CN101492229B - Pulling flow type anaerobe reactor - Google Patents
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- CN101492229B CN101492229B CN2009100681134A CN200910068113A CN101492229B CN 101492229 B CN101492229 B CN 101492229B CN 2009100681134 A CN2009100681134 A CN 2009100681134A CN 200910068113 A CN200910068113 A CN 200910068113A CN 101492229 B CN101492229 B CN 101492229B
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- 239000007788 liquid Substances 0.000 claims abstract description 43
- 244000005700 microbiome Species 0.000 claims abstract description 18
- 238000010792 warming Methods 0.000 claims abstract description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 14
- 239000010802 sludge Substances 0.000 claims abstract description 12
- 238000010438 heat treatment Methods 0.000 claims description 11
- 239000000463 material Substances 0.000 claims description 8
- 229910000831 Steel Inorganic materials 0.000 claims description 6
- 239000010959 steel Substances 0.000 claims description 6
- 239000004745 nonwoven fabric Substances 0.000 claims description 4
- 238000010992 reflux Methods 0.000 claims description 4
- 229920000742 Cotton Polymers 0.000 claims description 3
- 238000005260 corrosion Methods 0.000 claims description 3
- 230000007797 corrosion Effects 0.000 claims description 3
- 239000006228 supernatant Substances 0.000 claims description 3
- 229920011532 unplasticized polyvinyl chloride Polymers 0.000 claims description 3
- 238000006243 chemical reaction Methods 0.000 abstract description 13
- 230000000694 effects Effects 0.000 abstract description 12
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 abstract description 8
- 239000010865 sewage Substances 0.000 abstract description 6
- 230000007062 hydrolysis Effects 0.000 abstract description 5
- 238000006460 hydrolysis reaction Methods 0.000 abstract description 5
- 230000014759 maintenance of location Effects 0.000 abstract description 5
- 230000020477 pH reduction Effects 0.000 abstract description 5
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 239000005416 organic matter Substances 0.000 abstract description 4
- 230000008901 benefit Effects 0.000 abstract description 3
- 230000007613 environmental effect Effects 0.000 abstract description 2
- 230000008092 positive effect Effects 0.000 abstract description 2
- 238000000034 method Methods 0.000 description 8
- 238000005516 engineering process Methods 0.000 description 5
- 238000000855 fermentation Methods 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 241001148471 unidentified anaerobic bacterium Species 0.000 description 3
- 238000009360 aquaculture Methods 0.000 description 2
- 244000144974 aquaculture Species 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000009395 breeding Methods 0.000 description 2
- 230000001488 breeding effect Effects 0.000 description 2
- 230000015556 catabolic process Effects 0.000 description 2
- 238000006731 degradation reaction Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000009313 farming Methods 0.000 description 2
- 230000004151 fermentation Effects 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 230000001133 acceleration Effects 0.000 description 1
- 239000012298 atmosphere Substances 0.000 description 1
- 239000000969 carrier Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 239000003673 groundwater Substances 0.000 description 1
- 230000000696 methanogenic effect Effects 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 125000001477 organic nitrogen group Chemical group 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
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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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy
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Abstract
本发明属于农业环保领域,涉及一种用于污水处理的推流式厌氧生物反应器。本发明的推流式厌氧生物反应器,通过以下途径来实现,预处理后的料液输送至增温槽,进行增温,增温后的料液由溢流管进入进料池,再由进料池中的进料口转入反应器内部,料液与反应器内的覆膜载体、浮游厌氧微生物及活性污泥充分接触,然后被推流到水压间,上清液由溢流管排出,污泥则由吸泥车取走。本发明的优点和积极效果:增温槽使料液对能量的利用率升高,提高厌氧反应的酸化、水解和产甲烷过程,缩短料液滞留期,提高系统的处理能力和处理效果;反应器内覆膜载体和挡泥墙的设计,提升了反应器内的厌氧微生物数量,促进对料液中有机物的转化效率。
The invention belongs to the field of agricultural environmental protection and relates to a plug-flow anaerobic bioreactor for sewage treatment. The plug-flow anaerobic bioreactor of the present invention is realized by the following approach. The pretreated feed liquid is transported to the warming tank for temperature increase. The heated feed liquid enters the feed tank from the overflow pipe, and then It is transferred from the feed port in the feed tank to the inside of the reactor. The feed liquid fully contacts with the film-coated carrier, planktonic anaerobic microorganisms and activated sludge in the reactor, and then is pushed into the water pressure room. The overflow pipe is discharged, and the sludge is taken away by the suction truck. The advantages and positive effects of the present invention: the warming tank increases the energy utilization rate of the feed liquid, improves the acidification, hydrolysis and methane production process of the anaerobic reaction, shortens the retention period of the feed liquid, and improves the processing capacity and treatment effect of the system; The design of the film-covered carrier and the mud retaining wall in the reactor increases the number of anaerobic microorganisms in the reactor and promotes the conversion efficiency of organic matter in the feed liquid.
Description
【技术领域】【Technical field】
本发明属于农业环保领域,涉及一种用于污水处理的推流式厌氧生物反应器。The invention belongs to the field of agricultural environmental protection and relates to a plug-flow anaerobic bioreactor for sewage treatment.
【背景技术】【Background technique】
随着我国新农村建设步伐的加快,集约化养猪业的快速发展,养殖发展过程中产生的大量废水已经远不能被土地自然消纳,对大气、土壤、地下水及其它受纳水体都构成了严重的污染威胁,养殖业污染问题已经引起国家的高度重视。但是养猪业属于薄利行业,从而限制了污水处理投资能力不会太大,这就需要投资少、处理效果好、运行成本低,还具有一定经济效益的污水处理方法。With the acceleration of the construction of new rural areas in my country and the rapid development of intensive pig farming, the large amount of wastewater generated in the process of breeding development is far from being absorbed by the land naturally, and constitutes a serious threat to the atmosphere, soil, groundwater and other receiving water bodies. Serious threat of pollution, aquaculture pollution problem has aroused the country's great attention. However, pig farming is a low-profit industry, which limits the investment capacity of sewage treatment. This requires a sewage treatment method with low investment, good treatment effect, low operating cost, and certain economic benefits.
以好氧活性污泥法为主的污水处理技术,虽然污染物去除率高,但占地面积大、基础投资及运行费用高;而厌氧生物处理技术由于抗有机负荷能力高;不需要曝气供氧、节省操作费用;污泥产量少且易于处理;低能耗;厌氧过程中产生的沼气又可作为清洁能源回收,并加以利用,而成为国内外普遍关注的节能技术。Although the sewage treatment technology based on the aerobic activated sludge method has a high pollutant removal rate, it occupies a large area, and the basic investment and operating costs are high; while the anaerobic biological treatment technology has a high resistance to organic loads; it does not require exposure Gas oxygen supply, saving operating costs; less sludge output and easy to handle; low energy consumption; the biogas generated in the anaerobic process can be recovered as clean energy and utilized, and has become an energy-saving technology that is widely concerned at home and abroad.
厌氧生物反应器内微生物的活性和数量直接影响着反应器的净化效率,而温度的高低又直接影响着反应器内微生物的活性、数量和世代周期。一般地说,在其他工艺条件相同的情况下,在0℃~60℃范围内,温度每上升10℃,反应速度就大约增加2~4倍。因此提高反应器内发酵原料温度到最佳范围将有效提高系统的反应效率。The activity and quantity of microorganisms in the anaerobic bioreactor directly affect the purification efficiency of the reactor, and the temperature directly affects the activity, quantity and generation cycle of microorganisms in the reactor. Generally speaking, under the same other process conditions, in the range of 0°C to 60°C, the reaction rate will increase by about 2 to 4 times for every 10°C increase in temperature. Therefore, increasing the temperature of the fermentation raw materials in the reactor to the optimum range will effectively improve the reaction efficiency of the system.
本发明所述的经过改良的推流式厌氧生物反应器,辅以太阳能双效增温技术和覆膜载体技术,有助于提高发酵原料温度,促进厌氧微生物的活性,明显加快厌氧反应的酸化、水解和产甲烷过程,缩短料液滞留期,提高了系统的处理能力和处理效果。The improved plug-flow anaerobic bioreactor described in the present invention, supplemented by solar double-effect warming technology and film-covered carrier technology, helps to increase the temperature of fermentation raw materials, promote the activity of anaerobic microorganisms, and significantly accelerate the anaerobic process. The acidification, hydrolysis and methane production process of the reaction shorten the retention period of the feed liquid and improve the processing capacity and processing effect of the system.
【发明内容】【Content of invention】
本发明的推流式厌氧生物反应器,通过以下途径来实现,预处理后的料液输送至增温槽,进行增温,增温后的料液由溢流管进入进料池,再由进料池中的进料口转入反应器内部,料液与反应器内的覆膜载体、浮游厌氧微生物及活性污泥充分接触,然后被推流到水压间,上清液由溢流管排出,污泥则由吸泥车取走。The plug-flow anaerobic bioreactor of the present invention is realized by the following approach. The pretreated feed liquid is transported to the warming tank for temperature increase. The heated feed liquid enters the feed tank from the overflow pipe, and then It is transferred from the feed port in the feed tank to the inside of the reactor, and the feed liquid fully contacts with the film-coated carrier, planktonic anaerobic microorganisms and activated sludge in the reactor, and then is pushed into the water pressure room, and the supernatant is The overflow pipe is discharged, and the sludge is taken away by the suction truck.
所述的推流式厌氧生物反应器,在水压间设置回流系统,间断性把发酵后的富含厌氧微生物的料液回流到进料池。In the plug-flow anaerobic bioreactor, a reflux system is installed in the water pressure room to intermittently return the fermented feed liquid rich in anaerobic microorganisms to the feed tank.
所述的推流式厌氧生物反应器,反应器外围建温室或在反应器内部接入供暖管路,对料液进行强制增温,这样有助于促进厌氧菌的活性,明显提高厌氧反应的酸化、水解和产甲烷过程,缩短料液滞留期,提高系统的处理能力和处理效果。In the plug-flow anaerobic bioreactor, a greenhouse is built around the reactor or a heating pipeline is connected inside the reactor to forcibly increase the temperature of the feed liquid, which helps to promote the activity of anaerobic bacteria and significantly improves the anaerobic biological reactor. Oxygen reaction acidification, hydrolysis and methane production process shorten the retention period of feed liquid and improve the processing capacity and effect of the system.
覆膜载体为以钢管、钢筋或UPVC硬管硬性材料构建框架,采用多孔耐腐双面无纺布、无纺棉或类似材料作为附着体,与框架固定在一起构建成的单元模块组。The film-covered carrier is a frame made of steel pipes, steel bars or UPVC hard tube rigid materials, and a unit module group constructed by using porous and corrosion-resistant double-sided non-woven fabrics, non-woven cotton or similar materials as attachments, and fixed with the frame.
本发明的工作原理:Working principle of the present invention:
系统启动后,经过预处理的料液由提升泵输送至增温槽,增温槽的顶部有阳光板或玻璃或其它高透光材料制成的透光盖板,透光盖板与增温槽之间作密封配合,以阻挡增温槽中刺鼻气味的散出,料液在增温槽中滞留一段时间,日光温室内收集的热量和直射进温室的阳光会透过透光盖板为增温槽中的料液增温,增温后的料液会通过溢流管自流入进料池,并通过进料管流入反应器内部,增温槽中日久淤积的污泥可通过排泥管排出,进入反应器的料液以推流的方式与覆膜载体上、底部污泥中和料液中的厌氧微生物充分接触进行厌氧发酵,在微生物世代繁殖的过程中,料液中的有机质被分解和转化,以达到去除CODcr和悬浮物,转变有机氮和有机磷形态的目的;反应后的料液被新料液推流至水压间,然后由出水口排出。After the system is started, the pretreated material liquid is transported to the heating tank by the lift pump. There is a light-transmitting cover made of sunlight board or glass or other high-transparency materials on the top of the heating tank. The light-transmitting cover and the heating The tanks are sealed to prevent the pungent smell from the warming tank. The feed liquid stays in the warming tank for a period of time. The heat collected in the solar greenhouse and the sunlight directly entering the greenhouse will pass through the transparent cover plate for The feed liquid in the warming tank is heated, and the heated feed liquid will flow into the feed tank through the overflow pipe, and flow into the reactor through the feed pipe, and the sludge accumulated in the warming tank for a long time can be drained The mud pipe is discharged, and the feed liquid entering the reactor is fully contacted with the anaerobic microorganisms on the film-coated carrier, in the bottom sludge and in the feed liquid in a push flow manner to carry out anaerobic fermentation. During the generation of microorganisms, the feed liquid The organic matter in the reactor is decomposed and transformed to achieve the purpose of removing CODcr and suspended matter, and changing the form of organic nitrogen and organic phosphorus; the reacted feed liquid is pushed to the hydraulic room by the new feed liquid, and then discharged from the water outlet.
另外,在水压间设置回流系统,间断性把发酵后的富含厌氧微生物的料液回流到进料池,促进厌氧微生物与新进原料的充分接触,提高反应器的降解转化效率;也可以根据需要选择性的在反应器内部接入供暖管路,对料液进行强制增温,这样有助于促进厌氧菌的活性,明显提高厌氧反应的酸化、水解和产甲烷过程,缩短料液滞留期,提高系统的处理能力和处理效果。In addition, a reflux system is installed in the water pressure room to intermittently return the fermented feed liquid rich in anaerobic microorganisms to the feed tank, so as to promote full contact between anaerobic microorganisms and new raw materials, and improve the degradation conversion efficiency of the reactor; It is also possible to selectively connect heating pipes inside the reactor as needed to force the feed liquid to increase in temperature, which will help to promote the activity of anaerobic bacteria and significantly improve the acidification, hydrolysis and methanogenic processes of anaerobic reactions. Shorten the retention period of the feed liquid and improve the processing capacity and processing effect of the system.
本发明的优点和积极效果:Advantage and positive effect of the present invention:
①增温槽将有助于使料液对能量的利用率得到较大的提升;①The warming tank will help to greatly improve the energy utilization rate of the feed liquid;
②料液可以有效的利用太阳能或其它增温措施进行加热增温,有助于促进厌氧菌的活性,明显提高厌氧反应的酸化、水解和产甲烷过程,缩短料液滞留期,提高系统的处理能力和处理效果。② The feed liquid can effectively use solar energy or other warming measures to heat and increase the temperature, which is helpful to promote the activity of anaerobic bacteria, significantly improve the acidification, hydrolysis and methane production process of anaerobic reaction, shorten the retention period of the feed liquid, and improve the efficiency of the system. processing capacity and processing effect.
③反应器内覆膜载体和挡泥墙的引入,提升了反应器内的厌氧微生物数量,促进对料液中有机物的转化效率。③The introduction of film-covered carriers and mud walls in the reactor increases the number of anaerobic microorganisms in the reactor and promotes the conversion efficiency of organic matter in the feed liquid.
④水压间内设置回流系统,间断性把发酵后的料液上清液回流到进料池,促进厌氧微生物与新鲜料液的充分接触,提高反应器的降解转化效率。④ A reflux system is installed in the water pressure room to intermittently return the fermented feed liquid supernatant to the feed tank to promote full contact between anaerobic microorganisms and fresh feed liquid and improve the degradation conversion efficiency of the reactor.
⑤如反应器外围建造一座日光温室,充分利用了太阳能,节省了系统的能源供给。⑤ If a solar greenhouse is built around the reactor, the solar energy is fully utilized and the energy supply of the system is saved.
【附图说明】【Description of drawings】
图1厌氧生物反应器俯视图Figure 1 Top view of anaerobic bioreactor
图2厌氧生物反应器A-A剖视图Figure 2 A-A sectional view of anaerobic bioreactor
图3厌氧生物反应器B-B剖面图Figure 3 B-B Sectional View of Anaerobic Bioreactor
图4厌氧生物反应器C-C剖面图Figure 4 C-C Sectional Diagram of Anaerobic Bioreactor
图5厌氧生物反应器D-D剖面图Figure 5 D-D Sectional Diagram of Anaerobic Bioreactor
其中:1、上料管,2、增温槽,3、天窗口,4、进料池,5、溢流管,6、进料管,7、回流管,8、排泥管,9、覆膜载体,10、挡泥墙,11、供暖管路,12、日光温室。Among them: 1. Feeding pipe, 2. Warming tank, 3. Skylight, 4. Feed tank, 5. Overflow pipe, 6. Feed pipe, 7. Return pipe, 8. Mud discharge pipe, 9. Film-covered carrier, 10. mud retaining wall, 11. heating pipeline, 12. solar greenhouse.
【具体实施方式】【Detailed ways】
如图1~图5所示,本实施例的厌氧生物反应器结构要点包括增温槽、天窗口、溢流管、进料池、进料管、回流管、排泥管、覆膜载体、挡泥墙、供暖管路、日光温室、储气室、透光盖板、反应区、水压间和出水口等。覆膜载体为以钢管、钢筋或UPVC硬管硬性材料构建框架,采用多孔耐腐双面无纺布、无纺棉或类似材料作为附着体,与框架固定在一起构建成的单元模块组。As shown in Figures 1 to 5, the structural points of the anaerobic bioreactor in this embodiment include a warming tank, a skylight, an overflow pipe, a feed tank, a feed pipe, a return pipe, a sludge discharge pipe, and a film-coated carrier , mud wall, heating pipeline, solar greenhouse, gas storage room, light-transmitting cover, reaction area, water pressure room and water outlet, etc. The film-covered carrier is a frame made of steel pipes, steel bars or UPVC hard tube rigid materials, and a unit module group constructed by using porous and corrosion-resistant double-sided non-woven fabrics, non-woven cotton or similar materials as attachments, and fixed with the frame.
猪场或养殖小区的养殖废水经污水收集系统收集后,经过预处理,由提升泵通过上料管1输送至增温槽2,经过增温槽增温后,由溢流管5流入进料池4,再经由进料池底部的进料管6流入反应器内部,料液在反应器内部以推流的方式穿过覆膜载体9,与覆膜载体、挡泥墙10和水体中的厌氧微生物充分接触转化后,经由通道进入水压间,然后升流至出水口排出。通过回流管7可以定期定量的将一部分水压间内的发酵后料液回流至进料池,与溢流管流出的新鲜料液混合,促进新鲜料液与厌氧微生物的接触机会,也增加了池内料液的循环流动性,起到一定的混合搅拌的作用。料液在池内流动的过程中,沉淀下来的部分活性污泥被挡泥墙10截留,以保存活性微生物,促进对料液中有机物的分解和转化效果。After being collected by the sewage collection system, the aquaculture wastewater from pig farms or breeding areas is pretreated and transported by the lift pump to the
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| CN102041279B (en) * | 2009-10-21 | 2013-06-19 | 中国石油化工股份有限公司 | Biomembrane-electrodialysis coupling continuous production technology of L-lactic acid |
| CN102319715B (en) * | 2011-06-01 | 2013-07-31 | 上海亚舟环保科技事务所(普通合伙) | Horizontal plug flow solid waste anaerobic digestion equipment |
| CN102964149B (en) * | 2012-11-29 | 2014-04-09 | 湖南屎壳郎环境科技有限公司 | Pollution abatement method for livestock and poultry farm |
| CN106542654A (en) * | 2017-01-23 | 2017-03-29 | 中蓝连海设计研究院 | A kind of heat preserving method of biochemical treatment of wastewater |
| CN108485929A (en) * | 2018-05-24 | 2018-09-04 | 中国农业大学 | A kind of the pulling flow type biogas production and increasing heat-insulation system in the area that seasons oneself to cold |
| CN109734256A (en) * | 2019-03-11 | 2019-05-10 | 苏州科技大学 | An energy-saving and consumption-reducing denitrification and phosphorus removal device |
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| CN1055529A (en) * | 1990-04-02 | 1991-10-23 | 天津石油化工公司第二石油化工厂 | Treatment of waste water of cis-anhydride by anaerobic biological process |
| CN1401593A (en) * | 2002-10-17 | 2003-03-12 | 詹伯君 | Filler and pond for biochemical treatment of waste water |
| CN2913351Y (en) * | 2005-12-26 | 2007-06-20 | 陈勇 | Laminated push-flow type anaerobic filter |
| CN101381159A (en) * | 2008-10-23 | 2009-03-11 | 南京工业大学 | A vertical anaerobic reactor |
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Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1055529A (en) * | 1990-04-02 | 1991-10-23 | 天津石油化工公司第二石油化工厂 | Treatment of waste water of cis-anhydride by anaerobic biological process |
| CN1401593A (en) * | 2002-10-17 | 2003-03-12 | 詹伯君 | Filler and pond for biochemical treatment of waste water |
| CN2913351Y (en) * | 2005-12-26 | 2007-06-20 | 陈勇 | Laminated push-flow type anaerobic filter |
| CN101381159A (en) * | 2008-10-23 | 2009-03-11 | 南京工业大学 | A vertical anaerobic reactor |
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| Title |
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| JP特开2002-20188A 2002.01.23 |
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| CN101492229A (en) | 2009-07-29 |
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