CN201678490U - Condensation and recycling device for copolymerization resin waste water - Google Patents
Condensation and recycling device for copolymerization resin waste water Download PDFInfo
- Publication number
- CN201678490U CN201678490U CN2009202854612U CN200920285461U CN201678490U CN 201678490 U CN201678490 U CN 201678490U CN 2009202854612 U CN2009202854612 U CN 2009202854612U CN 200920285461 U CN200920285461 U CN 200920285461U CN 201678490 U CN201678490 U CN 201678490U
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- waste water
- outlet
- water outlet
- condensation
- recycling device
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Abstract
The utility model relates to a condensation and recycling device for copolymerization resin waste water comprises a film casing and is characterized in that a permeating chamber is arranged inside the film casing and has hundreds or even thousands of hollow fibers having an outer diameter of 1-2mm, only small molecular particles can penetrate the hollow fibers, the film casing is of tubular shape narrowing on both ends, of which one is a waste water inlet and the other is condensed liquid outlet, a first filtered water outlet is provided on the side of the waste water inlet end, a second filtered water outlet is provided on the side of the condensed liquid outlet end, a left separator is arranged between the waste water inlet and the first filtered water outlet, and a right separator is arranged between the condensed liquid outlet and the second filtered water outlet. The utility model is short in process flow and can operate continuously to recycle all waste water thereby saving production cost, realizing zero discharge and reaching the eco-production goal. Less complexity, small size and onetime distributing water lowers the total operation cost of the condensation and recycling device.
Description
Technical field
The utility model relates to a kind of centrifuge waste water and concentrates recovery system, specifically a kind of copolymer resins waste water concentrating recovery device that is used for vinylchlorid and vinyl acetate between to for plastic copolymer resins.
Background technology
In the prior art, vinylchlorid and the wastewater produced processing of vinyl acetate between to for plastic copolymer resins, usually adopt following method: in waste water, add special-purpose precipitation agent, solid in the emulsion is separated with liquid, get supernatant liquid again through biochemical treatment, clear liquor after the processing directly discharges, and solid sediment is then transported outward and entrusted other processed in units.
The defective of this processing mode is: waste water does not only utilize, and the transfer of the objectionable impurities in the solid, liquid, and unfavorable to environment, processing cost is higher.
Summary of the invention
The purpose of this utility model is to overcome the deficiencies in the prior art, provides a kind of and can reclaim useful matter in the waste water, can avoid the copolymer resins waste water concentrating recovery device of contaminate environment simultaneously.
The technical scheme that provides according to the utility model, described copolymer resins waste water concentrating recovery device, comprise putamina, it is characterized in that: be to see through the chamber in the described putamina, see through and in the chamber hundreds of to tens thousand of external diameters to be set the hollow tubular tubular fibre that is 1～2mm, described tubular fibre can only be through the small molecules particle and macromolecular particle only thoroughly; Described putamina is a cylindrical body, closes up in two ends, and first end is the waste water import, and second end is a concentrated solution outlet, is provided with the outlet of first permeate water in the side near first end, is provided with the outlet of second permeate water in the side near second end; Between waste water import and the outlet of first permeate water, be provided with left clapboard, between concentrated solution outlet and the outlet of second permeate water, be provided with right clapboard.
Described small molecules particle is the material of thousands of～tens thousand of molecular weight, and described macromolecular particle is the material of hundreds thousand of～millions of molecular weight.
The wastewater flow of described waste water import is 400～500L/m
2H; Pressure 0.07～0.15Mpa; The permeate water flow is 18～20L/m
2H; Wastewater pH is 2.5～3.0.
Operation scheme of the present utility model is successional, and technical process is short; The limit reuse is separated in waste water access to plant back, and waste water is all reclaimed, and has both saved production cost, has realized zero release again, has really reached green production.And equipment is few, and volume is little, and floor space is little; Fully automatic operation, disposable water delivery, power consumption is economized, and overall running cost is low, and processing costs is low.
Description of drawings
Fig. 1 is a structural representation of the present utility model.
Fig. 2 is the B-B view among Fig. 1.
Fig. 3 is the enlarged view of A among Fig. 1.
Embodiment
The utility model is described in further detail below in conjunction with concrete drawings and Examples.
Shown in Fig. 1～3: copolymer resins waste water concentrating recovery device comprises waste water import 1, end socket 2, left clapboard 3, first permeate water outlet 4, putamina 5, sees through chamber 6, tubular fibre 7, right clapboard 8, second permeate water outlet 9, concentrated solution outlet 10, macromolecular particle 11, small molecules particle 12 etc.
The utility model comprises putamina 5, be to see through chamber 6 in the described putamina 5, is the hollow tubular tubular fibre 7 of 1～2mm through being provided with hundreds of in the chamber 6 to tens thousand of external diameters, and described tubular fibre can only see through thousands of～tens thousand of molecular weight and the material of saturating only hundreds thousand of～millions of molecular weight; Described putamina 5 is a cylindrical body, close up in two ends, first end is that waste water import 1, the second end is a concentrated solution outlet 10, be provided with first permeate water outlet 4 in side, be provided with second permeate water outlet 9 in side near concentrated solution outlet 10 1 ends near waste water import 1 one ends; Between waste water import 1 and first permeate water outlet 4, be provided with left clapboard 3, between concentrated solution outlet 10 and second permeate water outlet 9, be provided with right clapboard 8.
After the adjusting waste water ph is 2.5～3.0, enter again in the putamina 5; When waste water flows into putamina 5 from waste water import 1 end, and enter in the tubular fibre 7, small molecules particle 12 sees through tubular fibre, flows out through lateral first permeate water outlet, 4 and second permeate water outlet 9, and macromolecular particle 11 flows out from the concentrated solution outlet 10 of second end.Therefore, waste water is by behind the tubular fibre 7, and small molecules particle 12 is separated with macromolecular particle 11, concentrates the purpose that reclaims thereby reach waste water.
Described waste water import 1 adopts big flow to advance waste water, and wastewater flow is 400～500L/m
2H; Low pressure operation operation, pressure 0.07～0.15MPa; The permeate water flow is 18～20L/m
2H.
The utility model adopts the ultra-filtration membrane isolation technique, and waste water can be separated into two parts: a part is a concentrated solution, i.e. suspension liquid body after concentrated, and this suspension liquid body can be used as raw material and is back on the production line; Another part is to see through liquid, and the thinner that can be used as pure raw material is back on the production line.The utility model can make the waste water fully recovering, realizes the waste water treatment zero release, reaches green production.
Claims (4)
1. copolymer resins waste water concentrating recovery device, comprise putamina (5), it is characterized in that: be to see through chamber (6) in the described putamina (5), see through the hollow tubular tubular fibre (7) that some external diameter 1～2mm are set in the chamber (6), described tubular fibre can only see through small molecules particle (12) and macromolecular particle (11) only thoroughly; Described putamina (5) is a cylindrical body, close up in two ends, first end wherein is waste water import (1), and second end is concentrated solution outlet (10), be provided with first permeate water outlet (4) in side, be provided with second permeate water outlet (9) in side near second end near first end; Between waste water import (1) and first permeate water outlet (4), be provided with left clapboard (3), between concentrated solution outlet (10) and second permeate water outlet (9), be provided with right clapboard (8).
2. copolymer resins waste water concentrating recovery device as claimed in claim 1 is characterized in that: described small molecules particle (12) is the material of thousands of～tens thousand of molecular weight, and described macromolecular particle (11) is the material of hundreds thousand of～millions of molecular weight.
3. copolymer resins waste water concentrating recovery device as claimed in claim 1 is characterized in that: the flow of waste water is 400～500L/m in the described waste water import (1)
2H; Pressure 0.07～0.15Mpa; The permeate water flow is 18～20L/m
2H.
4. copolymer resins waste water concentrating recovery device as claimed in claim 1 is characterized in that: wastewater pH is 2.5～3.0.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009202854612U CN201678490U (en) | 2009-12-29 | 2009-12-29 | Condensation and recycling device for copolymerization resin waste water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009202854612U CN201678490U (en) | 2009-12-29 | 2009-12-29 | Condensation and recycling device for copolymerization resin waste water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201678490U true CN201678490U (en) | 2010-12-22 |
Family
ID=43343543
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009202854612U Expired - Fee Related CN201678490U (en) | 2009-12-29 | 2009-12-29 | Condensation and recycling device for copolymerization resin waste water |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201678490U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103723795A (en) * | 2013-12-04 | 2014-04-16 | 江苏双净净化科技有限公司 | Concentrating and recovering device for copolymerization resin waste water and recovery method thereof |
| CN104394964A (en) * | 2012-11-26 | 2015-03-04 | 甘布罗伦迪亚股份公司 | Filter device combining beads and fibers |
| CN108636124A (en) * | 2012-05-23 | 2018-10-12 | 威立雅水务解决方案与技术支持公司 | Filter plant |
-
2009
- 2009-12-29 CN CN2009202854612U patent/CN201678490U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108636124A (en) * | 2012-05-23 | 2018-10-12 | 威立雅水务解决方案与技术支持公司 | Filter plant |
| CN108636124B (en) * | 2012-05-23 | 2021-03-19 | 威立雅水务解决方案与技术支持公司 | Filter device |
| CN104394964A (en) * | 2012-11-26 | 2015-03-04 | 甘布罗伦迪亚股份公司 | Filter device combining beads and fibers |
| CN103723795A (en) * | 2013-12-04 | 2014-04-16 | 江苏双净净化科技有限公司 | Concentrating and recovering device for copolymerization resin waste water and recovery method thereof |
| CN103723795B (en) * | 2013-12-04 | 2015-05-20 | 江苏双净净化科技有限公司 | Concentrating and recovering device for copolymerization resin waste water and recovery method thereof |
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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: JIANGSU SHUANGJING CLEANSING TECHNOLOGY CO., LTD. Free format text: FORMER NAME: WUXI SHUANGJING CLEANSING EQUIPMENT CO., LTD. |
|
| CP01 | Change in the name or title of a patent holder |
Address after: 214123 women's street, Binhu District, Jiangsu, Wuxi, 6 Patentee after: Jiangsu Shuangjing Purification Technology Co., Ltd. Address before: 214123 women's street, Binhu District, Jiangsu, Wuxi, 6 Patentee before: Wuxi Shuangjing Purification Equipment Co., Ltd. |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20101222 Termination date: 20151229 |