CN202610057U - Zero-emission comprehensive electroplating wastewater treatment equipment - Google Patents
Zero-emission comprehensive electroplating wastewater treatment equipment Download PDFInfo
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- CN202610057U CN202610057U CN 201220275425 CN201220275425U CN202610057U CN 202610057 U CN202610057 U CN 202610057U CN 201220275425 CN201220275425 CN 201220275425 CN 201220275425 U CN201220275425 U CN 201220275425U CN 202610057 U CN202610057 U CN 202610057U
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- electroplating wastewater
- water
- processing equipment
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- 238000009713 electroplating Methods 0.000 title claims abstract description 44
- 238000004065 wastewater treatment Methods 0.000 title abstract 8
- 239000002351 wastewater Substances 0.000 claims abstract description 56
- 239000000126 substance Substances 0.000 claims abstract description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 44
- 230000015572 biosynthetic process Effects 0.000 claims description 29
- 238000003786 synthesis reaction Methods 0.000 claims description 29
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 claims description 15
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 12
- 238000001914 filtration Methods 0.000 claims description 9
- 230000001105 regulatory effect Effects 0.000 claims description 8
- 239000006004 Quartz sand Substances 0.000 claims description 6
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 6
- 238000011001 backwashing Methods 0.000 claims description 6
- 238000009287 sand filtration Methods 0.000 claims description 6
- 239000003795 chemical substances by application Substances 0.000 claims description 3
- 238000005189 flocculation Methods 0.000 claims description 3
- 230000016615 flocculation Effects 0.000 claims description 3
- 239000002455 scale inhibitor Substances 0.000 claims description 3
- 238000000034 method Methods 0.000 abstract description 8
- 229910001385 heavy metal Inorganic materials 0.000 abstract description 4
- 239000003440 toxic substance Substances 0.000 abstract description 2
- 239000012528 membrane Substances 0.000 abstract 2
- 230000015556 catabolic process Effects 0.000 abstract 1
- 238000004140 cleaning Methods 0.000 abstract 1
- 238000006731 degradation reaction Methods 0.000 abstract 1
- 231100000614 poison Toxicity 0.000 abstract 1
- 238000000746 purification Methods 0.000 abstract 1
- 239000010865 sewage Substances 0.000 abstract 1
- 239000002699 waste material Substances 0.000 description 4
- 238000007599 discharging Methods 0.000 description 2
- 230000003670 easy-to-clean Effects 0.000 description 2
- 235000014347 soups Nutrition 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 231100000167 toxic agent Toxicity 0.000 description 1
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Abstract
The utility model relates to zero-emission comprehensive electroplating wastewater treatment equipment. Much of heavy metal is non-degradation toxic substances, does not have natural purification capability, and is difficult to remove from the environment once entering the environment. Currently, sewage treatment mostly adopts chemical methods, the chemical methods are adapted to wastewater difficult to treat such as high-concentration, high-salt and the like wastewater and are high in treatment cost, the wastewater cannot reach standard and are discharged, and the chemical methods are not available when the concentration of the wastewater is reduced to a certain limitation. The zero-emission comprehensive electroplating wastewater treatment equipment comprises standard comprehensive electroplating wastewater treatment equipment (1), wherein a wastewater storage pool (2) is connected with the standard comprehensive electroplating wastewater treatment equipment, the standard comprehensive electroplating wastewater treatment equipment is connected with an intermediate pool (3), the intermediate pool is connected with membrane treatment equipment (4), and the membrane treatment equipment is connected with a cleaning pool (5). The zero-emission comprehensive electroplating wastewater treatment equipment is used for electroplating wastewater treatment.
Description
Technical field:
the utility model relates to a kind of zero-emission structural synthesis electroplating wastewater processing equipment.
Background technology:
Mostly
heavy metal is non-degraded type toxic substance, does not possess natural purifying ability, just is difficult to from environment, remove in case get into environment.Chemical method is used in WWT at present mostly; Chemical method uses at unmanageable waste water of waste water such as some high densitys, high salt; Chemical method not only processing cost height but also waste water can't be accomplished qualified discharge through chemical method, just can't continue when waste strength is reduced to certain limit to have used chemical Treatment.
Summary of the invention:
The purpose of
the utility model is to make a kind of zero-emission structural synthesis electroplating wastewater processing equipment; Through film treatment facility, structural synthesis electroplating wastewater processing equipment up to standard etc. electroplating wastewater is handled; Waste water after the processing is far superior to discharging standards, the easy to clean transportation.
Above-mentioned purpose realizes through following technical scheme:
a kind of zero-emission structural synthesis electroplating wastewater processing equipment; Its composition comprises: structural synthesis electroplating wastewater processing equipment up to standard; Waste water storage pond is connected with described structural synthesis electroplating wastewater processing equipment up to standard; Described structural synthesis electroplating wastewater processing equipment up to standard is connected with middle pond, and described middle pond is connected with the film treatment facility, and described film treatment facility is connected with clean water basin.
described zero-emission structural synthesis electroplating wastewater processing equipment; Described structural synthesis electroplating wastewater processing equipment up to standard is formed and comprised: liquidometer is the vacuum primingpump of control automatically; Waste water storage pond is controlled vacuum primingpump automatically through described liquidometer and is connected with reactor drum, and the Teat pipette that the dosing under meter connects connects described reactor drum, and described reactor drum is connected with dashpot; Described dashpot is connected with the press filtration pump of liquidometer control; Described press filtration pump is connected with pressure filter, and described pressure filter is connected with the PH regulating tank, and described PH regulating tank is connected with clean water basin.
described zero-emission structural synthesis electroplating wastewater processing equipment; Described film treatment facility is formed and comprised: former water lift pump, described former water lift pump are connected with described middle pond, raw water box respectively, and the described raw water box that the flocculation agent chemicals feeder connects is connected with raw water pump; Described raw water pump is connected with the quartz sand filtration device; Described quartz sand filtration device is connected with activated charcoal filter, and described activated charcoal filter is connected with 5 μ m accurate filters, and described 5 μ m accurate filters are connected with UF ultrafiltration-3T; Described UF ultrafiltration-3T connects described middle pond, pure water water tank A, backwashing pump respectively; Described backwashing pump is connected with described pure water water tank A, and described pure water water tank A is connected with HPP through the Scale inhibitors chemicals feeder, and described HPP is connected with RO r-o--03T; Described RO r-o--03T is connected with pure water water tank B, and described pure water water tank B is connected with described clean water basin, pure water pump.
Beneficial effect:
1. at first waste water is through structural synthesis electroplating wastewater processing device processes up to standard, and again through the processing of film treatment facility, but 2/3rds waste water complete-reclaiming is in the Electroplating Production water.The pond circulation realized electroplating wastewater zero in the middle of 1/3rd dense water returned.The dense water that recycles regularly (1 year) will give the locality useless admittedly center processing.
2. handle electroplating wastewater through film treatment facility, structural synthesis electroplating wastewater processing equipment up to standard etc.
, and the waste water after the processing is far superior to discharging standards, the easy to clean transportation.
Description of drawings:
accompanying drawing 1 is the structural representation of this product.
accompanying drawing 2 is structural representations of structural synthesis electroplating wastewater processing equipment up to standard in the accompanying drawing 1.
accompanying drawing 3 is structural representations of film treatment facility in the accompanying drawing 1.
Embodiment:
Embodiment 1:
a kind of zero-emission structural synthesis electroplating wastewater processing equipment; Its composition comprises: structural synthesis electroplating wastewater processing equipment 1 up to standard; Waste water storage pond 2 is connected with described structural synthesis electroplating wastewater processing equipment up to standard; Described structural synthesis electroplating wastewater processing equipment up to standard is connected with middle pond 3, and described middle pond is connected with film treatment facility 4, and described film treatment facility is connected with clean water basin 5.
Embodiment 2:
are according to embodiment 1 described zero-emission structural synthesis electroplating wastewater processing equipment; Described structural synthesis electroplating wastewater processing equipment up to standard is formed and comprised: liquidometer is controlled vacuum primingpump 6 automatically; The described liquidometer that passes through in described waste water storage pond is controlled vacuum primingpump automatically and is connected with reactor drum 7, the described reactor drum of Teat pipette 29 connections of dosing under meter 28 connections, and described reactor drum is connected with dashpot 8; Described dashpot is connected with the press filtration pump 9 of liquidometer 12 controls; Described press filtration pump is connected with pressure filter 10, and described pressure filter is connected with PH regulating tank 11, and described PH regulating tank is connected with described clean water basin.
Embodiment 3:
According to embodiment 1 described zero-emission structural synthesis electroplating wastewater processing equipment, described film treatment facility is formed and comprised
: former water lift pump 13, described former water lift pump are connected with described middle pond, raw water box 14 respectively; Described raw water box is connected with raw water pump 16 through flocculation agent chemicals feeder 15, and described raw water pump is connected with quartz sand filtration device 17, and described quartz sand filtration device is connected with activated charcoal filter 18; Described activated charcoal filter is connected with 5 μ m accurate filters 19; Described 5 μ m accurate filters and UF ultrafiltration-3T, piece number: 20 connect, and described UF ultrafiltration-3T connects described middle pond, pure water water tank A respectively; Piece number: 21, backwashing pump 22; Described backwashing pump is connected with described pure water water tank A, and described pure water water tank A is connected described HPP and RO r-o--03T through Scale inhibitors chemicals feeder 23 with HPP 24; Piece number: 25 connect; Described RO r-o--03T and pure water water tank B, piece number: 26 connect, and described pure water water tank B is connected with described clean water basin, pure water pump 27.
Principle of work:
integrative electroplating waste flows into waste water storage pond; Automatically control the start and stop of vacuum primingpump by liquidometer, in vacuum primingpump suction structural synthesis electroplating wastewater processing up to standard Device Host pipeline reactor, the soup for preparing in advance of main frame is controlled through the dosing under meter by Teat pipette simultaneously; Automatically add in the pipeline reactor; Waste water and soup thorough mixing, moment is accomplished chemical reaction, forms the heavy metal precipitation thing.Reacted wastewater flows in the dashpot, by liquidometer control press filtration pump, makes it in high-water work again, and low-water level stops, in order to avoid press filtration pump depletion or dashpot waste water overflow.Waste water carries out solid-liquid separation through press filtration pump suction chamber-type press filter, and with the removal of heavy metal ions in the waste water, the chamber-type press filter water outlet is regulated PH:6.5-8.5 through the PH regulating tank and is disposed to middle pond.The waste residue that produces gives the locality useless admittedly center processing.The water of intermediate pool is got in the film treatment facility by water pump lifting and handles, and the water that accounts for Total Water 2/3rds after the processing can be back to but water of electroplating rinse water or cold circulation, pond circulation in the middle of all the other dense water that account for Total Water 1/3rd return.Be that integrative electroplating waste is handled the realization zero release.
Claims (3)
1. zero-emission structural synthesis electroplating wastewater processing equipment; Its composition comprises: structural synthesis electroplating wastewater processing equipment up to standard; It is characterized in that: waste water storage pond is connected with described structural synthesis electroplating wastewater processing equipment up to standard; Described structural synthesis electroplating wastewater processing equipment up to standard is connected with middle pond, and described middle pond is connected with the film treatment facility, and described film treatment facility is connected with clean water basin.
2. zero-emission structural synthesis electroplating wastewater processing equipment according to claim 1; It is characterized in that: described structural synthesis electroplating wastewater processing equipment up to standard is formed and comprised: liquidometer is the vacuum primingpump of control automatically; Waste water storage pond is controlled vacuum primingpump automatically through described liquidometer and is connected with reactor drum, and the Teat pipette that the dosing under meter connects connects described reactor drum, and described reactor drum is connected with dashpot; Described dashpot is connected with the press filtration pump of liquidometer control; Described press filtration pump is connected with pressure filter, and described pressure filter is connected with the PH regulating tank, and described PH regulating tank is connected with clean water basin.
3. zero-emission structural synthesis electroplating wastewater processing equipment according to claim 1 and 2; It is characterized in that: described film treatment facility is formed and comprised: former water lift pump, described former water lift pump are connected with described middle pond, raw water box respectively, and the described raw water box that the flocculation agent chemicals feeder connects is connected with raw water pump; Described raw water pump is connected with the quartz sand filtration device; Described quartz sand filtration device is connected with activated charcoal filter, and described activated charcoal filter is connected with 5 μ m accurate filters, and described 5 μ m accurate filters are connected with UF ultrafiltration-3T; Described UF ultrafiltration-3T connects described middle pond, pure water water tank A, backwashing pump respectively; Described backwashing pump is connected with described pure water water tank A, and described pure water water tank A is connected with HPP through the Scale inhibitors chemicals feeder, and described HPP is connected with RO r-o--03T; Described RO r-o--03T is connected with pure water water tank B, and described pure water water tank B is connected with described clean water basin, pure water pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220275425 CN202610057U (en) | 2012-06-12 | 2012-06-12 | Zero-emission comprehensive electroplating wastewater treatment equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220275425 CN202610057U (en) | 2012-06-12 | 2012-06-12 | Zero-emission comprehensive electroplating wastewater treatment equipment |
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| Publication Number | Publication Date |
|---|---|
| CN202610057U true CN202610057U (en) | 2012-12-19 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220275425 Expired - Fee Related CN202610057U (en) | 2012-06-12 | 2012-06-12 | Zero-emission comprehensive electroplating wastewater treatment equipment |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104098198A (en) * | 2014-07-14 | 2014-10-15 | 甘肃锦世化工有限责任公司 | Method for treating heavy metal chromium in industrial exterior drainage water to achieve emission on standard |
| CN105347539A (en) * | 2015-12-15 | 2016-02-24 | 苏州依斯倍环保装备科技有限公司 | Integrated and automatic device for recycling water in industrial wastewater |
-
2012
- 2012-06-12 CN CN 201220275425 patent/CN202610057U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104098198A (en) * | 2014-07-14 | 2014-10-15 | 甘肃锦世化工有限责任公司 | Method for treating heavy metal chromium in industrial exterior drainage water to achieve emission on standard |
| CN104098198B (en) * | 2014-07-14 | 2016-05-18 | 甘肃锦世化工有限责任公司 | A kind of method of processing the outer draining heavy metal chromium qualified discharge of industry |
| CN105347539A (en) * | 2015-12-15 | 2016-02-24 | 苏州依斯倍环保装备科技有限公司 | Integrated and automatic device for recycling water in industrial wastewater |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Free format text: FORMER OWNER: ZHAO XIAOLIN LI ZHAOQUAN Effective date: 20130222 Owner name: HARBIN XIANFENG ENVIRONMENT PROTECTION EQUIPMENT M Free format text: FORMER OWNER: SUN YEJUN Effective date: 20130222 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 150000 HARBIN, HEILONGJIANG PROVINCE TO: 150086 HARBIN, HEILONGJIANG PROVINCE |
|
| TR01 | Transfer of patent right |
Effective date of registration: 20130222 Address after: 150086 No. 430, Xuefu Road, Power District, Heilongjiang, Harbin Patentee after: Harbin Xianfeng environmental protection equipment manufacturing Co., Ltd. Address before: 301, room 3, unit 53, Xuan Xi community, the Yellow River Road, Nangang District, Heilongjiang, Harbin, 150000 Patentee before: Sun Yejun Patentee before: Zhao Xiaolin Patentee before: Li Zhaoquan |
|
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20121219 Termination date: 20180612 |