CN205241845U - Electroplating effluent recycle device - Google Patents
Electroplating effluent recycle device Download PDFInfo
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- CN205241845U CN205241845U CN201520868816.6U CN201520868816U CN205241845U CN 205241845 U CN205241845 U CN 205241845U CN 201520868816 U CN201520868816 U CN 201520868816U CN 205241845 U CN205241845 U CN 205241845U
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- reverse osmosis
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Abstract
The utility model discloses an electroplating effluent recycle device, including the plating bath, electroplate the potcher, electroplating effluent collects the water tank, provided is a high pressure pum, the reverse osmosis membrane device, specific conductivity detection device and pipeline, electroplate the potcher, electroplating effluent collects the water tank, high -pressure pump and reverse osmosis membrane device connect gradually through the pipeline, the waste water of electroplating the potcher carries out hydrone permeation separation through the conduit flow to the reverse osmosis membrane device, pure water after the infiltration of reverse osmosis membrane device flows back to the electroplating potcher through the pipeline, high concentration containing metal concentrate after the infiltration flows back to the plating bath through the pipeline. The utility model discloses simple structure is practical, and the electroplating effluent that the process was handled is divided into two (being divided into pure water and high concentration containing metal concentrate), and pure water time production line is as rinsing water, and high concentration metallic solution telegram in reply coating bath continues the use. Whole process is not discharged, and metal, water all obtain recycle.
Description
Technical field
The utility model relates to electroplating waste water treatment technology field, particularly relates to a kind of electroplating wastewater recycle device.
Background technology
Electroplating industry waste water has that the water yield is large, complicated component, environmental pollution are serious, noble metal and the feature such as heavy metal is many, the domestic improvement to such waste water at present, generally adopt general materialization treatment process processing, simultaneously adopt not up to standard be back to accident pool continue process after meeting environmental requirement, discharge. but there is following defect in the method: the one, and in materialization processing procedure, need to add a large amount of medicaments, and then produce a large amount of materialized muds, environment is caused to secondary pollution, the 2nd, a large amount of noble metals in electroplating wastewater and heavy metal can not get recycling, and have both caused environmental pollution, have again the shortcoming of waste. for the problems referred to above, people are studied again exploitation, obtain the technological means that ion exchange resin is combined with electrolysis tech, can better process electroplating wastewater, reclaim heavy metal wherein simultaneously, but in real operation, neither one normative reference, operator often processes according to the experience of oneself, be placed in the examination criteria that whether fully do not have of processing, and, metal in waste water can not be fully effective recycling, electroplating wastewater processing bad, pollute on the one hand environment, on the other hand, waste the energy, can not fully accomplish the requirement of energy-conserving and environment-protective.
Utility model content
The purpose of this utility model is to provide a kind of electroplating wastewater recycle device, realizes the zero-emission of electroplating wastewater, reduces the waste of the energy.
The technical solution of the utility model is as follows: a kind of electroplating wastewater retracting device, comprise electroplating bath, electroplate rinsing groove, electroplating wastewater is collected water tank, high-pressure pump, reverse osmosis membrane apparatus, water conductivity checkout gear and pipeline, electroplate rinsing groove, electroplating wastewater is collected water tank, high-pressure pump and reverse osmosis membrane apparatus connect successively by pipeline, the waste water of electroplate rinsing groove carries out hydrone permeability and separation by pipeline flow-direction reverse osmosis membrane apparatus, pure water after reverse osmosis membrane apparatus infiltration flows back to electroplate rinsing groove by pipeline, high concentration containing metal concentrate after infiltration flows back to electroplating bath by pipeline.
Described reverse osmosis membrane apparatus comprises a square casing, and box house is provided with the semi-transparent rete that can only see through hydrone, and casing is separated to form the first cavity and the second cavity by described semi-transparent rete.
Described the first cavity is provided with water inlet, and described water inlet connects high-pressure pump by pipeline, and described the first cavity is also provided with liquid outlet, and described liquid outlet connects electroplating bath by pipeline; Described the second cavity is provided with delivery port, and described delivery port connects electroplate rinsing groove by pipeline.
Described the first cavity inside is also provided with propeller.
Described the second cavity inside is also provided with water conductivity checkout gear.
The beneficial effects of the utility model: the utility model is simple and practical, treated electroplating wastewater is divided into two (being divided into pure water and high concentration containing metal concentrate), and pure water returns production line as rinse water, and high concentration metallic solution telegram in reply coating bath continues to use. Whole process is not discharged, and metallic solution, water are all recycled utilization.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
Fig. 2 is the structural representation of reverse osmosis membrane apparatus in the utility model.
Detailed description of the invention
For making the purpose of this utility model, technical scheme and advantage clearer, clear and definite, referring to the accompanying drawing embodiment that develops simultaneously, the utility model is further described.
The utility model discloses a kind of electroplating wastewater recycle device, as Fig. 1, shown in 2, comprise electroplating bath 100, electroplate rinsing groove 200, electroplating wastewater is collected water tank 300, high-pressure pump 400, reverse osmosis membrane apparatus 500, water conductivity checkout gear 550 and pipeline 600, described electroplate rinsing groove 200, electroplating wastewater is collected water tank 300, high-pressure pump 400 and reverse osmosis membrane apparatus 500 connect successively by pipeline 600, the waste water of electroplate rinsing groove 200 flows to reverse osmosis membrane apparatus 500 by pipeline 600 and carries out hydrone permeability and separation, pure water after reverse osmosis membrane apparatus 500 infiltrations flows back to electroplate rinsing groove 200 by pipeline 600, high concentration containing metal concentrate after infiltration flows back to electroplating bath 100 by pipeline 600.
In practical application, in order to facilitate the processing in electroplating wastewater, reverse osmosis membrane apparatus 500 comprises a square casing, and box house is provided with the semi-transparent rete 580 that can only see through hydrone, and casing is separated to form the first cavity 520 and the second cavity 530 by semi-transparent rete 580. The first cavity 520 is provided with water inlet 560, and water inlet 560 connects high-pressure pump 400, the first cavitys 520 by pipeline 600 and is also provided with liquid outlet 570, and liquid outlet 570 connects electroplating bath 100 by pipeline 600; The second cavity 530 is provided with delivery port 540, and delivery port 540 connects electroplate rinsing groove 200 by pipeline 600.
In practical application, in order to reach the object of counter-infiltration, in the first cavity 520, be provided with a propeller 510 for pressurization downwards, to electroplating wastewater pressurization, make the hydrone in electroplating wastewater enter the second cavity 530 through pellicle 580.
In practical application, in order to check purity and the monitoring reverse osmosis unit 500 through the water of pellicle 580, in the second cavity 530, be provided with water conductivity checkout gear 550.
The course of work of the present utility model is as follows: the plating element (not drawing in figure) after electroplating bath 100 has been electroplated, move on in electroplate rinsing groove 200 and carry out rinsing with pure water, the electroplating wastewater that rinsing produces is flowed in electroplating wastewater collection water tank 300 and is collected by pipeline 600. high-pressure pump 400 is worked, by pipeline 600, the electroplating wastewater of collection is pumped to in the first cavity 520 in reverse osmosis membrane apparatus 500, (water inlet 560 of the first cavity is now opened, liquid outlet 570 is closed), in the time that the electroplating wastewater in the first cavity 520 reaches certain amount, close the water inlet 560 of high-pressure pump 400 and the first cavity 520, then reverse osmosis membrane apparatus 500 is started working, propeller 510 in the first cavity 520 is exerted pressure to the electroplating wastewater liquid level in chamber downwards, under the ordering about of pressure, hydrone in electroplating wastewater sees through pellicle 580 and enters the second cavity 530 that pure water is housed, because angle of rake pressure is greater than the osmotic pressure of two empty intracavity liquids, therefore hydrone can not see through pellicle 580 from the second cavity 530 along the direction of osmotic pressure and enter the first cavity 520, having realized effective counter-infiltration is divided into two (being divided into pure water and metallic concentrate) electroplating wastewater, pure water is by the delivery port 540 of the second cavity 530, along with pipeline 600 flows back to electroplate rinsing groove 200, metallic concentrate flows back to electroplating bath 100 by the liquid outlet 570 of the first cavity 520 to be reused, make so whole process not discharge, the concentrated solution of metal and water are all recycled utilization. and be arranged on the water conductivity checkout gear 550 in the second cavity 530, moment is detected pure electrical conductivity of water, rinsing water has quality requirement, the purer electricity of purity of water is led lower, meanwhile, once pure electrical conductivity of water becomes greatly suddenly, this just illustrates that reverse osmosis unit goes wrong, so conductivity detector 550 also plays the effect of monitoring reverse osmosis unit 500 in playing the effect of detection pure water water quality.
Should be understood that; application of the present utility model is not limited to above-mentioned giving an example; for those of ordinary skills, can be improved according to the above description or convert, all these improvement and conversion all should belong to the protection domain of the utility model claims.
Claims (3)
1. an electroplating wastewater recycle device, it is characterized in that, comprise electroplating bath, electroplate rinsing groove, electroplating wastewater is collected water tank, high-pressure pump, reverse osmosis membrane apparatus, water conductivity checkout gear and pipeline, described electroplate rinsing groove, electroplating wastewater is collected water tank, high-pressure pump and reverse osmosis membrane apparatus connect successively by pipeline, the waste water of electroplate rinsing groove carries out hydrone permeability and separation by pipeline flow-direction reverse osmosis membrane apparatus, pure water after reverse osmosis membrane apparatus infiltration flows back to electroplate rinsing groove by pipeline, high concentration containing metal concentrate after infiltration flows back to electroplating bath by pipeline,
Described reverse osmosis membrane apparatus comprises a square casing, and box house is provided with the semi-transparent rete that can only see through hydrone, and casing is separated to form the first cavity and the second cavity by described semi-transparent rete;
Described the first cavity inside is also provided with propeller.
2. electroplating wastewater recycle device according to claim 1, it is characterized in that, described the first cavity is provided with water inlet, and described water inlet connects high-pressure pump by pipeline, described the first cavity is also provided with liquid outlet, and described liquid outlet connects electroplating bath by pipeline; Described the second cavity is provided with delivery port, and described delivery port connects electroplate rinsing groove by pipeline.
3. electroplating wastewater recycle device according to claim 2, is characterized in that, described the second cavity inside is also provided with water conductivity checkout gear.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520868816.6U CN205241845U (en) | 2015-11-04 | 2015-11-04 | Electroplating effluent recycle device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520868816.6U CN205241845U (en) | 2015-11-04 | 2015-11-04 | Electroplating effluent recycle device |
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| Publication Number | Publication Date |
|---|---|
| CN205241845U true CN205241845U (en) | 2016-05-18 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201520868816.6U Active CN205241845U (en) | 2015-11-04 | 2015-11-04 | Electroplating effluent recycle device |
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| CN (1) | CN205241845U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108793463A (en) * | 2018-06-12 | 2018-11-13 | 合肥丰洁生物科技有限公司 | A kind of electroplating wastewater film condensing device |
| CN117574296A (en) * | 2023-11-23 | 2024-02-20 | 清远市信和实业有限公司 | Plating bath liquid flow distribution detection system and method thereof |
-
2015
- 2015-11-04 CN CN201520868816.6U patent/CN205241845U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108793463A (en) * | 2018-06-12 | 2018-11-13 | 合肥丰洁生物科技有限公司 | A kind of electroplating wastewater film condensing device |
| CN117574296A (en) * | 2023-11-23 | 2024-02-20 | 清远市信和实业有限公司 | Plating bath liquid flow distribution detection system and method thereof |
| CN117574296B (en) * | 2023-11-23 | 2024-04-23 | 清远市信和实业有限公司 | Plating bath liquid flow distribution detection system and method thereof |
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