CN103663880A - Method for treating sewage by biofilm technology - Google Patents
Method for treating sewage by biofilm technology Download PDFInfo
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- CN103663880A CN103663880A CN201310729630.8A CN201310729630A CN103663880A CN 103663880 A CN103663880 A CN 103663880A CN 201310729630 A CN201310729630 A CN 201310729630A CN 103663880 A CN103663880 A CN 103663880A
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- sewage
- pond
- water
- basin
- sludge
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- 239000010865 sewage Substances 0.000 title claims abstract description 78
- 238000000034 method Methods 0.000 title claims abstract description 42
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 68
- 239000010802 sludge Substances 0.000 claims abstract description 32
- 238000004519 manufacturing process Methods 0.000 claims abstract description 10
- 238000000926 separation method Methods 0.000 claims abstract description 8
- 239000011259 mixed solution Substances 0.000 claims abstract description 6
- 238000005345 coagulation Methods 0.000 claims description 18
- 230000015271 coagulation Effects 0.000 claims description 18
- 238000005189 flocculation Methods 0.000 claims description 15
- 230000016615 flocculation Effects 0.000 claims description 15
- 239000003795 chemical substances by application Substances 0.000 claims description 14
- 238000005273 aeration Methods 0.000 claims description 10
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 10
- 239000001301 oxygen Substances 0.000 claims description 10
- 229910052760 oxygen Inorganic materials 0.000 claims description 10
- 239000002699 waste material Substances 0.000 claims description 7
- 238000010521 absorption reaction Methods 0.000 claims description 6
- 239000003610 charcoal Substances 0.000 claims description 6
- 238000005202 decontamination Methods 0.000 claims description 6
- 230000003588 decontaminative effect Effects 0.000 claims description 6
- 238000001914 filtration Methods 0.000 claims description 6
- 239000007788 liquid Substances 0.000 claims description 6
- 239000002957 persistent organic pollutant Substances 0.000 claims description 6
- 229920002401 polyacrylamide Polymers 0.000 claims description 5
- 238000010992 reflux Methods 0.000 claims description 5
- 125000000129 anionic group Chemical group 0.000 claims description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 10
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 abstract description 6
- 230000000694 effects Effects 0.000 abstract description 6
- 238000004062 sedimentation Methods 0.000 abstract description 5
- 239000006004 Quartz sand Substances 0.000 abstract description 2
- 206010021143 Hypoxia Diseases 0.000 abstract 3
- 230000002708 enhancing effect Effects 0.000 abstract 2
- 230000001146 hypoxic effect Effects 0.000 abstract 2
- 238000011001 backwashing Methods 0.000 abstract 1
- 239000008394 flocculating agent Substances 0.000 abstract 1
- 238000000265 homogenisation Methods 0.000 abstract 1
- 239000000945 filler Substances 0.000 description 8
- 230000001376 precipitating effect Effects 0.000 description 4
- 239000010453 quartz Substances 0.000 description 4
- 238000004065 wastewater treatment Methods 0.000 description 4
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- 238000006213 oxygenation reaction Methods 0.000 description 3
- 239000002028 Biomass Substances 0.000 description 2
- 238000006424 Flood reaction Methods 0.000 description 2
- 230000005540 biological transmission Effects 0.000 description 2
- 230000004060 metabolic process Effects 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- JLVVSXFLKOJNIY-UHFFFAOYSA-N Magnesium ion Chemical compound [Mg+2] JLVVSXFLKOJNIY-UHFFFAOYSA-N 0.000 description 1
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 1
- 238000006701 autoxidation reaction Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 229910001425 magnesium ion Inorganic materials 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Images
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- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The invention discloses a method for treating sewage by a biofilm technology. The method comprises the following steps: (1) first-stage treatment: enabling living sewage, production sewage and pretreated cyanogens-containing sewage to enter a homogenization adjustment basin after the living sewage, the production sewage and the pretreated cyanogens-containing sewage are subjected to sewage removal through a mechanical grid and an artificial grid; (2) second-stage treatment: lifting the sewage into a hypoxic-aerobiotic basin through a sewage lifting pump, wherein the sewage lifting pump comprises a hypoxic basin and an aerobiotic basin, enabling the sewage subjected to the first-stage treatment to enter from the hypoxic basin to the aerobiotic basin, and feeding a flocculating agent at the water outlet end of the aerobiotic basin; (3) third-stage treatment: enabling sludge and water mixed solution subjected to the second-stage treatment to enter a secondary sedimentation basin for sludge and water separation, and treating and utilizing water discharged by the secondary sedimentation basin through an advanced treatment system. The method for treating the sewage by the biofilm technology has the characteristics of enhancing the sewage treatment effect, enhancing the sedimentation effect of the secondary sedimentation basin, relieving the load on the advanced treatment system and reducing the backwashing frequency of a quartz sand filter and an activated carbon filter.
Description
Technical field
The invention belongs to environmental technology field, specifically relate to a kind of method that biomembrance process is disposed of sewage.
Background technology
Production waste that each production equipment discharges and the sanitary sewage of on-site are received and processed to generalization plant effuent treatment station, and the clear water after processing is as circulating water system, de-mineralized water reuse water, and on-the-spot greenings etc., to realize water-saving and emission-reducing, energy-saving and cost-reducing.Ammonia nitrogen concentration for water inlet is higher, adopts the contact oxidation method of adding filler.Biological contact oxidation process is a kind of bio membrane process between activated sludge process and biological filter, be characterized in arranging filler in pond, at the bottom of pond, aeration carries out oxygenation to sewage, and make body interior sewage in pond in flow state, to guarantee that sewage fully contacts with the filler in pond, avoid existing sewage to contact uneven defect with filler in biological contact oxidation pond.
In prior art, biomembrance process: A/O(aerobic/anaerobic) filled biomass carrier (filler) in pond, sewage floods filler, at the bottom of pond, pass into air aeration, oxygenation, stirring, three relative current contacts, transmission, by the biomembranous metabolism of filling surface, be purified sewage.But due to the liquid that enters second pond, often calcium, magnesium ion state are more, water yield load impact or long-term excess load; Because short stream has reduced the residence time, so that flco flows out effluent weir before sedimentation; Aeration tank active sludge excess aeration, makes mud autoxidation and disintegrates, and will produce following drawback like this:
1, second pond, flocculation tank, clean water basin water outlet muddiness, wastewater treatment efficiency is undesirable.
2, second pond sludge settling weak effect, system sludge is difficult for draining into sludge sump.
3, advanced treatment system load is heavier, and quartz sand and gac life cycle are short, high with changing frequency.
4, quartz filter and activated charcoal filter backwash frequency are high, and backwash water enters Sewage treatment systems again, cause sewage load to increase.
Summary of the invention
The object of the invention is to overcome above-mentioned shortcoming and a kind of wastewater treatment efficiency that can improve is provided, improve second pond effect of settling, alleviate advanced treatment system load, the method that the biomembrance process of reduction quartz filter and activated charcoal filter backwash frequency is disposed of sewage.
The method that a kind of biomembrance process of the present invention is disposed of sewage, comprises the steps:
(1) coagulation: sanitary sewage, production waste and pretreated cyanogens-containing sewage water are entered to homogeneous equalizing tank after mechanical grille and artificial grid decontamination;
(2) second-stage treatment: rise to anaerobic-aerobic pond with sewage pump, anaerobic-aerobic pond comprises anoxic pond and Aerobic Pond, sewage through coagulation enters pond, aerobic zone from pond, oxygen-starved area, wherein dissolved oxygen in anoxic tank concentration is controlled at 0.3～0.5mg/l, return current ratio of the mixed liquid is controlled at 200～500%, and sewage stops 1～2h; The Dissolved Oxygen concentration Control of Aerobic Pond is at 2～3mg/l, aeration time 4～8h, and return sludge ratio, 50～100%, is removed the organic pollutant in sewage by the biochemical treatment of anaerobic-aerobic pond; And add flocculation agent in Aerobic Pond water side;
(3) tertiary treatment: muddy water mixed solution enters second pond and carries out mud-water separation after second-stage treatment, the water outlet of second pond is processed, is utilized through advanced treatment system, second pond mud enters mud-collecting well and partly delivers to anoxic pond by sludge reflux pump, to guarantee sludge concentration, excess sludge enters sludge sump.
The method that above-mentioned biomembrance process is disposed of sewage, wherein: described flocculation agent is that concentration is 0.5～1 ‰ zwitter-ion or anionic polyacrylamide.
The method that above-mentioned biomembrance process is disposed of sewage, wherein: described flocculation agent adds by volume pump.
The method that above-mentioned biomembrance process is disposed of sewage, wherein: in described anoxic pond, stirrer is set.
The method that above-mentioned biomembrance process is disposed of sewage, wherein: described advanced treatment system through coagulation, filtration, the laggard clean water basin of charcoal absorption, is delivered to desalted water station reuse by tail water lift pump by the water outlet of second pond.
The present invention compares with prior art, there is obvious beneficial effect, from above scheme, coagulation: sanitary sewage, production waste and pretreated cyanogens-containing sewage water are entered to homogeneous equalizing tank after mechanical grille and artificial grid decontamination, mainly by physical means, to reach the object of suspended substance in Separation of Water, even water quality, for follow-up biochemical treatment creates conditions.Second-stage treatment: rise to anaerobic-aerobic pond with sewage pump, anaerobic-aerobic pond comprises anoxic pond and Aerobic Pond, sewage through coagulation enters pond, aerobic zone from pond, oxygen-starved area, filled biomass carrier (filler) in anaerobic-aerobic pond, sewage floods filler, passes into air aeration at the bottom of pond, oxygenation, stirring, three relative current contacts, transmission, by the biomembranous metabolism of filling surface, remove the organic pollutant in sewage, sewage is purified.In anoxic pond, be provided with stirrer, can prevent that mud from precipitating in anoxic pond.In Aerobic Pond water side, add flocculation agent and improve wastewater treatment efficiency, can improve second pond effect of settling, alleviate advanced treatment system load, reduce quartz filter and activated charcoal filter backwash frequency.Flocculation agent adds by volume pump, by dosage, regulates second pond water outlet clarity.Tertiary treatment: second pond carries out mud-water separation, advanced treatment system through coagulation, filtration, the laggard clean water basin of charcoal absorption, is delivered to desalted water station reuse by tail water lift pump by the water outlet of second pond, completes the processing of sewage.In a word, the present invention has raising wastewater treatment efficiency, improves second pond effect of settling, alleviates advanced treatment system load, reduces the feature of quartz filter and activated charcoal filter backwash frequency.
attached body explanation
Fig. 1 is process flow sheet of the present invention.
Embodiment
embodiment 1
Referring to Fig. 1, a kind of method that biomembrance process is disposed of sewage, comprises the steps:
(1) coagulation: sanitary sewage, production waste and pretreated cyanogens-containing sewage water are entered to homogeneous equalizing tank after mechanical grille and artificial grid decontamination;
(2) second-stage treatment: rise to anaerobic-aerobic pond with sewage pump, anaerobic-aerobic pond comprises anoxic pond and Aerobic Pond, sewage through coagulation enters pond, aerobic zone from pond, oxygen-starved area, stirrer is set in anoxic pond, prevent that mud from precipitating in anoxic pond, wherein dissolved oxygen in anoxic tank concentration is controlled at 0.3mg/l, and return current ratio of the mixed liquid is controlled at 200%, and sewage stops 1h; The Dissolved Oxygen concentration Control of Aerobic Pond is at 2/l, aeration time 4h, and return sludge ratio, 50%, is removed the organic pollutant in sewage by the biochemical treatment of anaerobic-aerobic pond; And in Aerobic Pond water side, by volume pump, add flocculation agent, flocculation agent is that concentration is 0.5 ‰ zwitter-ion polyacrylamide;
(3) tertiary treatment: muddy water mixed solution enters second pond and carries out mud-water separation after second-stage treatment, the water outlet of second pond is processed through advanced treatment system, advanced treatment system through coagulation, filtration, the laggard clean water basin of charcoal absorption, is delivered to desalted water station reuse by tail water lift pump by the water outlet of second pond; Second pond mud enters mud-collecting well and partly delivers to anoxic pond by sludge reflux pump, and to guarantee sludge concentration, excess sludge enters sludge sump.
embodiment 2
Referring to Fig. 1, a kind of method that biomembrance process is disposed of sewage, comprises the steps:
(1) coagulation: sanitary sewage, production waste and pretreated cyanogens-containing sewage water are entered to homogeneous equalizing tank after mechanical grille and artificial grid decontamination;
(2) second-stage treatment: rise to anaerobic-aerobic pond with sewage pump, anaerobic-aerobic pond comprises anoxic pond and Aerobic Pond, sewage through coagulation enters pond, aerobic zone from pond, oxygen-starved area, stirrer is set in anoxic pond, prevent that mud from precipitating in anoxic pond, wherein dissolved oxygen in anoxic tank concentration is controlled at 0.4mg/l, and return current ratio of the mixed liquid is controlled at 300%, and sewage stops 1.5h; The Dissolved Oxygen concentration Control of Aerobic Pond is at 2.5mg/l, aeration time 6h, and return sludge ratio, 75%, is removed the organic pollutant in sewage by the biochemical treatment of anaerobic-aerobic pond; And in Aerobic Pond water side, by volume pump, add flocculation agent, flocculation agent is that concentration is 1 ‰ zwitter-ion polyacrylamide;
(3) tertiary treatment: muddy water mixed solution enters second pond and carries out mud-water separation after second-stage treatment, the water outlet of second pond is processed through advanced treatment system, advanced treatment system through coagulation, filtration, the laggard clean water basin of charcoal absorption, is delivered to desalted water station reuse by tail water lift pump by the water outlet of second pond; Second pond mud enters mud-collecting well and partly delivers to anoxic pond by sludge reflux pump, and to guarantee sludge concentration, excess sludge enters sludge sump.
embodiment 3
Referring to Fig. 1, a kind of method that biomembrance process is disposed of sewage, comprises the steps:
(1) coagulation: sanitary sewage, production waste and pretreated cyanogens-containing sewage water are entered to homogeneous equalizing tank after mechanical grille and artificial grid decontamination;
(2) second-stage treatment: rise to anaerobic-aerobic pond with sewage pump, anaerobic-aerobic pond comprises anoxic pond and Aerobic Pond, sewage through coagulation enters pond, aerobic zone from pond, oxygen-starved area, stirrer is set in anoxic pond, prevent that mud from precipitating in anoxic pond, wherein dissolved oxygen in anoxic tank concentration is controlled at 0.5mg/l, and return current ratio of the mixed liquid is controlled at 500%, and sewage stops 2h; The Dissolved Oxygen concentration Control of Aerobic Pond is at 3mg/l, aeration time 8h, and return sludge ratio, 100%, is removed the organic pollutant in sewage by the biochemical treatment of anaerobic-aerobic pond; And in Aerobic Pond water side, by volume pump, add flocculation agent, flocculation agent is that concentration is 1 ‰ anionic polyacrylamide;
(3) tertiary treatment: muddy water mixed solution enters second pond and carries out mud-water separation after second-stage treatment, the water outlet of second pond is processed through advanced treatment system, advanced treatment system through coagulation, filtration, the laggard clean water basin of charcoal absorption, is delivered to desalted water station reuse by tail water lift pump by the water outlet of second pond; Second pond mud enters mud-collecting well and partly delivers to anoxic pond by sludge reflux pump, and to guarantee sludge concentration, excess sludge enters sludge sump.
The above, it is only preferred embodiment of the present invention, not the present invention is done to any pro forma restriction, any technical solution of the present invention content that do not depart from, any simple modification, equivalent variations and the modification above embodiment done according to technical spirit of the present invention, all still belong in the scope of technical solution of the present invention.
Claims (5)
1. the method that biomembrance process is disposed of sewage, comprises the steps:
(1) coagulation: sanitary sewage, production waste and pretreated cyanogens-containing sewage water are entered to homogeneous equalizing tank after mechanical grille and artificial grid decontamination;
(2) second-stage treatment: rise to anaerobic-aerobic pond with sewage pump, anaerobic-aerobic pond comprises anoxic pond and Aerobic Pond, sewage through coagulation enters pond, aerobic zone from pond, oxygen-starved area, wherein dissolved oxygen in anoxic tank concentration is controlled at 0.3～0.5mg/l, return current ratio of the mixed liquid is controlled at 200～500%, and sewage stops 1～2h; The Dissolved Oxygen concentration Control of Aerobic Pond is at 2～3mg/l, aeration time 4～8h, and return sludge ratio, 50～100%, is removed the organic pollutant in sewage by the biochemical treatment of anaerobic-aerobic pond; And add flocculation agent in Aerobic Pond water side;
(3) tertiary treatment: muddy water mixed solution enters second pond and carries out mud-water separation after second-stage treatment, the water outlet of second pond is processed, is utilized through advanced treatment system, second pond mud enters mud-collecting well and partly delivers to anoxic pond by sludge reflux pump, to guarantee sludge concentration, excess sludge enters sludge sump.
2. the method that biomembrance process as claimed in claim 1 is disposed of sewage, is characterized in that: described flocculation agent is that concentration is 0.5～1 ‰ zwitter-ion or anionic polyacrylamide.
3. the method that biomembrance process as claimed in claim 1 or 2 is disposed of sewage, is characterized in that: described flocculation agent adds by volume pump.
4. the method that biomembrance process as claimed in claim 1 or 2 is disposed of sewage, is characterized in that: in described anoxic pond, stirrer is set.
5. the method that biomembrance process as claimed in claim 1 or 2 is disposed of sewage, is characterized in that: described advanced treatment system through coagulation, filtration, the laggard clean water basin of charcoal absorption, is delivered to desalted water station reuse by tail water lift pump by the water outlet of second pond.
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| CN201310729630.8A CN103663880B (en) | 2013-12-26 | 2013-12-26 | A kind of biomembrance process processes the method for sewage |
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| CN201310729630.8A CN103663880B (en) | 2013-12-26 | 2013-12-26 | A kind of biomembrance process processes the method for sewage |
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| CN103663880A true CN103663880A (en) | 2014-03-26 |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108128975A (en) * | 2017-12-28 | 2018-06-08 | 重庆市桑麻环保科技有限公司 | A kind of method for treating rural wastewater |
| CN108314254A (en) * | 2018-03-15 | 2018-07-24 | 贵州中大环境科技有限公司 | A kind of town domestic sewage reflow treatment device |
| CN108503019A (en) * | 2018-03-20 | 2018-09-07 | 清华大学深圳研究生院 | A kind of membrane bioreactor and sewage water treatment method |
| CN109626687A (en) * | 2018-12-06 | 2019-04-16 | 中国矿业大学 | A kind of mine water based on ultrasound freezing desalting system and method |
| CN110642350A (en) * | 2019-09-30 | 2020-01-03 | 天津科技大学 | A kind of deep phosphorus removal method of urban domestic sewage |
| CN111517565A (en) * | 2020-04-16 | 2020-08-11 | 北京博泰至淳生物科技有限公司 | Sewage treatment control method and system for realizing in-situ improvement of treatment scale |
| CN111533363A (en) * | 2020-04-03 | 2020-08-14 | 北京博泰至淳生物科技有限公司 | Sewage treatment method and system for realizing in-situ improvement of treatment scale |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1843981A (en) * | 2005-04-07 | 2006-10-11 | 同济大学 | An integrated sewage suspension carrier biological treatment process |
| CN203159366U (en) * | 2013-03-12 | 2013-08-28 | 贵州天福化工有限责任公司 | Modern coal chemical industry sewage treatment device |
-
2013
- 2013-12-26 CN CN201310729630.8A patent/CN103663880B/en active Active
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1843981A (en) * | 2005-04-07 | 2006-10-11 | 同济大学 | An integrated sewage suspension carrier biological treatment process |
| CN203159366U (en) * | 2013-03-12 | 2013-08-28 | 贵州天福化工有限责任公司 | Modern coal chemical industry sewage treatment device |
Non-Patent Citations (1)
| Title |
|---|
| 马千里等: ""城镇污水处理厂好氧池出水加药絮凝试验"", 《工业用水与废水》, vol. 41, no. 2, 30 April 2010 (2010-04-30), pages 49 - 52 * |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108128975A (en) * | 2017-12-28 | 2018-06-08 | 重庆市桑麻环保科技有限公司 | A kind of method for treating rural wastewater |
| CN108314254A (en) * | 2018-03-15 | 2018-07-24 | 贵州中大环境科技有限公司 | A kind of town domestic sewage reflow treatment device |
| CN108503019A (en) * | 2018-03-20 | 2018-09-07 | 清华大学深圳研究生院 | A kind of membrane bioreactor and sewage water treatment method |
| CN108503019B (en) * | 2018-03-20 | 2024-05-07 | 清华大学深圳研究生院 | Membrane bioreactor and sewage treatment method |
| CN109626687A (en) * | 2018-12-06 | 2019-04-16 | 中国矿业大学 | A kind of mine water based on ultrasound freezing desalting system and method |
| CN110642350A (en) * | 2019-09-30 | 2020-01-03 | 天津科技大学 | A kind of deep phosphorus removal method of urban domestic sewage |
| CN111533363A (en) * | 2020-04-03 | 2020-08-14 | 北京博泰至淳生物科技有限公司 | Sewage treatment method and system for realizing in-situ improvement of treatment scale |
| CN111533363B (en) * | 2020-04-03 | 2022-05-03 | 北京博泰至淳生物科技有限公司 | Sewage treatment method and system for realizing in-situ improvement of treatment scale |
| CN111517565A (en) * | 2020-04-16 | 2020-08-11 | 北京博泰至淳生物科技有限公司 | Sewage treatment control method and system for realizing in-situ improvement of treatment scale |
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| CN103663880B (en) | 2016-08-17 |
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