sludge suction pump 11, a sludge outlet pipe 21 penetrating into the, the heater 13 is installed on the top of the inside of the drying box 12, the activated carbon filter screen 14 is arranged inside the filter cabin 19, the water tank 17 is arranged on one side of the device main body 1, the water tank 17 is connected with the filter cabin 19 through the water pipe 16, and the water pump 15 is installed in the middle of the water pipe 16.
The utility model discloses a (mixing) shaft 4 of the 3 both sides of cylinder 3 and cylinder that set up can make lead zinc ore dressing waste water and the iron carbon filler in the cylinder 3 carry out abundant reaction, and then make lead zinc ore dressing waste water can generate the precipitate, the precipitate subsides in the bottom of stirring cabin 18, waste water after the processing is along connecting pipe 9 through activated carbon filter screen 14, the heavy metal ion in the waste water can be adsorbed to the activated carbon, make cleaner that waste water can handle, water pump 15 can be with in the water suction water tank 17 after handling, simultaneously suction dredge pump 11 can be with subsiding in the precipitate suction stoving case 12 of stirring cabin 18 bottom, heater 13 can dry the precipitate, make the evaporation of water in the precipitate, remain the precipitate solid at last, the catalysis efficiency is improved.
Referring to fig. 1, a door 7 is hinge-connected to one side of the apparatus body 1.
This kind of catalytic unit of lead zinc ore dressing waste water accelerated oxidation passes through hinge hinged connection's chamber door 7 for the staff can wash device main part 1 is inside, and collect remaining precipitate in the device main part 1.
Please refer to fig. 1, one end of the connection pipe 9 is provided with a filter cloth 10.
This kind of catalytic unit of lead zinc ore dressing waste water oxidation with higher speed can prevent through the filter cloth 10 that sets up that the precipitate from getting into filtration cabin 19 through connecting pipe 9, prevents that the precipitate from blockking up the inside active carbon filter screen 14 of filtration cabin 19, also prevents simultaneously that the precipitate from polluting the active carbon.
Please refer to fig. 1, the top ends of the connecting pipe 9, the mud sucking pipe 20 and the water pipe 16 are provided with valves.
This kind of catalytic unit of lead zinc ore dressing waste water accelerated oxidation blocks the water and the precipitate in the device main part 1 through the multiunit valve that sets up, and only when the valve was opened, the water and the precipitate after handling could get into corresponding pipeline.
Please refer to fig. 1 and 2, the outer wall of the drum 3 is uniformly provided with a plurality of sets of through holes 5.
This kind of catalytic unit of lead zinc ore dressing waste water oxidation with higher speed makes the iron carbon filler in the cylinder 3 can carry out abundant reaction with lead zinc ore dressing waste water through the multiunit through-hole 5 that sets up for lead zinc ore dressing waste water generation deposits.
Referring to fig. 1 and 2, the outer wall of the drum 3 is provided with a hatch 6.
This kind of catalytic unit of lead zinc ore dressing waste water oxidation with higher speed makes the staff can put in the iron carbon filler to 3 interior cylinders through the hatch door 6 that sets up, also can clear up 3 insides of cylinder simultaneously, prevents that the iron carbon filler from blockking up the through-hole 5 of 3 outer walls of cylinder.
The working principle is as follows: firstly, opening a box door 7 on one side of a stirring cabin 18, then opening a box door 6 on a roller 3, putting iron-carbon filler into the roller 3, then closing the box door 6 and the box door 7, then pouring lead-zinc ore dressing wastewater into the stirring cabin 18, simultaneously adding a coagulant into the lead-zinc ore dressing wastewater, switching on a power supply, starting a motor 2 to rotate, driving the roller 3 to rotate by an output end, enabling the lead-zinc ore dressing wastewater to fully react with the iron-carbon filler and the coagulant in the roller 3, carrying out micro-electrolysis treatment on the lead-zinc ore dressing wastewater by the iron-carbon filler, enabling the lead-zinc ore dressing wastewater to generate precipitates by the coagulant, after reacting for a period of time, closing the motor 2, standing the lead-zinc ore dressing wastewater for a period of time, generating the precipitates at the bottom of the stirring cabin 18, then opening a valve on a connecting pipe 9, and enabling the treated wastewater to flow through, activated carbon can adsorb the heavy metal ion in the waste water, make waste water purified more thoroughly, the standard of emission has been reached, water pump 15 on one side of filter chamber 19 will handle through water pipe 16 in the water suction water tank 17, simultaneously dredge pump 11 inhales the stoving case 12 with the precipitate in the agitator chamber 18 in, filter screen in the stoving case 12 carries out primary filtration to the precipitate earlier, the partly moisture of filtering detach is discharged through the valve of stoving case 12 bottom, then heater 13 dries the precipitate in the stoving case 12, get rid of remaining moisture evaporation in the precipitate, the precipitate after getting rid of moisture has become the solid, it handles more conveniently, the chamber door 7 on one side of agitator chamber 18 makes can change the iron and carbon filler in cylinder 3, also can clear up the inside of agitator chamber 18 simultaneously.
It is obvious to a person skilled in the art that the invention is not restricted to details of the above-described exemplary embodiments, but that it can be implemented in other specific forms without departing from the spirit or essential characteristics of the invention. The present embodiments are therefore to be considered in all respects as illustrative and not restrictive, the scope of the invention being indicated by the appended claims rather than by the foregoing description, and all changes which come within the meaning and range of equivalency of the claims are therefore intended to be embraced therein. Any reference sign in a claim should not be construed as limiting the claim concerned.
Claims (6)
1. The utility model provides a catalytic unit that is used for lead zinc ore dressing waste water to accelerate oxidation, includes device main part (1), its characterized in that: the device comprises a device body (1) and is characterized in that the device body (1) comprises a stirring cabin (18) and a filtering cabin (19), a motor (2) is installed at the top of the stirring cabin (18), a roller (3) is arranged at the output end of the motor (2), multiple groups of stirring shafts (4) are uniformly arranged on two sides of the roller (3), a water inlet (8) is formed in one side of the top of the stirring cabin (18), a connecting pipe (9) is arranged on one side of the device body (1), one end of the connecting pipe (9) penetrates through the stirring cabin (18), the other end of the connecting pipe (9) penetrates through the filtering cabin (19), a mud suction pump (11) is installed on one side, away from the connecting pipe (9), of the device body (1), a mud suction pipe (20) penetrating through the inside of the stirring cabin (18) is arranged at the mud suction end of the mud pump (11), a drying box (12) is arranged on, the mud discharging end of the mud suction pump (11) is provided with a mud discharging pipe (21) penetrating to the inside of the drying box (12), the top end of the inside of the drying box (12) is provided with a heater (13), the inside of the filtering cabin (19) is provided with an activated carbon filtering net (14), one side of the device main body (1) is provided with a water tank (17), the water tank (17) is connected with the filtering cabin (19) through a water pipe (16), and a water pump (15) is installed in the middle of the water pipe (16).
2. The catalytic device for the accelerated oxidation of lead-zinc beneficiation wastewater according to claim 1, characterized in that: one side of the device main body (1) is hinged with a box door (7) through a hinge.
3. The catalytic device for the accelerated oxidation of lead-zinc beneficiation wastewater according to claim 1, characterized in that: one end of the connecting pipe (9) is provided with a filter cloth (10).
4. The catalytic device for the accelerated oxidation of lead-zinc beneficiation wastewater according to claim 1, characterized in that: the top ends of the connecting pipe (9), the sludge suction pipe (20) and the water pipe (16) are all provided with valves.
5. The catalytic device for the accelerated oxidation of lead-zinc beneficiation wastewater according to claim 1, characterized in that: the outer wall of the roller (3) is uniformly provided with a plurality of groups of through holes (5).
6. The catalytic device for the accelerated oxidation of lead-zinc beneficiation wastewater according to claim 1, characterized in that: and a cabin door (6) is arranged on the outer wall of the roller (3).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921263506.6U CN210505892U (en) | 2019-08-06 | 2019-08-06 | Catalytic device for accelerating oxidation of lead-zinc beneficiation wastewater |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921263506.6U CN210505892U (en) | 2019-08-06 | 2019-08-06 | Catalytic device for accelerating oxidation of lead-zinc beneficiation wastewater |
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| CN210505892U true CN210505892U (en) | 2020-05-12 |
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| CN201921263506.6U Active CN210505892U (en) | 2019-08-06 | 2019-08-06 | Catalytic device for accelerating oxidation of lead-zinc beneficiation wastewater |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114988605A (en) * | 2022-06-08 | 2022-09-02 | 江西睿锋环保有限公司 | Tin-lead-zinc multi-metal vulcanization wastewater treatment equipment |
-
2019
- 2019-08-06 CN CN201921263506.6U patent/CN210505892U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114988605A (en) * | 2022-06-08 | 2022-09-02 | 江西睿锋环保有限公司 | Tin-lead-zinc multi-metal vulcanization wastewater treatment equipment |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20200916 Address after: Room 3005 (b), management committee building, No.23 Chuangye Road, industrial transfer industrial park, Zhenjiang District, Shaoguan City, Guangdong Province Patentee after: GUANGDONG ZHONGJIN LINGNAN ENVIRONMENTAL PROTECTION ENGINEERING Co.,Ltd. Address before: 510640 building 3, South China Normal University, Guangzhou University City, Panyu District, Guangzhou City, Guangdong Province Patentee before: SOUTH CHINA NORMAL University |
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| TR01 | Transfer of patent right |