CN104030519A - Production process wastewater recycling system - Google Patents
Production process wastewater recycling system Download PDFInfo
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- CN104030519A CN104030519A CN201410205419.0A CN201410205419A CN104030519A CN 104030519 A CN104030519 A CN 104030519A CN 201410205419 A CN201410205419 A CN 201410205419A CN 104030519 A CN104030519 A CN 104030519A
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- water
- membrane carrier
- recycling system
- settling bowl
- pool
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- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The invention provides a production process wastewater recycling system including a wastewater pool, a biological reaction pool, an activated carbon adsorption pool, a first sedimentation pool, an ultrafiltration membrane carrier pool, a second sedimentation pool, a reverse osmosis membrane carrier pool and a clear water pool. The production process wastewater recycling system realizes production reuse of water, reduces the adding amount of chemical drugs, is low in operating cost, has simple and easily operated treatment flow, greatly releases a part of labor for wastewater treatment into real product production chains, and reduces labor costs.
Description
Technical field
The present invention relates to a kind of system, relate in particular to a kind of production technique wastewater recycling system.
Background technology
The production technique waste water of textile industry is mainly dyeing waste water, and concentration of organic wastewater is high, of a great variety, complex structure, belong to unmanageable trade effluent.The simple traditional technology taking biological treatment as master, has been difficult to adapt to biodegradability treatment of dyeing wastewater worse and worse.At present China's whole textile industry wastewater recycle rate less than 10%, therefore, employs new technology, saving water resource, and the reclamation rate that improves 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, and described wastewater disposal basin the right is provided with water outlet; 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, and described biological reaction tank the right is provided with outlet conduit; Described activated carbon adsorption tank bottom is provided with water circulating pump, and described gac water circulating pump is connected with described biological reaction tank outlet conduit; Described the first settling bowl top is provided with water-in and water outlet, and the water-in of described the 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 the 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 under High Temperature 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 the first settling bowl.
The water-in of described the 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 the 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 processing advantage of ultra-filtration membrane and two kinds of films of reverse osmosis membrane, realize the degraded of Organic Pollutants in Wastewater, realize 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 compactness, takes up an area less, and management maintenance is convenient, has reduced chemical agent dosage, and 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, and described wastewater disposal basin the right is provided with water outlet; 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, and described biological reaction tank the right is provided with outlet conduit; Described activated carbon adsorption tank bottom is provided with water circulating pump, and described gac water circulating pump is connected with described biological reaction tank outlet conduit; Described the first settling bowl top is provided with water-in and water outlet, and the water-in of described the 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 the 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 under High Temperature 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 the first settling bowl.The water-in of described the 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 the 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 preferred embodiments of the present invention; protection scope of the present invention is not limited with above-mentioned embodiment; in every case the equivalence that those of ordinary skill in the art do according to disclosed content is modified or is changed, and all should include in the protection domain of recording in claims.
Claims (7)
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, and described wastewater disposal basin the right is provided with water outlet; 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, and described biological reaction tank the right is provided with outlet conduit; Described activated carbon adsorption tank bottom is provided with water circulating pump, and described gac water circulating pump is connected with described biological reaction tank outlet conduit; Described the first settling bowl top is provided with water-in and water outlet, and the water-in of described the 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 the 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.
2. production technique wastewater recycling system according to claim 1, is characterized in that: described activated carbon adsorption tank completes absorption under High Temperature High Pressure, described temperature is 180-210 DEG C, and described pressure is 500-600MPa.
3. production technique wastewater recycling system according to claim 2, is characterized in that: described temperature is 195 DEG C.
4. production technique wastewater recycling system according to claim 2, is characterized in that: described pressure is 550MPa.
5. 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 the first settling bowl.
6. production technique wastewater recycling system according to claim 1, is characterized in that: the water-in of described the second settling bowl is connected with the water outlet of ultra-filtration membrane carrier.
7. 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 the 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 |
|---|---|---|---|
| CN201410205419.0A CN104030519B (en) | 2014-05-16 | 2014-05-16 | Production technique wastewater recycling system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410205419.0A CN104030519B (en) | 2014-05-16 | 2014-05-16 | Production technique wastewater recycling system |
Publications (2)
| Publication Number | Publication Date |
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| CN104030519A true CN104030519A (en) | 2014-09-10 |
| CN104030519B CN104030519B (en) | 2016-04-20 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201410205419.0A Active CN104030519B (en) | 2014-05-16 | 2014-05-16 | Production technique wastewater recycling system |
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Citations (9)
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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 |
| US20090266763A1 (en) * | 2005-09-14 | 2009-10-29 | Sharp Kabushiki Kaisha | Water Treatment Apparatus and Water Treatment Method |
| 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 |
-
2014
- 2014-05-16 CN CN201410205419.0A patent/CN104030519B/en active Active
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2347969Y (en) * | 1998-08-25 | 1999-11-10 | 彭虎 | Drinking water purifier |
| US20090266763A1 (en) * | 2005-09-14 | 2009-10-29 | Sharp Kabushiki Kaisha | Water Treatment Apparatus and Water Treatment Method |
| 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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| CN104030519B (en) | 2016-04-20 |
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