CN201762202U - Electroplating purified water treatment device - Google Patents
Electroplating purified water treatment device Download PDFInfo
- Publication number
- CN201762202U CN201762202U CN2010202800371U CN201020280037U CN201762202U CN 201762202 U CN201762202 U CN 201762202U CN 2010202800371 U CN2010202800371 U CN 2010202800371U CN 201020280037 U CN201020280037 U CN 201020280037U CN 201762202 U CN201762202 U CN 201762202U
- Authority
- CN
- China
- Prior art keywords
- reverse osmosis
- water
- osmosis device
- level
- pump
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Images
Abstract
An electroplating purified water treatment device is mainly characterized by the inclusion of a sand filtering system (3), a carbon filtering system (4), a softening bed (5), a primary microporous filter (6), a medicine feeding machine (7), a primary reverse osmosis device (9), a primary ultrafiltration water tank (10), a secondary reverse osmosis device (11), a secondary microporous filter (14), a medical cleaning pump (15) and a medical cleaning barrel (16). The electroplating purified water treatment device utilizes the sand filtering system, the carbon filtering system, the softening bed, the microporous filters and the reverse osmosis devices together to accomplish the electroplating operation, so that the waste water exhaust treatment is achieved and the quality of purified water is eventually obtained; and the manufacturing cost is effectively saved due to the cycle use of liquid medicine. The electroplating purified water treatment device has the advantages of reasonable structure, reasonable composition, low cost, small occupied land, high purification efficiency, high yield and the like, and is particularly applicable to purified water preparation by utilizing electroplating wastewater.
Description
Technical field
The utility model belongs to industry and electroplates water-treatment technology field, is specifically related to a kind of plating pure water treatment unit.
Background technology
High speed development along with scientific-technical progress and industrial production technology, particularly plating waits improving constantly of industry product quality and state of the art, the demand of electroplating industry water is increasing, no longer be that the minority process procedure uses pure water, the quality requirements of product has needed to change the water of production whole process into pure water from tap water, no longer is fit to the needs that this class is produced so buy the method for the self-control pure water of the mode of commercial pure water and higher cost in the past.Carry out further advanced treatment with electroplate rinsing wastewater through chemical treatment and pretreated water up to standard, the pure water of generation returns plating line once more and uses, and can satisfy the processing requirement of plating line rinsing to pure water.
Summary of the invention
The purpose of this utility model is to provide the plating pure water treatment unit of a kind of simple in structure, system water stay in grade, economy and durability, this electroplates the pure water treatment unit will be through the further advanced treatment of the electroplating wastewater of comprehensive qualified discharge, obtain pure water, satisfy industry, water of productive use demand.
The technical solution of the utility model is:
A kind of plating pure water treatment unit, it is mainly by the sand filtration system, the carbon filtering system, softening bed, the one-level millipore filter, chemicals feeder, the first-stage reverse osmosis device, one-level ultrafiltration water tank, the two-pass reverse osmosis device, the secondary millipore filter, pump washed by medicine and the medicine cask washing is formed, described sand filtration system, the carbon filtering system is connected successively with softening bed, the water outlet of softening bed connects the water-in of one-level millipore filter, the water outlet of one-level millipore filter connects the first-stage reverse osmosis device, the water outlet of first-stage reverse osmosis device connects the two-pass reverse osmosis device by one-level ultrafiltration water tank, be provided with chemicals feeder between one-level millipore filter and the first-stage reverse osmosis device, the discharge of wastewater mouth of first-stage reverse osmosis device connects the medicine cask washing, and the medicine cask washing is washed the water-in that pump is connected the first-stage reverse osmosis device by secondary millipore filter and medicine.
Be provided with the ultrafiltration high-pressure pump before the water-in of described first-stage reverse osmosis device.
The water outlet of described two-pass reverse osmosis device is connected with the pure water case, and the pure water case connects by the pure water topping-up pump uses water spot.
The filter core of described one-level millipore filter is the micron order filter core; The filter core of described secondary millipore filter is the micron order filter core.。
Also comprise reaching drain box and raw water pump, the described water inlet pipe that reaches drain box connects and comprehensively reaches effluent, and the bottom water outlet that reaches drain box connects raw water pump, and raw water pump connects the water-in of described sand filtration system.
The beneficial effects of the utility model are:
Plating pure water treatment unit of the present utility model adopts sand filtration, carbon filter, softening bed, millipore filter and reverse osmosis unit to finish jointly and electroplates the processing that reaches effluent, guarantee finally to obtain the quality of pure water, by to the recycling of soup, effectively save production cost.Of the present utility model rational in infrastructure, form rationally, have advantages such as cost is low, the equipment occupation of land is little, purification efficiency is high, output is big, can be particularly useful for electroplating wastewater and prepare pure water.
Description of drawings
Fig. 1 is an one-piece construction synoptic diagram of the present utility model.
Among the figure: 1 washes pump, 16 for secondary millipore filter, 15 for medicine for pure water topping-up pump, 14 for pure water case, 13 for two-pass reverse osmosis device, 12 for one-level ultrafiltration water tank, 11 for first-stage reverse osmosis device, 10 for ultrafiltration high-pressure pump, 9 for chemicals feeder, 8 for one-level millipore filter, 7 for softening bed, 6 for carbon filtering system, 5 for sand filtration system, 4 for raw water pump, 3 and is the medicine cask washing for reaching drain box, 2.
Embodiment
Below in conjunction with accompanying drawing the utility model is further described:
A kind of plating pure water treatment unit, it is mainly by sand filtration system 3, carbon filtering system 4, softening bed 5, one-level millipore filter 6, chemicals feeder 7, first-stage reverse osmosis device 9, one-level ultrafiltration water tank 10, two-pass reverse osmosis device 11, secondary millipore filter 14, pump 15 washed by medicine and medicine cask washing 16 is formed, described sand filtration system 3, carbon filtering system 4 is connected successively with softening bed 5, the water outlet of softening bed 5 connects the water-in of one-level millipore filter 6, the water outlet of one-level millipore filter 6 connects first-stage reverse osmosis device 9, the water outlet of first-stage reverse osmosis device 9 connects two-pass reverse osmosis device 11 by one-level ultrafiltration water tank 10, be provided with chemicals feeder 7 between one-level millipore filter 6 and the first-stage reverse osmosis device 9, the discharge of wastewater mouth of first-stage reverse osmosis device 9 connects medicine cask washing 16, and medicine cask washing 16 is washed the water-in that pump 15 is connected first-stage reverse osmosis device 9 by secondary millipore filter 14 and medicine.
Be provided with ultrafiltration high-pressure pump 8 before the water-in of first-stage reverse osmosis device 9.
The water outlet of two-pass reverse osmosis device 11 is connected with pure water case 12, and pure water case 12 connects by pure water topping-up pump 13 uses water spot.
The filter core of one-level millipore filter 6 is the micron order filter core; The filter core of described secondary millipore filter 14 is the micron order filter core.
The discharge of wastewater of first-stage reverse osmosis device 9 is to wastewater disposal basin, and the water port of two-pass reverse osmosis device 11 connects one-level intelligence ultrafiltration water tank 10.
Also comprise reaching drain box 1 and raw water pump 2, the described water inlet pipe connection that reaches drain box 1 comprehensively reaches effluent, and the bottom water outlet that reaches drain box 1 connects raw water pump 2, the water-in of the described sand filtration of raw water pump 2 connections system 3.
Basic procedure of the present utility model is that the raw water pump 2 of 0.2～1MPa reaches effluent and sends into sand filtration system 3, carbon filtering system 4, softening bed 5 and one-level millipore filter 6 successively electroplating integrated for the applying pressure scope, and the water after the ultrafiltration high-pressure pump 8 that re-uses pressure range and be 1.2～1.8MPa will be filtered is sent into 9 processing of first-stage reverse osmosis device.Grade one filter 6 of the present utility model is selected the filter core of precision 1um for use, secondary millipore filter 14 is selected the filter core of precision 1 μ m for use, the reverse osmosis membrane RO film significant parameter of first-stage reverse osmosis device 9 is: ph value scope 3-10, the highest working pressure 4mPa, film sees through liquid 1.7T/H, ratio of desalinization 99.6%, service temperature is below 45 ℃.The system that one section treatment process reverse osmosis membrane of RO film one-level constitutes finishes.Wherein, behind the suspended substance in the first coarse filtration water, impurity, the organism, ultra-filtration membrane and the processing of RO film through membrane module 9 at last reaches requirement.Multi-filtering before the RO film mainly is compositions such as the organism, impurity, suspended substance in the filtering water, in order to avoid these materials enter the RO film, result in blockage, pollution and work-ing life shorten etc., particularly ultra-filtration membrane is a kind of porous-film with super " screening " function.Can effectively remove more particulate, colloid, bacterium and macromolecule organic matter in the water, reduce turbidity, water-quality guideline such as COD, TOC, make reverse osmosis membrane obtain more reliable protection.The RO film is selected the CPA3 low pressure composite membrane, and its significant parameter is: ph value scope 3-10, and the highest working pressure 4mPa, film sees through liquid 1.7T/H, ratio of desalinization 99.6%, service temperature is below 45 ℃.Every grade of strainer is all sent into water by topping-up pump, and ultrafiltration applying pressure scope is 0.2～1MPa, and the working barrel of RO film is a high-pressure pump, and the pressure range of high-pressure pump is generally 1～2.5MPa.Originally be that specific conductivity with the novel pure water of making is generally below 10 μ S/cm.
Claims (5)
1. electroplate the pure water treatment unit for one kind, it is characterized in that it is mainly by sand filtration system (3), carbon filtering system (4), softening bed (5), one-level millipore filter (6), chemicals feeder (7), first-stage reverse osmosis device (9), one-level RO water tank (10), two-pass reverse osmosis device (11), secondary millipore filter (14), pump (15) washed by medicine and medicine cask washing (16) is formed, described sand filtration system (3), carbon filtering system (4) is connected successively with softening bed (5), the water outlet of softening bed (5) connects the water-in of one-level millipore filter (6), the water outlet of one-level millipore filter (6) connects first-stage reverse osmosis device (9), the water outlet of first-stage reverse osmosis device (9) connects two-pass reverse osmosis device (11) by one-level RO water tank (10), be provided with chemicals feeder (7) between one-level millipore filter (6) and the first-stage reverse osmosis device (9), the discharge of wastewater mouth of first-stage reverse osmosis device (9) connects medicine cask washing (16), and medicine cask washing (16) is washed the water-in that pump (15) is connected first-stage reverse osmosis device (9) by secondary millipore filter (14) and medicine.
2. plating pure water treatment unit according to claim 1 is characterized in that being provided with one-level RO high-pressure pump (8) before the water-in of described first-stage reverse osmosis device (9).
3. plating pure water treatment unit according to claim 1 is characterized in that the water outlet of described two-pass reverse osmosis device (11) is connected with pure water case (12), and pure water case (12) connects by pure water topping-up pump (13) uses water spot.
4. plating pure water treatment unit according to claim 1, the filter core that it is characterized in that described one-level millipore filter (6) is the micron order filter core; The filter core of described secondary millipore filter (14) is the micron order filter core.
5. plating pure water treatment unit according to claim 1, it is characterized in that also comprising and reach drain box (1) and raw water pump (2), the described water inlet pipe connection that reaches drain box (1) comprehensively reaches effluent, the bottom water outlet that reaches drain box (1) connects raw water pump (2), and raw water pump (2) connects the water-in of described sand filtration system (3).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010202800371U CN201762202U (en) | 2010-08-03 | 2010-08-03 | Electroplating purified water treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010202800371U CN201762202U (en) | 2010-08-03 | 2010-08-03 | Electroplating purified water treatment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201762202U true CN201762202U (en) | 2011-03-16 |
Family
ID=43714813
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010202800371U Expired - Lifetime CN201762202U (en) | 2010-08-03 | 2010-08-03 | Electroplating purified water treatment device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201762202U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103539294A (en) * | 2013-10-08 | 2014-01-29 | 南京源泉环保科技股份有限公司 | Method for recovering silver plating wastewater and silver |
-
2010
- 2010-08-03 CN CN2010202800371U patent/CN201762202U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103539294A (en) * | 2013-10-08 | 2014-01-29 | 南京源泉环保科技股份有限公司 | Method for recovering silver plating wastewater and silver |
| CN103539294B (en) * | 2013-10-08 | 2015-07-29 | 南京源泉环保科技股份有限公司 | Reclaim the method for silver-plated waste water and silver |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN110156363B (en) | Sea sand desalination device and method | |
| CN202358976U (en) | Glass wastewater treatment equipment | |
| CN202912799U (en) | Comprehensive recycling system of metal plating wastewater resources | |
| CN102358651B (en) | Advanced treatment process for fermented pharmaceutical waste water | |
| CN102249459A (en) | System for desalinating sea water | |
| CN101367586B (en) | Desalting method for sewage water from oil production | |
| CN105152399A (en) | Reverse osmosis container-type sea water desalination plant and water producing process thereof | |
| CN103601310A (en) | Water processing method and device thereof of seawater desalination system | |
| CN205133204U (en) | Border on sea device of water of one -level three -section reverse osmosis treatment | |
| CN101462804A (en) | Electromembrane seawater desalination method and complete set of equipment | |
| CN201284277Y (en) | Small-sized water purifying appliance | |
| CN103204598A (en) | Whole-house quality-divided purification method | |
| CN102627364A (en) | Process flow for recycling and treating reverse osmosis concentrated water | |
| CN201065345Y (en) | Device for producing ultra-pure water by desalinizing sea water | |
| CN201610402U (en) | Recycling and deep treatment device for electronic electroplating wastewater | |
| CN203373223U (en) | Water treatment device of seawater desalination system | |
| CN105399249B (en) | A kind of device and method of municipal wastewater advanced treating | |
| CN206395957U (en) | A kind of cleaning system of drinking water system | |
| CN210103778U (en) | Sea sand desalination device | |
| CN101781041A (en) | Method for desalting bitter by electromembrane method and equipment thereof | |
| CN210313765U (en) | Fluorine-containing high-salinity wastewater recycling system | |
| CN201762202U (en) | Electroplating purified water treatment device | |
| CN105948291A (en) | Titanium-dioxide low-salt-waste-water recycling device and recycling method for low-salt waste water | |
| CN203498181U (en) | System for recycling waste acid and waste alkali | |
| CN201753291U (en) | Reclaimed water recycling device for electroplating wastewater |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee |
Owner name: CHANGCHUN ANKE PRECISION ELECTRONIC INDUSTRY CO., Free format text: FORMER NAME: CHANGCHUN ALLDAY ELECTROMAGNETIC SECURITY INDUSTRY CO., LTD. |
|
| CP03 | Change of name, title or address |
Address after: 130302, No. five, No. 001, Wei Sha Industrial Concentration Area, Changchun City, Jilin, Dehui Co-patentee after: Nanjing Spring Environmental Science & Technology Co., Ltd. Patentee after: Changchun Anchor Precise Electronic Industry Co., Ltd. Address before: 130302, Changchun, Jilin province rice sand industry concentrated area (standard workshop room 418) Co-patentee before: Nanjing Spring Environmental Science & Technology Co., Ltd. Patentee before: Beijing Allday Science and Technology Co., Ltd. |
|
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20110316 |