CN101468861A - Treating system for dyeing waste water - Google Patents
Treating system for dyeing waste water Download PDFInfo
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- CN101468861A CN101468861A CNA2007103045413A CN200710304541A CN101468861A CN 101468861 A CN101468861 A CN 101468861A CN A2007103045413 A CNA2007103045413 A CN A2007103045413A CN 200710304541 A CN200710304541 A CN 200710304541A CN 101468861 A CN101468861 A CN 101468861A
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- dyeing wastewater
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Abstract
The invention relates to a system for treating dye printing wastewater. The system mainly comprises a pre-aeration adjusting pool, a primary precipitation pool, a hydrolysis acidification pool, an aerobic biological filter tank, a secondary precipitation pool and electric biological oxidation treatment equipment sequentially connected; the electric biological oxidation treatment equipment comprises a shell; the inside of the shell is provided with a space forming a water flow passage; the inside of the space forming the water flow passage is provided with a biological filler; the inside of the space is also provided with a plurality of pairs of electrodes; and the extending direction of the electrodes is vertical to the extending direction of the water flow passage. The system has reasonable matching of process flow, can effectively remove organic pollutants in the dye printing wastewater, combine the electrolysis treatment process and biotreatment process into a whole through the electric biological oxidation treatment equipment, exert the oxidation-reduction function of electrolysis, simultaneously improve the environment for biotreatment, increase the whole treatment capacity and treatment effect and realize satisfactory treatment effect.
Description
Invention field
The present invention relates to a kind of Waste Water Treatment of handling dyeing and printing sewage that is mainly used in, belong to the environmental protection field.
Background technology
Dyeing waste water contains COD, BOD and the colourity of higher concentration, and wherein colourity can reach 100-400 times, BOD
5Can reach 100-400mg/l, COD
CrCan reach 600-800mg/l, and biodegradability of organic matter wherein is poor, the quantity discharged instability adopts common biological treatment mode difficulty bigger.
Summary of the invention
For overcoming the above-mentioned defective of prior art, the invention provides a kind of printing and dyeing wastewater treatment system, the technical process collocation rationally, can eliminate the organic pollutant in the dyeing waste water effectively, and by electric biochemical processing device electrolysis treatment process and biological treatment process are integrated, not only bring into play electrolytic redoxomorphism, also improved the environment of biological treatment simultaneously, improve whole processing power and treatment effect, realized satisfied treatment effect.
The present invention realizes that the technical scheme of above-mentioned purpose is: a kind of printing and dyeing wastewater treatment system, mainly by the preaeration equalizing tank, one heavy pond, hydrolysis acidification pool, aerobic biofilter, second pond and electric bio-oxidation treatment facility constitute, described preaeration equalizing tank, one heavy pond, hydrolysis acidification pool, aerobic biofilter, second pond and electric bio-oxidation treating pond interconnect successively, described electric bio-oxidation treatment facility comprises housing, be provided with the space that constitutes water stream channel in its housing, be provided with biologic packing material in the space of described formation water stream channel, also be provided with some counter electrode, the bearing of trend of described electrode is vertical mutually with the bearing of trend of described water stream channel.
Because the present invention has adopted rational processing step and processing unit, earlier unsettled draining is regulated, carrying out preaeration simultaneously in the process of regulating handles, improve its organic biodegradability by hydrolysis acidification pool, and carry out purifying treatment by aerobic biofilter efficiently, organic pollutant content in the sewage after the processing reduces significantly, handle for the efficient electric bio-oxidation that wherein partly is difficult to the electric bio-oxidation treatment facility of biodegradable process again, by in water, forming partial electrolysis, the Oxidizing and Reducing Agents that generates carries out oxidation or reduction reaction to the organism in the water, biology direct and on every side contacts, help to improve the speed of biological treatment, and reduce the density of electrolysis resultant at any time, make electrolytic equilibrium help direction object space exhibition to resultant, improve electrolytic effect, formed mutually promoting of biological treatment and electrolysis treatment thus, make whole structure be better than electrolysis and biological two independent treating processess, although at present because biological complicacy, also do not understand biological mechanism of answering under the electrolysis fully, but this structure of mutually promoting is sure.In addition, because electrode direction is vertical with water (flow) direction, the electric field change that helps the route of current process, making different water all pass through similar electric field alternately changes, avoid the treatment effect because of the uneven influence integral body that weighs of the treatment effect of each several part current, it is just accurate to make final outflow water meet country's discharging.
Description of drawings
Fig. 1 is a structural representation of the present invention;
Fig. 2 is the structural representation of the present invention's electricity bio-oxidation treatment facility.
Embodiment
Referring to Fig. 1, printing and dyeing wastewater treatment system provided by the invention is mainly by the preaeration equalizing tank, one heavy pond, hydrolysis acidification pool, aerobic biofilter, second pond and electric bio-oxidation treatment facility constitute, described preaeration equalizing tank, one heavy pond, hydrolysis acidification pool, aerobic biofilter, second pond and electric bio-oxidation treating pond interconnect successively, described electric bio-oxidation treatment facility comprises housing, be provided with the space that constitutes water stream channel in its housing, be provided with biologic packing material in the space of described formation water stream channel, also be provided with some counter electrode, the bearing of trend of described electrode is vertical mutually with the bearing of trend of described water stream channel.
Described preaeration equalizing tank front can be provided with grid.
Inhomogeneous state of peak valley that described preaeration equalizing tank is mainly used in regulating pondage and the pH that regulates sewage when carrying out the adjusting of the homogeneous water yield, regulate the pH value of sewage by adding alkali, to guarantee carrying out smoothly of subsequent treatment process.
Can add the flocculation agent of ferrous sulfate as decoloring reaction to a heavy pond, decolorizing effect is the most obvious when pH is between 8.5-9, by the flocculation and the precipitation in a heavy pond, can remove the pollutents such as colourity, COD and SS of part in the water.
Described hydrolysis acidification pool be provided with mainly be because dyeing waste water in contain macromolecule organic than difficulty directly by aerobic degradation, in the acidication stage, degrade by anoxic, make larger molecular organics in the water be decomposed into the small organic molecule of easy biochemistry, thereby improve the biodegradability of waste water, guarantee follow-up biochemical treatment effect.
The impeller of diving under water at a high speed can be installed in the described hydrolysis acidification pool, guarantee that anaerobion can fully contact with waste water, evenly water quality.
Described aerobic biofilter can be equipped with biofilter material or the other biological filtrate that plastics are carrier, and the micro porous aeration head aeration is set at the bottom of the pond, the organism that aerobic bacteria can be accessed in the enough oxygen utilization waste water carries out metabolism, remove the pollution substance in the water, aeration also helps making pool inner water fully to contact with microorganism simultaneously.
Described second pond is provided with sludge return pipe and connects aerobic biofilter, keeps activated sludge concentration in the aerobic biofilter so that reflux by mud.
Referring to Fig. 2, electric bio-oxidation treatment facility of the present invention comprises housing 8, be provided with the space that constitutes water stream channel in its housing, be provided with biofilter material 5 in the space of described formation water stream channel, also be provided with some electrodes to being made of positive pole 7 and negative pole 6, the bearing of trend of described electrode is vertical mutually with the bearing of trend of described water stream channel.
The intravital space of described shell quilt is two water distribution boards 10 up and down, 4 are partitioned into hydroecium 11 from top to bottom successively, reaction chamber and intake chamber 3, the water-supplying chamber on top is provided with rising pipe 9, the intake chamber of bottom is provided with water inlet pipe 1, aerator 2 is installed in its bottom, the intravital reaction chamber of shell is equipped with biofilter material 5, and be provided with the positive and negative electrode of horizontal expansion, it can be the pair of electrodes that distributes up and down, the pair of electrodes that distributes about also can being, according to the intravital arrangement space of shell, when adopt vertical and about distribute three-dimensional distribution mode the time, described positive and negative electrode laterally and on vertical all should be alternately distributed, positive negative electricity interts between filtrate.
Skeleton in the described filtrate can be organic polymer filler, mineral filler or inertia embedding medium carriers such as sodium alginate, PVA.
Described filtrate can be piled up placement at reaction chamber, also can hang placement, and its stacking filling ratio in reaction chamber can be for 20%-95%.
Described case top can be provided with the anti-explosion alarming device.
The electrode that described positive and negative electrode can adopt carbon, iron, stainless steel, nickel porous,, platinum or germanium are made with catalytic activity.
Distance can be 20 1 500mm between the described adjacent positive and negative electrode.
The transverse shape of described housing can be circular, also can be rectangle.
Described housing can adopt vertical structure, and its water-in is positioned at the below, and current are bottom-up stream in housing, helps reducing flow resistance thus.
Described housing also can adopt horizontal type structure, and current are transverse flow in housing, and this mode helps forming long length.
Claims (10)
1. printing and dyeing wastewater treatment system, mainly by the preaeration equalizing tank, one heavy pond, hydrolysis acidification pool, aerobic biofilter, second pond and electric bio-oxidation treatment facility constitute, described preaeration equalizing tank, one heavy pond, hydrolysis acidification pool, aerobic biofilter, second pond and electric bio-oxidation treatment facility interconnect successively, described electric bio-oxidation treatment facility comprises housing, be provided with the space that constitutes water stream channel in its housing, be provided with biologic packing material in the space of described formation water stream channel, also be provided with some counter electrode, the bearing of trend of described electrode is vertical mutually with the bearing of trend of described water stream channel.
2. printing and dyeing wastewater treatment system as claimed in claim 1 is characterized in that described preaeration equalizing tank front is provided with grid, and the impeller of diving under water at a high speed is installed in the described hydrolysis acidification pool.
3. printing and dyeing wastewater treatment system as claimed in claim 1, it is characterized in that described aerobic biofilter is equipped with biofilter material or the other biological filtrate that plastics are carrier, and the micro porous aeration head aeration is set at the bottom of the pond, described second pond is provided with sludge return pipe and connects aerobic biofilter.
4. as claim 1,2 or 3 described printing and dyeing wastewater treatment systems, two water distribution boards are separated into water-supplying chamber, reaction chamber and intake chamber from top to bottom successively about it is characterized in that the intravital space of described shell quilt, superposed water-supplying chamber is provided with rising pipe, aerator is installed in the intake chamber bottom that is positioned at the bottom, and the reaction chamber that is positioned at the middle part is equipped with biofilter material.
5. printing and dyeing wastewater treatment system as claimed in claim 4 is characterized in that described filtrate in reaction chamber accumulation placement or suspension placement, and described positive negative electricity interts between described filtrate.
6. printing and dyeing wastewater treatment system as claimed in claim 5, it is characterized in that described positive and negative electrode is the pair of electrodes that distributes up and down, or about the pair of electrodes that distributes, or many counter electrode, when many counter electrode vertical and about distribute three-dimensional distribution mode the time, described positive and negative electrode laterally and on vertical all is being alternately distributed, and positive negative electricity interts between filtrate.
7. printing and dyeing wastewater treatment system as claimed in claim 6, it is characterized in that described adjacent positive and negative electrode between the distance be 20-500mm.
8. printing and dyeing wastewater treatment system as claimed in claim 7 is characterized in that described case top is provided with the anti-explosion alarming device.
9. printing and dyeing wastewater treatment system as claimed in claim 8, the transverse shape that it is characterized in that described housing are circle or rectangle.
10. printing and dyeing wastewater treatment system as claimed in claim 9 is characterized in that described housing adopts vertical structure or horizontal type structure.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNA2007103045413A CN101468861A (en) | 2007-12-28 | 2007-12-28 | Treating system for dyeing waste water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNA2007103045413A CN101468861A (en) | 2007-12-28 | 2007-12-28 | Treating system for dyeing waste water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN101468861A true CN101468861A (en) | 2009-07-01 |
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ID=40826709
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNA2007103045413A Pending CN101468861A (en) | 2007-12-28 | 2007-12-28 | Treating system for dyeing waste water |
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| CN (1) | CN101468861A (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101774715A (en) * | 2010-03-10 | 2010-07-14 | 华南师范大学 | System and method for advanced treatment and reuse of dyeing wastewater |
| CN102153243A (en) * | 2011-04-27 | 2011-08-17 | 安徽南风环境工程技术有限公司 | High efficient multifunctional wastewater treatment system |
| CN102583898A (en) * | 2012-03-06 | 2012-07-18 | 哈尔滨工业大学 | Strengthened hard-degradation-wastewater treatment device with biocatalysis electrolysis and anaerobic hydrolysis acidification being coupled |
| CN103641271A (en) * | 2013-11-28 | 2014-03-19 | 哈尔滨工业大学 | Microorganism reinforced gallery pushing flow type wastewater treatment bioelectrochemical device |
| CN106007206A (en) * | 2016-07-06 | 2016-10-12 | 广州新能源水处理有限公司 | Refuse leachate biochemical and membrane separation tail end concentrated solution treatment device and treatment technology |
| CN106045142A (en) * | 2016-07-06 | 2016-10-26 | 广州新能源水处理有限公司 | Counter-current filter and electrolysis device and filter and electrolysis process |
-
2007
- 2007-12-28 CN CNA2007103045413A patent/CN101468861A/en active Pending
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101774715A (en) * | 2010-03-10 | 2010-07-14 | 华南师范大学 | System and method for advanced treatment and reuse of dyeing wastewater |
| CN102153243A (en) * | 2011-04-27 | 2011-08-17 | 安徽南风环境工程技术有限公司 | High efficient multifunctional wastewater treatment system |
| CN102583898A (en) * | 2012-03-06 | 2012-07-18 | 哈尔滨工业大学 | Strengthened hard-degradation-wastewater treatment device with biocatalysis electrolysis and anaerobic hydrolysis acidification being coupled |
| CN103641271A (en) * | 2013-11-28 | 2014-03-19 | 哈尔滨工业大学 | Microorganism reinforced gallery pushing flow type wastewater treatment bioelectrochemical device |
| CN103641271B (en) * | 2013-11-28 | 2016-02-17 | 哈尔滨工业大学 | A kind of microbial augmentation type gallery pulling flow type wastewater treatment Bioelectrochemical device |
| CN106007206A (en) * | 2016-07-06 | 2016-10-12 | 广州新能源水处理有限公司 | Refuse leachate biochemical and membrane separation tail end concentrated solution treatment device and treatment technology |
| CN106045142A (en) * | 2016-07-06 | 2016-10-26 | 广州新能源水处理有限公司 | Counter-current filter and electrolysis device and filter and electrolysis process |
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Open date: 20090701 |