CN1821128A - Method for treating high concentration organic waste water - Google Patents
Method for treating high concentration organic waste water Download PDFInfo
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- CN1821128A CN1821128A CNA2006100204540A CN200610020454A CN1821128A CN 1821128 A CN1821128 A CN 1821128A CN A2006100204540 A CNA2006100204540 A CN A2006100204540A CN 200610020454 A CN200610020454 A CN 200610020454A CN 1821128 A CN1821128 A CN 1821128A
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
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Abstract
The method of treating high concentration organic waste water includes eliminating sand and slag, and flocculating deposition to separate, as well as microbial degradation and catalytic oxidizing degradation in an integrated degrading tank, and electrolyzing oxidation degradation. After depositing separation, the sludge is incinerated and the catalytic oxidant is regenerated for reuse. The treated waste water is drained or reused. The present invention integrates various water treating modes, physical, biological, chemical, electrochemical, etc. and has high waste water purifying effect.
Description
Technical field
The invention belongs to the multiple-stage treatment of water, waste water or sewage, relate to a kind of treatment process of high concentration organic sewage.
Background technology
Industry such as organic chemical industry, food-processing, textile printing and dyeing, papermaking, leather, medicine and hold the organic sewage that produces in the industry production such as fowl breed enters rivers and will cause severe contamination, and then causes water resources to lack and the quality of water environment deterioration.In the prior art, the processing mode of organic sewage is more, and for example: flocculant biological flow bed processing, aerobic and anaerobic biological treatment, chemical agent are handled or the like, but these modes are for high concentration organic sewage, particularly COD
Cr(chemical oxygen demand) high concentration organic sewage more than 10000mg/l, the ubiquity pollutants removal rate is big than the end, facility floor space, the processing cycle is long, processing cost is higher, water quality can not stably reaching standard, easily cause secondary environmental pollution, be difficult to handle in a large number economically deficiency such as high concentration organic sewage.
Summary of the invention
Purpose of the present invention is intended to overcome above-mentioned deficiency of the prior art, integrate the integrated conduct method of modes such as physics, biology, the catalytic oxidant that recycles, electrochemical treatment by employing, thereby a kind of treatment process that can make the high concentration organic sewage that high concentration organic sewage is effectively purified, effluent characteristics stable, the processing cycle is short and processing cost is low efficiently is provided.
Content of the present invention is: a kind of treatment process of high concentration organic sewage comprises:
A. pre-treatment: organic sewage is handled through the desanding slagging-off, removed solids;
B. flocculation sediment separates: add flocculation agent in organic sewage, through stirring, precipitate, filtering, remove filter residue;
It is characterized in that also comprising the following steps:
C. integrated degraded: organic sewage is pumped into the bottom in integrated degraded pond (4) and relies on the pressure of water pump to carry out the uniform mixing that waterpower stirs realization sewage through sump pump (3), flow through whole integrated degraded pond (4) with certain flow velocity then, this integrated degraded pond (4) is one and has that (lattice quantity is 1-n by a plurality of lattices, pollution load on sewage is decided) anaerobic treatment pond (4-1) and the integrated treatment tank formed of catalyzed oxidation pond (4-2), bottom with swash plate (25) precipitation function, integrated degraded pond (4) is built-in with microorganism and catalytic oxidant, be provided with the aeration head (26) that is communicated with gas blower (10) in the catalyzed oxidation pond (4-2), through microbiological deterioration and catalyzing oxidizing degrading, the gases such as methane that produce in anaerobic treatment pond (4-1) concentrate in the water-sealed tank (7) organic sewage in integrated degraded pond (4);
D. electrochemical treatment: each integrated degraded pond (4) is equipped with and is communicated with an electrochemical treater (12), and the organic sewage of discharging from integrated degraded pond (4) enters further electrolytic oxidation degraded the electrochemical treater (12);
E. the sludge incineration catalytic oxidant recycling utilization of holding concurrently: the organic sewage of discharging from electrochemical treater (12) pumps into settling pond (14) precipitate and separate through sump pump (13), sedimentary mud is delivered to filter (17) through slush pump (15) and is filtered, filter residue uses the methane that reclaims in the step c anaerobic degradation to be fuel in converter (8) through slush pump (16), and the organic substance that the contains conversion of burning in the mud, the burned removing of organic pollution materials, catalytic oxidant is got back to original state under reaction conditions, recycle through the catalyzed oxidation pond (4-2) that turns back to integrated degraded pond (4) after pharmacy slot (11) modulation;
F. aftertreatment: the interior organic sewage of settling pond (14) is sent into by aftertreatment pond (18), aftertreatment pond (18) is built-in with microorganism, organic sewage enters further electrolytic oxidation degraded of an electrochemical treater (20) in aftertreatment pond (18) after microbiological deterioration, the organic sewage of discharging from electrochemical treater (20) pumps into settling pond (22) precipitate and separate through sump pump (21), gives off water up to standard (or recycling use) through settling pond (22) post precipitation; The sedimentary mud of settling pond (22) returns settling pond (14) through slush pump (23) and focuses on.Organic sewage through aftertreatment is degraded to COD
CrIn the scope of=20-100mg/l, meet the discharging or the cyclically utilizing standard of national regulation.
In the content of the present invention: can carry out adjustable reflux cycle by sump pump (5) and pipeline between bottom, the described catalyzed oxidation of step c pond (4-2) and the inlet area, anaerobic treatment pond (4-1); The upflow velocity that refluxes be 1-5 rice/hour, thereby regulate the efficient of upflow velocity control anaerobic digestion that the waterpower of anaerobic zone could be regulated and control to return flow.
In the content of the present invention: the integrated degraded pond (4) of described combination-electrochemical treater (12) can according to the pollution load setting of processed sewage, can be handled COD to high concentration organic sewage for 1 cover or the number cover of serial or parallel connection
CrWithin the scope of=500-2000mg/l.
In the content of the present invention: the tail gas that the described converter of step e (8) is discharged is through wet cleaner (24) dedusting washing back emptying, and the sewage of washing tail gas returns in the integrated degraded pond (4), thereby eliminates tail gas pollution.
In the content of the present invention: the microorganism described in step c and the step f can for anerobe, cellulose-decomposing bacteria, nitrifier, enzyme, ammonifying bacteria, the microorganism of using in the prior art such as polyP bacteria, its concentration can be the 50-70 mg/litre.
In the content of the present invention: the upflow velocity of organic sewage in described integrated degraded pond (4) be 1-5 rice/hour.
In the content of the present invention: the upflow velocity of organic sewage in described aftertreatment pond (18) be 1-5 rice/hour.
In the content of the present invention: described aftertreatment pond (18) can be made up of transition zone (18-1), anaerobic zone (18-2) and oxidation zone (18-3), is provided with the aeration head (28) that is communicated with gas blower (27) in the oxidation zone (18-3).
In the content of the present invention: the catalytic oxidant described in the step c can be manganous sulfate and magnesian mixture, its concentration can be 1-5 kg/ton organic sewage, also can be that other that use in the prior art is used for for example inorganic salt etc. of iron content, copper of catalytic oxidant that organic sewage handles.
In the content of the present invention: can carry out adjustable reflux cycle by sump pump (19) and pipeline between the interior oxidation zone in described aftertreatment pond (18) (18-3) bottom and transition zone (18-1) inlet area; The upflow velocity that refluxes be 1-5 rice/hour.
In the content of the present invention: described electrochemical treater (12), electrochemical treater (20) have that number of patent application is 03250448.9 or 200520004320.0, invention and created name is the 26S Proteasome Structure and Function described in the utility application file of " a kind of filling electrode waste disposal plant with katalysis ", the artificial yellow Shang Xun of application.Also can adopt apparatus for electrochemical treatment of the prior art.
In the content of the present invention: concentrate on gases such as methane in the water-sealed tank 7 and both can be used as fuel the organic pollution materials burning is removed, made catalytic oxidant get back to original state, also can be used as the clean energy that the user uses.
Compared with prior art, the present invention has following characteristics and beneficial effect:
(1) adopts the present invention, the dual-use function that has microbiological deterioration and catalyzing oxidizing degrading in integrated degraded pond simultaneously, and possesses quite effectively cohesion, its degradation capability is considerably beyond the Degradation (through measuring, the degradation rate of unit time unit volume has improved 10-20 doubly) of general bio-oxidation pond; Integrated degraded pond-electrochemical treater combination can be handled COD to high concentration organic sewage
Cr=500-2000mg/l; The hold concurrently process of catalytic oxidant recycling utilization of sludge incineration only consumes a spot of recovery methane and just can reach secondary pollution and the catalytic oxidant regenerated dual purpose of eliminating excess sludge, not only eliminated secondary pollution, and greatly reduce the load of microbiological deterioration and the consumption of processing catalytic oxidant, greatly reduce the floor space and the construction investment of processing cost and treatment unit; Organic sewage further is degraded to COD through aftertreatment
CrIn the scope of=20-100mg/l, promptly meet national " integrated wastewater discharge standard " through the settling pond post precipitation, but qualified discharge or cyclically utilizing;
(2) the present invention organically is integrated in one modes such as physics, biology, chemistry (catalytic oxidant that recycles), electrochemical treatment, can make efficiently that high concentration organic sewage is effectively purified, effluent characteristics is stable, the processing cycle is short, processing cost is low;
(3) adopt the recyclable a large amount of clean energies such as methane of the present invention, the discharging of non-secondary pollution thing, reduced investment, take up an area of less, at the bottom of the running cost, treatment capacity is changeable, efficient is high, practical, have significant social, economy and ecological benefits.
Description of drawings
Fig. 1 is the process flow sheet of the embodiment of the invention.
Among the figure: the 1-flocculation basin, the 2-slush pump, the 3-sump pump, the integrated degraded of 4-pond, the 5-sump pump, the 6-filter, the 7-water-sealed tank, the 8-converter, the 9-compound pump, the 10-gas blower, the 11-pharmacy slot, the 12-electrochemical treater, the 13-sump pump, the 14-settling pond, the 15-slush pump, the 16-slush pump, the 17-filter, 18-aftertreatment pond, the 19-sump pump, the 20-electrochemical treater, the 21-sump pump, the 22-settling pond, the 23-slush pump, the 24-wet cleaner, the 25-swash plate, the 26-aeration head, the 27-gas blower, the 28-aeration head.
Embodiment
Also the invention will be further described in conjunction with the accompanying drawings below by embodiment:
Embodiment 1: referring to accompanying drawing.
A kind of treatment process of high concentration organic sewage, mainly form by the following step:
A. pre-treatment: organic sewage is handled through the desanding slagging-off, removed solids; The one-level treatment facility that comprises common needs in the pre-treatment flow process, as coarse rack, fine fack, settling pit or the like, these equipment can design according to the particular case of implementing enterprise's sewage;
B. flocculation sediment separates: add flocculation agent (for example polyacrylamide, silica gel etc., with the flocculation agent that uses in the prior art) in organic sewage, through stirring, precipitation, filtering, remove filter residue;
At first enter flocculation basin 1 through the organic sewage after the desanding slagging-off, carry out preliminary flocculation sediment here and separate, so that reclaim utilizable useful matter (for example protein) or the like in the sewage; Flocculation basin 1 can be made up of stirring reaction district and settling region two portions, sewage is in stirring area and medicament (being flocculation agent) hybrid reaction generation cohesion, enter the mud that the settling region precipitate and separate condenses out then, these mud are transported to automatic discharging and filtering machine through slush pump 2 and filter, filtrate is returned the settling region of flocculation basin 1, and filter residue is packed afterwards through further processing (for example dry) and sold;
C. integrated degraded: organic sewage is pumped into the bottom in integrated degraded pond 4 and relies on the pressure of water pump to carry out the uniform mixing that waterpower stirs realization sewage through sump pump 3, flow through whole integrated degraded pond 4 with certain flow velocity (upflow velocity be 1-5 rice/hour) then, majority of organic pollutants is effectively degraded in this process, this integrated degraded pond 4 is one and has that (lattice quantity can be 1-n by 4 lattices, pollution load on sewage is decided) anaerobic treatment pond 4-1 and the integrated treatment tank formed of bottom catalyzed oxidation pond 4-2 with swash plate 25 precipitation functions, integrated degraded pond 4 is built-in with microorganism and catalytic oxidant, be provided with the aeration head 26 that is communicated with gas blower 10 in the 4-2 of catalyzed oxidation pond, through microbiological deterioration and catalyzing oxidizing degrading, the gases such as methane that produce in the 4-1 of anaerobic treatment pond concentrate on (as the fuel of subsequent handling or the clean energy of user's use) in the water-sealed tank 7 to organic sewage in integrated degraded pond 4; The microbiological deterioration that has simultaneously in the integrated degraded pond 4 and the dual-use function of catalyzing oxidizing degrading, and possesses quite effectively cohesion, so its degradation capability is considerably beyond the Degradation (through measuring, the degradation rate of unit time unit volume has improved 10-20 doubly) of general bio-oxidation pond; Integrated degraded pond 4 has mud and the isolating function of sewage simultaneously, so anaerobic degrading pool no longer needs triphase separator;
Carry out adjustable reflux cycle by sump pump 5 and pipeline between described catalyzed oxidation pond 4-2 bottom and the 4-1 inlet area, anaerobic treatment pond; The upflow velocity that refluxes be 1-5 rice/hour, thereby regulate the efficient of upflow velocity control anaerobic digestion that the waterpower of anaerobic zone could be regulated and control to return flow.
D. electrochemical treatment: each integrated degraded pond 4 is equipped with also and is communicated with an electrochemical treater 12, forms an organic whole, and 4 organic sewages of discharging enter the electrochemical treater 12 further electrolytic oxidation and degrade from integrated degraded pond;
The integrated degraded pond 4-electrochemical treater 12 of combination is 1 cover or the number cover of serial or parallel connection, according to the pollution load setting of processed sewage, can handle COD to high concentration organic sewage
CrWithin the scope of=500-2000mg/l.
E. the sludge incineration catalytic oxidant recycling utilization of holding concurrently: the organic sewage of discharging from electrochemical treater 12 pumps into settling pond 14 precipitate and separate through sump pump 13, sedimentary mud is delivered to filter 17 through slush pump 15 and is filtered, filter residue uses the methane that reclaims in the step c anaerobic degradation to be fuel in converter 8 through slush pump 16, and the organic substance that the contains conversion of burning in the mud, the burned removing of organic pollution materials, catalytic oxidant is got back to original state under reaction conditions, recycle through the catalyzed oxidation pond 4-2 that turns back to integrated degraded pond 4 after pharmacy slot 11 modulation; So the catalytic oxidant in this sewage treatment process does not consume basically, has only a spot of circulation loss;
The tail gas that converter 8 is discharged can be eliminated tail gas pollution through wet cleaner 24 dedustings washing back emptying, and the sewage of washing tail gas returns in the integrated degraded pond 4, thereby eliminates tail gas pollution.
The employing of this processing step, only consume a spot of recovery methane and just reached secondary pollution and the catalytic oxidant regenerated dual purpose of eliminating excess sludge, not only eliminated secondary pollution, and greatly reduce the load of microbiological deterioration and the consumption of processing catalytic oxidant, greatly reduce the floor space and the construction investment of processing cost and treatment unit;
F. aftertreatment: organic sewage in the settling pond 14 is sent into by aftertreatment pond 18, and aftertreatment pond 18 is made up of transition zone 18-1, anaerobic zone 18-2 and oxidation zone 18-3, is provided with the aeration head 28 that is communicated with gas blower 27 in the oxidation zone 18-3; Aftertreatment pond 18 is built-in with microorganism, organic sewage (organic sewage described aftertreatment pond 18 upflow velocity be 1-5 rice/hour) after microbiological deterioration, enter the 20 further electrolytic oxidations degradeds of an electrochemical treater in aftertreatment pond 18, the organic sewage of discharging from electrochemical treater 20 pumps into settling pond 22 precipitate and separate through sump pump 21, gives off water up to standard (or recycling use) through settling pond 22 post precipitations; Organic sewage is degraded to COD in aftertreatment pond 18
Cr=100-300mg/l further is degraded to COD then in electrochemical treater 20
CrIn the scope of=20-100mg/l; Settling pond 22 sedimentary mud return settling pond 14 through slush pump 23 and focus on.Organic sewage through aftertreatment is degraded to COD
CrIn the scope of=20-100mg/l, meet national specified discharge standard.
Carry out adjustable reflux cycle by sump pump 19 and pipeline between oxidation zone 18-3 bottom and the transition zone 18-1 inlet area in the described aftertreatment pond 18; The upflow velocity that refluxes be 1-5 rice/hour.
Microorganism described in step c and the step f be anerobe, cellulose-decomposing bacteria, nitrifier, enzyme, ammonifying bacteria, the microorganism of using in the prior art such as polyP bacteria, its concentration can be the 50-70 mg/litre.
Catalytic oxidant described in the step c can be for manganous sulfate or/and magnesium oxide, its concentration can be 1-5 kg/ton organic sewage, also can be that other that use in the prior art is used for for example inorganic salt etc. of iron content, copper of catalytic oxidant that organic sewage handles.
Described electrochemical treater 12, electrochemical treater 20 have that number of patent application is 03250448.9 or 200520004320.0, invention and created name is the 26S Proteasome Structure and Function described in the utility application file of " a kind of filling electrode waste disposal plant with katalysis ", the artificial yellow Shang Xun of application.
High concentration organic sewage meets " integrated wastewater discharge standard " of country after present embodiment is handled, and can recycling use.
This embodiment is used for the direct processing (reclaiming without alkali) of black liquid, the COD of black liquid
Cr=25000-50000mg/l, treatment capacity 1500m
3/ day, the water COD after the processing
Cr=30-80mg/l.
This embodiment is used to produce per year the alcohol waste water processing of 50000 tons of alcohol, the COD of waste water before handling
Cr=60000-80000mg/l, treatment capacity 2500m
3/ day, the water COD after the processing
Cr=30-80mg/l has obtained good effect.
The invention is not restricted to this embodiment, content of the present invention is described all can implement and have described good result.
Claims (10)
1, a kind of treatment process of high concentration organic sewage comprises:
A. pre-treatment: organic sewage is handled through the desanding slagging-off, removed solids;
B. flocculation sediment separates: add flocculation agent in organic sewage, through stirring, precipitate, filtering, remove filter residue;
It is characterized in that also comprising the following steps:
C. integrated degraded: organic sewage is pumped into the bottom in integrated degraded pond (4) and relies on the pressure of water pump to carry out the uniform mixing that waterpower stirs realization sewage through sump pump (3), flow through whole integrated degraded pond (4) with certain flow velocity then, this integrated degraded pond (4) is one and has the integrated treatment tank that the catalyzed oxidation pond (4-2) that has swash plate (25) precipitation function by the anaerobic treatment pond (4-1) of a plurality of lattices and bottom is formed, integrated degraded pond (4) is built-in with microorganism and catalytic oxidant, be provided with the aeration head (26) that is communicated with gas blower (10) in the catalyzed oxidation pond (4-2), through microbiological deterioration and catalyzing oxidizing degrading, the gases such as methane that produce in anaerobic treatment pond (4-1) concentrate in the water-sealed tank (7) organic sewage in integrated degraded pond (4);
D. electrochemical treatment: each integrated degraded pond (4) is equipped with and is communicated with an electrochemical treater (12), and the organic sewage of discharging from integrated degraded pond (4) enters further electrolytic oxidation degraded the electrochemical treater (12);
E. the sludge incineration catalytic oxidant recycling utilization of holding concurrently: the organic sewage of discharging from electrochemical treater (12) pumps into settling pond (14) precipitate and separate through sump pump (13), sedimentary mud is delivered to filter (17) through slush pump (15) and is filtered, filter residue uses the methane that reclaims in the step c anaerobic degradation to be fuel in converter (8) through slush pump (16), and the organic substance that the contains conversion of burning in the mud, the burned removing of organic pollution materials, catalytic oxidant is got back to original state under reaction conditions, recycle through the catalyzed oxidation pond (4-2) that turns back to integrated degraded pond (4) after pharmacy slot (11) modulation;
F. aftertreatment: the interior organic sewage of settling pond (14) is sent into by aftertreatment pond (18), aftertreatment pond (18) is built-in with microorganism, organic sewage enters further electrolytic oxidation degraded of an electrochemical treater (20) in aftertreatment pond (18) after microbiological deterioration, the organic sewage of discharging from electrochemical treater (20) pumps into settling pond (22) precipitate and separate through sump pump (21), gives off water up to standard through settling pond (22) post precipitation; The sedimentary mud of settling pond (22) returns settling pond (14) through slush pump (23) and focuses on.
2, by the treatment process of the described high concentration organic sewage of claim 1, it is characterized in that: carry out adjustable reflux cycle by sump pump (5) and pipeline between bottom, the described catalyzed oxidation of step c pond (4-2) and the inlet area, anaerobic treatment pond (4-1).
3, by the treatment process of the described high concentration organic sewage of claim 1, it is characterized in that: the integrated degraded pond (4) of combination-electrochemical treater (12) is 1 cover or the number cover of serial or parallel connection.
4, by the treatment process of the described high concentration organic sewage of claim 1, it is characterized in that: the tail gas that the described converter of step e (8) is discharged is through wet cleaner (24) dedusting washing back emptying, and the sewage of washing tail gas returns in the integrated degraded pond (4).
5, by the treatment process of the described high concentration organic sewage of claim 1, it is characterized in that: the microorganism described in step c and the step f be anerobe, cellulose-decomposing bacteria, nitrifier, enzyme, ammonifying bacteria, polyP bacteria, its concentration can be the 50-70 mg/litre.
6, by the treatment process of the described high concentration organic sewage of claim 1, it is characterized in that: the upflow velocity of organic sewage in described integrated degraded pond (4) be 1-5 rice/hour.
7, by the treatment process of the described high concentration organic sewage of claim 1, it is characterized in that: the upflow velocity of organic sewage in described aftertreatment pond (18) be 1-5 rice/hour.
8, press the treatment process of the described high concentration organic sewage of claim 1, it is characterized in that: described aftertreatment pond (18) is made up of transition zone (18-1), anaerobic zone (18-2) and oxidation zone (18-3), is provided with the aeration head (28) that is communicated with gas blower (27) in the oxidation zone (18-3).
9, by the treatment process of the described high concentration organic sewage of claim 1, it is characterized in that: the catalytic oxidant described in the step c is a manganous sulfate or/and magnesium oxide, and its concentration is 1-5 kg/ton organic sewage.
10, by the treatment process of the described high concentration organic sewage of claim 8, it is characterized in that: carry out adjustable reflux cycle by sump pump (19) and pipeline between the interior oxidation zone in described aftertreatment pond (18) (18-3) bottom and transition zone (18-1) inlet area.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006100204540A CN100368324C (en) | 2006-03-09 | 2006-03-09 | Method for treating high concentration organic waste water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006100204540A CN100368324C (en) | 2006-03-09 | 2006-03-09 | Method for treating high concentration organic waste water |
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| CN1821128A true CN1821128A (en) | 2006-08-23 |
| CN100368324C CN100368324C (en) | 2008-02-13 |
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| CNB2006100204540A Expired - Fee Related CN100368324C (en) | 2006-03-09 | 2006-03-09 | Method for treating high concentration organic waste water |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100415338C (en) * | 2007-06-01 | 2008-09-03 | 华电水处理技术工程有限公司 | Method and equipment for purifying recirculated cooling water or town B-grade sewage |
| CN100460348C (en) * | 2007-03-16 | 2009-02-11 | 嘉兴市新大众印染有限公司 | Method for treating and reclaiming wastewater of polyester piece goods dyeing and finishing |
| CN102010107A (en) * | 2010-12-24 | 2011-04-13 | 波鹰(厦门)科技有限公司 | Treatment and cyclic utilization device and method of tannery wastewater |
| CN102701519A (en) * | 2012-05-17 | 2012-10-03 | 杭州共创环保科技有限公司 | Method for ecological control on black-odor watercourse by combining electrochemistry with biology |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP3267935B2 (en) * | 1997-12-19 | 2002-03-25 | 神鋼パンテツク株式会社 | Method and apparatus for treating organic wastewater |
| CN1257853C (en) * | 2003-10-30 | 2006-05-31 | 中国石油化工股份有限公司 | Method for treating or ganic waste water with nigh concentration |
| CN1631818A (en) * | 2003-12-23 | 2005-06-29 | 何义亮 | Organic waste water treatment process |
| CN1270985C (en) * | 2004-06-08 | 2006-08-23 | 武汉化工学院 | Anaerobic treating process for high concentration organic waste water |
| CN100334017C (en) * | 2005-03-10 | 2007-08-29 | 华东理工大学 | BCB combination process of treating organic waste water |
-
2006
- 2006-03-09 CN CNB2006100204540A patent/CN100368324C/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100460348C (en) * | 2007-03-16 | 2009-02-11 | 嘉兴市新大众印染有限公司 | Method for treating and reclaiming wastewater of polyester piece goods dyeing and finishing |
| CN100415338C (en) * | 2007-06-01 | 2008-09-03 | 华电水处理技术工程有限公司 | Method and equipment for purifying recirculated cooling water or town B-grade sewage |
| CN102010107A (en) * | 2010-12-24 | 2011-04-13 | 波鹰(厦门)科技有限公司 | Treatment and cyclic utilization device and method of tannery wastewater |
| CN102010107B (en) * | 2010-12-24 | 2011-12-28 | 波鹰(厦门)科技有限公司 | Treatment and cyclic utilization device and method of tannery wastewater |
| CN102701519A (en) * | 2012-05-17 | 2012-10-03 | 杭州共创环保科技有限公司 | Method for ecological control on black-odor watercourse by combining electrochemistry with biology |
| CN102701519B (en) * | 2012-05-17 | 2013-09-04 | 杭州共创环保科技有限公司 | Method for ecological control on black-odor watercourse by combining electrochemistry with biology |
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| CN100368324C (en) | 2008-02-13 |
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