CN104030519B - Production technique wastewater recycling system - Google Patents
Production technique wastewater recycling system Download PDFInfo
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- CN104030519B CN104030519B CN201410205419.0A CN201410205419A CN104030519B CN 104030519 B CN104030519 B CN 104030519B CN 201410205419 A CN201410205419 A CN 201410205419A CN 104030519 B CN104030519 B CN 104030519B
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Abstract
The invention provides a kind of production technique wastewater recycling system, comprise wastewater disposal basin, biological reaction tank, activated carbon adsorption tank, the first settling bowl, ultra-filtration membrane carrier pond, the second settling bowl, reverse osmosis membrane carrier pond and clean water basin.Present invention achieves the production reuse of water, decrease chemical agent dosage, working cost is low, and the simple easy handling for the treatment of scheme, greatly the part labor force of wastewater treatment is discharged into real products production link, reduces labour cost.
Description
Technical field
The present invention relates to a kind of system, particularly relate to a kind of production technique wastewater recycling system.
Background technology
The production technique waste water mainly dyeing waste water of textile industry, concentration of organic wastewater is high, of a great variety, complex structure, belong to unmanageable trade effluent.Simple based on the traditional technology of biological treatment, be difficult to adaptation biodegradability treatment of dyeing wastewater worse and worse.The whole textile industry wastewater recycle rate of current China, less than 10%, therefore, to be employed new technology, saving water resource, and the reclamation rate improving water is the very important and difficult task of textile industry.
Summary of the invention
Technical problem to be solved by this invention is to provide a kind of textile production process wastewater recycling system.
For solving the problems of the technologies described above, the invention provides a kind of production technique wastewater recycling system, comprise wastewater disposal basin, biological reaction tank, activated carbon adsorption tank, the first settling bowl, ultra-filtration membrane carrier pond, the second settling bowl, reverse osmosis membrane carrier pond and clean water basin, the described wastewater disposal basin left side is provided with water-in, is provided with water outlet on the right of described wastewater disposal basin; The described biological reaction tank left side is provided with inlet channel, and described inlet channel is connected with described wastewater disposal basin water outlet, is provided with outlet conduit on the right of described biological reaction tank; Be provided with water circulating pump bottom described activated carbon adsorption tank, described gac water circulating pump is connected with described biological reaction tank outlet conduit; Described first settling bowl top is provided with water-in and water outlet, and the water-in of described first settling bowl is connected with described gac water circulating pump; The left side, described ultra-filtration membrane carrier pond is provided with inlet channel, and the right is provided with outlet conduit; Described second settling bowl top is provided with water-in and water outlet; The left side, described reverse osmosis membrane carrier pond is provided with intake pump, and the right is provided with out water pump; The described clean water basin left side is provided with water-in.
Described activated carbon adsorption tank completes absorption at high temperature under high pressure, and described temperature is 180-210 DEG C, and described pressure is 500-600MPa.
Described temperature is 195 DEG C.
Described pressure is 550MPa.
The inlet channel in described ultra-filtration membrane carrier pond is connected with the water outlet of described first settling bowl.
The water-in of described second settling bowl is connected with the water outlet of ultra-filtration membrane carrier.
The water-in in described reverse osmosis membrane carrier pond is connected with the water outlet of described second settling bowl; The intake-outlet of described reverse osmosis membrane carrier is connected with the water-in of described clean water basin.
Compared with prior art, beneficial effect of the present invention is: 1. this treatment process effectively combines the process advantage of ultra-filtration membrane and reverse osmosis membrane two kinds of films, achieve the degraded of Organic Pollutants in Wastewater, achieve the production reuse of water, waste water recycling, to production process, takes full advantage of calorific value in water resources and water.
2. treatment unit is compact, and take up an area few, management maintenance is convenient, and decrease chemical agent dosage, working cost is low.
3. the simple easy handling for the treatment of scheme, is discharged into real products production link by the part labor force of wastewater treatment greatly, reduces labour cost.
Embodiment
Below in conjunction with embodiment, the present invention is described in further details: a kind of production technique wastewater recycling system, comprise wastewater disposal basin, biological reaction tank, activated carbon adsorption tank, the first settling bowl, ultra-filtration membrane carrier pond, the second settling bowl, reverse osmosis membrane carrier pond and clean water basin, the described wastewater disposal basin left side is provided with water-in, is provided with water outlet on the right of described wastewater disposal basin; The described biological reaction tank left side is provided with inlet channel, and described inlet channel is connected with described wastewater disposal basin water outlet, is provided with outlet conduit on the right of described biological reaction tank; Be provided with water circulating pump bottom described activated carbon adsorption tank, described gac water circulating pump is connected with described biological reaction tank outlet conduit; Described first settling bowl top is provided with water-in and water outlet, and the water-in of described first settling bowl is connected with described gac water circulating pump; The left side, described ultra-filtration membrane carrier pond is provided with inlet channel, and the right is provided with outlet conduit; Described second settling bowl top is provided with water-in and water outlet; The left side, described reverse osmosis membrane carrier pond is provided with intake pump, and the right is provided with out water pump; The described clean water basin left side is provided with water-in.Described activated carbon adsorption tank completes absorption at high temperature under high pressure, and described temperature is 180-210 DEG C, and described pressure is 500-600MPa.Described temperature is 195 DEG C.Described pressure is 550MPa.The inlet channel in described ultra-filtration membrane carrier pond is connected with the water outlet of described first settling bowl.The water-in of described second settling bowl is connected with the water outlet of ultra-filtration membrane carrier.The water-in in described reverse osmosis membrane carrier pond is connected with the water outlet of described second settling bowl; The intake-outlet of described reverse osmosis membrane carrier is connected with the water-in of described clean water basin.
In sum, step of the present invention is simple, easy to operate.
The foregoing is only better embodiment of the present invention; protection scope of the present invention is not limited with above-mentioned embodiment; in every case those of ordinary skill in the art modify or change according to the equivalence that disclosed content is done, and all should include in the protection domain recorded in claims.
Claims (6)
1. production technique wastewater recycling system, comprise wastewater disposal basin, characterized by further comprising: biological reaction tank, activated carbon adsorption tank, the first settling bowl, ultra-filtration membrane carrier pond, the second settling bowl, reverse osmosis membrane carrier pond and clean water basin, the described wastewater disposal basin left side is provided with water-in, is provided with water outlet on the right of described wastewater disposal basin; The described biological reaction tank left side is provided with inlet channel, and described inlet channel is connected with described wastewater disposal basin water outlet, is provided with outlet conduit on the right of described biological reaction tank; Be provided with water circulating pump bottom described activated carbon adsorption tank, described water circulating pump is connected with described biological reaction tank outlet conduit; Described first settling bowl top is provided with water-in and water outlet, and the water-in of described first settling bowl is connected with described water circulating pump; The left side, described ultra-filtration membrane carrier pond is provided with inlet channel, and the right is provided with outlet conduit; Described second settling bowl top is provided with water-in and water outlet; The left side, described reverse osmosis membrane carrier pond is provided with intake pump, and the right is provided with out water pump; The described clean water basin left side is provided with water-in; Described activated carbon adsorption tank completes absorption at high temperature under high pressure, and described high temperature is 180-210 DEG C, and described high pressure is 500-600MPa.
2. production technique wastewater recycling system according to claim 1, is characterized in that: described high temperature is 195 DEG C.
3. production technique wastewater recycling system according to claim 1, is characterized in that: described high pressure is 550MPa.
4. production technique wastewater recycling system according to claim 1, is characterized in that: the inlet channel in described ultra-filtration membrane carrier pond is connected with the water outlet of described first settling bowl.
5. production technique wastewater recycling system according to claim 1, is characterized in that: the water-in of described second settling bowl is connected with the water outlet of ultra-filtration membrane carrier.
6. production technique wastewater recycling system according to claim 1, is characterized in that: the water-in in described reverse osmosis membrane carrier pond is connected with the water outlet of described second settling bowl; The intake-outlet of described reverse osmosis membrane carrier is connected with the water-in of described clean water basin.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CN201410205419.0A CN104030519B (en) | 2014-05-16 | 2014-05-16 | Production technique wastewater recycling system |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201410205419.0A CN104030519B (en) | 2014-05-16 | 2014-05-16 | Production technique wastewater recycling system |
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| CN104030519A CN104030519A (en) | 2014-09-10 |
| CN104030519B true CN104030519B (en) | 2016-04-20 |
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| CN201410205419.0A Active CN104030519B (en) | 2014-05-16 | 2014-05-16 | Production technique wastewater recycling system |
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| CN2347969Y (en) * | 1998-08-25 | 1999-11-10 | 彭虎 | Drinking water purifier |
| CN2856038Y (en) * | 2005-10-27 | 2007-01-10 | 韩春来 | Recovery and utilizing appts, for sewage from oil refining and chemistry |
| CN101041532A (en) * | 2007-02-15 | 2007-09-26 | 三达膜科技（厦门）有限公司 | Printing and dyeing waste water treatment method based on film technology |
| CN101311132A (en) * | 2008-05-23 | 2008-11-26 | 王俊川 | Waste water recycling comprehensive processing process |
| CN101633541A (en) * | 2008-07-21 | 2010-01-27 | 浙江四通环境工程有限公司 | Integrated technology for deep purification treatment for printing and dyeing waste water |
| CN202322568U (en) * | 2011-11-18 | 2012-07-11 | 北京伊普国际水务有限公司 | Deep treatment system of high-concentration percolate of integrated garbage treatment site |
| CN103011524A (en) * | 2012-12-28 | 2013-04-03 | 湖北君集水处理有限公司 | Recycling and processing method for printing and dyeing wastewater |
| CN103359878A (en) * | 2013-07-12 | 2013-10-23 | 华南理工大学 | Treatment method for realizing zero emission of printing and dyeing wastewater |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4029100B2 (en) * | 2005-09-14 | 2008-01-09 | シャープ株式会社 | Water treatment apparatus and water treatment method |
-
2014
- 2014-05-16 CN CN201410205419.0A patent/CN104030519B/en active Active
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2347969Y (en) * | 1998-08-25 | 1999-11-10 | 彭虎 | Drinking water purifier |
| CN2856038Y (en) * | 2005-10-27 | 2007-01-10 | 韩春来 | Recovery and utilizing appts, for sewage from oil refining and chemistry |
| CN101041532A (en) * | 2007-02-15 | 2007-09-26 | 三达膜科技（厦门）有限公司 | Printing and dyeing waste water treatment method based on film technology |
| CN101311132A (en) * | 2008-05-23 | 2008-11-26 | 王俊川 | Waste water recycling comprehensive processing process |
| CN101633541A (en) * | 2008-07-21 | 2010-01-27 | 浙江四通环境工程有限公司 | Integrated technology for deep purification treatment for printing and dyeing waste water |
| CN202322568U (en) * | 2011-11-18 | 2012-07-11 | 北京伊普国际水务有限公司 | Deep treatment system of high-concentration percolate of integrated garbage treatment site |
| CN103011524A (en) * | 2012-12-28 | 2013-04-03 | 湖北君集水处理有限公司 | Recycling and processing method for printing and dyeing wastewater |
| CN103359878A (en) * | 2013-07-12 | 2013-10-23 | 华南理工大学 | Treatment method for realizing zero emission of printing and dyeing wastewater |
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| CN104030519A (en) | 2014-09-10 |
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