CN103553271B - A multi-stage treatment and purification process for groundwater pollution - Google Patents
A multi-stage treatment and purification process for groundwater pollution Download PDFInfo
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- CN103553271B CN103553271B CN201310547704.6A CN201310547704A CN103553271B CN 103553271 B CN103553271 B CN 103553271B CN 201310547704 A CN201310547704 A CN 201310547704A CN 103553271 B CN103553271 B CN 103553271B
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- 238000000746 purification Methods 0.000 title claims abstract description 14
- 238000003895 groundwater pollution Methods 0.000 title claims abstract description 9
- 238000000605 extraction Methods 0.000 claims abstract description 32
- 238000006243 chemical reaction Methods 0.000 claims abstract description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 16
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 claims abstract description 11
- 238000000034 method Methods 0.000 claims abstract description 9
- 150000008282 halocarbons Chemical class 0.000 claims abstract description 7
- 239000000203 mixture Substances 0.000 claims abstract description 5
- 230000008595 infiltration Effects 0.000 claims abstract 3
- 238000001764 infiltration Methods 0.000 claims abstract 3
- 239000003673 groundwater Substances 0.000 claims description 22
- 238000005243 fluidization Methods 0.000 claims description 14
- 239000003344 environmental pollutant Substances 0.000 claims description 10
- 231100000719 pollutant Toxicity 0.000 claims description 10
- 241000196324 Embryophyta Species 0.000 claims description 9
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 9
- 239000001301 oxygen Substances 0.000 claims description 9
- 229910052760 oxygen Inorganic materials 0.000 claims description 9
- MMDJDBSEMBIJBB-UHFFFAOYSA-N [O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.[NH6+3] Chemical compound [O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.[NH6+3] MMDJDBSEMBIJBB-UHFFFAOYSA-N 0.000 claims description 7
- 244000005700 microbiome Species 0.000 claims description 7
- 239000000463 material Substances 0.000 claims description 6
- 239000004576 sand Substances 0.000 claims description 6
- 241000218998 Salicaceae Species 0.000 claims description 5
- 238000005273 aeration Methods 0.000 claims description 5
- 239000000945 filler Substances 0.000 claims description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 4
- 229920000642 polymer Polymers 0.000 claims description 3
- 229920002635 polyurethane Polymers 0.000 claims description 3
- 239000004814 polyurethane Substances 0.000 claims description 3
- 230000000813 microbial effect Effects 0.000 claims description 2
- 229910052757 nitrogen Inorganic materials 0.000 claims description 2
- 239000005416 organic matter Substances 0.000 claims description 2
- 238000011946 reduction process Methods 0.000 claims description 2
- 239000000126 substance Substances 0.000 claims description 2
- 230000015556 catabolic process Effects 0.000 claims 1
- 150000001875 compounds Chemical class 0.000 claims 1
- 238000006731 degradation reaction Methods 0.000 claims 1
- 239000003651 drinking water Substances 0.000 abstract description 3
- 235000020188 drinking water Nutrition 0.000 abstract description 3
- 230000009286 beneficial effect Effects 0.000 abstract description 2
- 235000008733 Citrus aurantifolia Nutrition 0.000 abstract 1
- 235000011941 Tilia x europaea Nutrition 0.000 abstract 1
- 238000001914 filtration Methods 0.000 abstract 1
- 239000004571 lime Substances 0.000 abstract 1
- 239000002699 waste material Substances 0.000 abstract 1
- 239000002131 composite material Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000012466 permeate Substances 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
- Y02W10/10—Biological treatment of water, waste water, or sewage
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- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
- Biological Treatment Of Waste Water (AREA)
Abstract
Description
技术领域technical field
本发明涉及被污染的地下水修复技术,尤其涉及一种地下水污染多级处理净化工艺。The invention relates to a polluted groundwater restoration technology, in particular to a groundwater pollution multi-stage treatment and purification process.
背景技术Background technique
随着城市的飞速发展,收纳垃圾的量越来越多,垃圾场也越来越多,这就不可避免的会产生垃圾渗透液污染地下水的事情发生,这些问题不断加剧,使得本就不多的地下水,能被人直接使用的变得更少。垃圾渗透液中主要是氨氮和卤代烃的含量比较高,成为了污染地下水的主要因素,现有的处理系统主要由水里隔离技术、化学处理和真空抽提等,运行费用高,结构复杂,但是仍达不到很理想的处理效果,地下水还需要进一步净化才能达到饮用水的标准。With the rapid development of the city, the amount of garbage collected is increasing, and there are more and more garbage dumps. This will inevitably cause garbage seepage to pollute the groundwater. These problems continue to aggravate, making it difficult to less groundwater can be directly used by humans. The content of ammonia nitrogen and halogenated hydrocarbons in the garbage permeate is relatively high, which has become the main factor of polluting groundwater. The existing treatment system mainly consists of water isolation technology, chemical treatment and vacuum extraction, etc., with high operating costs and complex structure. , but still can not reach very ideal treatment effect, the groundwater needs to be further purified to meet the standard of drinking water.
发明内容Contents of the invention
本发明的目的在于克服现有技术中的不足之处,提供了一种地下水污染多级处理净化工艺。The object of the present invention is to overcome the deficiencies in the prior art and provide a multi-stage treatment and purification process for groundwater pollution.
为了达到上述目的,本发明是通过以下技术方案实现的:In order to achieve the above object, the present invention is achieved through the following technical solutions:
一种地下水污染多级处理净化工艺,包括从左到右依次连接的曝气生物流化池、过滤池和反应池,抽提管连通至抽提井的底部,抽提管在地表连接到抽提泵上,抽提泵通过管路连接到曝气生物流化池,反应池通过输送管与输送泵相连接,与输送泵另一端连接的排水管延伸至渗透渠内部,反应池内填充油填充料,填充料为发酵树皮和沙子的混合物,发酵树皮和沙子的体积比大于等于1:1。A multi-stage treatment and purification process for groundwater pollution, including an aerated biological fluidization tank, a filter tank and a reaction tank connected in sequence from left to right. The extraction pipe is connected to the bottom of the extraction well, and the extraction pipe is connected to the extraction well on the surface. On the lifting pump, the extraction pump is connected to the aerated biological fluidization tank through a pipeline, the reaction tank is connected to the delivery pump through a delivery pipe, and the drain pipe connected to the other end of the delivery pump extends to the inside of the permeation channel, and the reaction tank is filled with oil. The filling material is a mixture of fermented bark and sand, and the volume ratio of fermented bark and sand is greater than or equal to 1:1.
进一步所述曝气生物流化池底部设置有微孔曝气系统,内部填充油多空高分子填料为微生物的载体,载体使用的材料为聚氨酯海绵,过滤池上部种植有净水植物,净水植物采用的是根系发达的杨柳科植物。Further, a microporous aeration system is provided at the bottom of the aerated biological fluidization tank, and the interior is filled with oil and porous polymer fillers as the carrier of microorganisms. The material used for the carrier is polyurethane sponge, and water purification plants are planted on the upper part of the filter tank. What the plant adopts is the salicaceae plant with well-developed root system.
本发明具有以下有益效果:The present invention has the following beneficial effects:
本发明的地下水污染多级处理净化工艺,针对了垃圾污染物渗透的地下水的成分特点,通过多级处理方法,能有有效去除地下水中的氨氮和卤代烃污染物,使地下水能够满足饮用水水质标准,设计合理,结构简单,安全可靠,使用方便,易于维护,具有推广使用的价值。附图说明The groundwater pollution multi-stage treatment and purification process of the present invention is aimed at the composition characteristics of the groundwater infiltrated by garbage pollutants. Through the multi-stage treatment method, the ammonia nitrogen and halogenated hydrocarbon pollutants in the groundwater can be effectively removed, so that the groundwater can meet the requirements of drinking water. Standard water quality, reasonable design, simple structure, safe and reliable, easy to use, easy to maintain, and has the value of popularization. Description of drawings
图1为本发明所提供的多级处理净化工艺结构图。Figure 1 is a structural diagram of the multi-stage treatment and purification process provided by the present invention.
符号说明:Symbol Description:
1:曝气生物流化池2:过滤池3:反应池4:渗透渠1: Biological aerated fluidization tank 2: Filter tank 3: Reaction tank 4: Permeation channel
5:净水植物6:填充料7:载体8:抽提泵9:抽提管5: Water purification plant 6: Filling material 7: Carrier 8: Extraction pump 9: Extraction tube
10:管路11:抽提井12:输送管13:输送泵14:排水管10: Pipeline 11: Extraction well 12: Delivery pipe 13: Delivery pump 14: Drainage pipe
具体实施方式Detailed ways
以下结合附图和实施例对本发明作进一步的描述。The present invention will be further described below in conjunction with the accompanying drawings and embodiments.
作为本发明的一种实施方式,参阅图1,一种地下水污染多级处理净化工艺,包括从左到右依次连接的曝气生物流化池1、过滤池2和反应池3,抽提管9连通至抽提井11的底部,抽提管9在地表连接到抽提泵8上,抽提泵8通过管路10连接到曝气生物流化池1,反应池3通过输送管12与输送泵13相连接,与输送泵13另一端连接的排水管14延伸至渗透渠4内部,反应池3内填充油填充料6,填充料6为发酵树皮和沙子的混合物,发酵树皮和沙子的体积比大于等于1:1。As an embodiment of the present invention, referring to Fig. 1, a multi-stage treatment and purification process for groundwater pollution includes a biological aerated fluidization tank 1, a filter tank 2 and a reaction tank 3 connected in sequence from left to right, and an extraction pipe 9 is connected to the bottom of the extraction well 11, the extraction pipe 9 is connected to the extraction pump 8 on the surface, the extraction pump 8 is connected to the aerated biological fluidization tank 1 through the pipeline 10, and the reaction tank 3 is connected to the aerated biological fluidization tank 1 through the delivery pipe 12 The delivery pump 13 is connected, and the drain pipe 14 connected to the other end of the delivery pump 13 extends to the inside of the permeation channel 4, and the reaction tank 3 is filled with oil filling material 6, which is a mixture of fermented bark and sand, fermented bark and The volume ratio of sand is greater than or equal to 1:1.
进一步所述曝气生物流化池1底部设置有微孔曝气系统,内部填充油多空高分子填料为微生物的载体7,载体7使用的材料为聚氨酯海绵,过滤池2上部种植有净水植物5,净水植物5采用的是根系发达的杨柳科植物。Further, the bottom of the aerated biological fluidization tank 1 is provided with a microporous aeration system, and the interior is filled with oily and porous polymer fillers as the carrier 7 of microorganisms. The material used for the carrier 7 is polyurethane sponge, and the upper part of the filter tank 2 is planted with clean water Plant 5, what water purification plant 5 adopted is the Salicaceae plant with well-developed root system.
工作时,在地下水受到氨氮或者卤代烃等污染物污染的区域,打一口抽提井11,地表的抽提泵8通过连通到抽提井11底部的抽提管9把被污染的地下水抽提到地表,并通过管路10把地下水送到曝气生物流化池1。曝气生物流化池1内的载体7上投放有复合微生物菌种,微生物在曝气过程中获得充足的氧气,把氨氮污染物直接氧化为硝态氮,这个过程能够清除掉大部分的氨氮污染物。这时候还溶有很多氧气的地下水进入到过滤池2中,在好氧条件下,剩余的氨氮污染物进一步氧化为硝态氮。过滤池2上部种植有净水植物5,为根系发达的杨柳科植物,不仅能净化地下水,还能消耗掉水中的氧气,减少地下水中溶解的氧气,保证反应池3为厌氧环境。在厌氧环境的反应池3中,硝态氮完成反硝化作用,硝态氮还原成氮气,自行挥发出去,同时反应池3中的厌氧微生物,能够把卤代烃一类的氧化态污染物还原降解,发酵树皮中的有机质可作为电子给体,提高还原过程的速率。这样通过处理的地下水,被输送泵13通过输送管12输送到地表,再通过排水管14排放到渗透渠4内,这样就完成了一整个底下污染水处理的过程,简单有效,处理效率高。During work, in the area where the groundwater is polluted by pollutants such as ammonia nitrogen or halogenated hydrocarbons, an extraction well 11 is drilled, and the extraction pump 8 on the surface pumps the polluted groundwater through the extraction pipe 9 connected to the bottom of the extraction well 11. Mention the ground surface, and send the groundwater to the aerated biological fluidization tank 1 through the pipeline 10. The carrier 7 in the aerated biological fluidization tank 1 is placed with composite microbial strains. The microorganisms obtain sufficient oxygen during the aeration process, and directly oxidize ammonia nitrogen pollutants into nitrate nitrogen. This process can remove most of the ammonia nitrogen. pollutants. At this time, the groundwater that still has a lot of oxygen dissolved enters the filter tank 2, and under aerobic conditions, the remaining ammonia nitrogen pollutants are further oxidized to nitrate nitrogen. Water purifying plants 5 are planted on the upper part of the filter tank 2, which are Salicaceae plants with well-developed roots, which can not only purify the groundwater, but also consume oxygen in the water, reduce dissolved oxygen in the groundwater, and ensure that the reaction tank 3 is an anaerobic environment. In the reaction tank 3 in the anaerobic environment, the denitrification is completed, and the nitrate nitrogen is reduced to nitrogen, which volatilizes by itself. At the same time, the anaerobic microorganisms in the reaction tank 3 can pollute the oxidation state of halogenated hydrocarbons. The organic matter in the fermented bark can be used as an electron donor to increase the rate of the reduction process. The treated groundwater is transported to the surface by the delivery pump 13 through the delivery pipe 12, and then discharged into the permeation channel 4 through the drain pipe 14, thus completing a whole bottom polluted water treatment process, which is simple and effective with high treatment efficiency.
综上所述,本发明仅对地下水污染多级处理净化工艺的一个实施例进行了说明,但是本发明不限于此,本领域技术人员应当知道,在不脱离本发明的权利要求书所记载的保护范围的情况下可进行任意变更和修改。In summary, the present invention has only described one embodiment of the multi-stage treatment and purification process for groundwater pollution, but the present invention is not limited thereto, and those skilled in the art should know that without departing from the scope of the claims described in the present invention Any changes and modifications are possible without the scope of protection.
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CN104261588B (en) * | 2014-09-29 | 2015-12-30 | 滁州友林科技发展有限公司 | The treatment unit of oil-containing underground water and control method |
CN104671409B (en) * | 2014-12-31 | 2016-08-24 | 浙江至美环境科技有限公司 | A kind of method utilizing biological fluidized bed to process sewage |
CN105923886A (en) * | 2016-03-17 | 2016-09-07 | 深圳市东华园林股份有限公司 | Sewage recycling purification treatment system and method using the system |
CN110563161A (en) * | 2019-10-21 | 2019-12-13 | 上海洁壤环保科技有限公司 | long-acting restoration system and method for pollution control site in water-deficient area |
CN110563126A (en) * | 2019-10-21 | 2019-12-13 | 上海洁壤环保科技有限公司 | System and method for repairing volatile organic compounds in underground water |
CN112094003B (en) * | 2020-11-17 | 2021-02-02 | 湖南艾布鲁环保科技股份有限公司 | Integrated solar sewage treatment equipment and sewage treatment method |
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Publication number | Priority date | Publication date | Assignee | Title |
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CN201232038Y (en) * | 2008-04-15 | 2009-05-06 | 南京圣卡孚科技有限公司 | Continuous biological composite bed for water treatment |
CN101948171A (en) * | 2010-08-20 | 2011-01-19 | 北京大学 | Permeable reaction wall method capable of repairing halohydrocarbon and nitrate polluted groundwater |
CN102491583A (en) * | 2011-11-16 | 2012-06-13 | 温州大学 | Constructed wetland with sewage treatment function |
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CN201232038Y (en) * | 2008-04-15 | 2009-05-06 | 南京圣卡孚科技有限公司 | Continuous biological composite bed for water treatment |
CN101948171A (en) * | 2010-08-20 | 2011-01-19 | 北京大学 | Permeable reaction wall method capable of repairing halohydrocarbon and nitrate polluted groundwater |
CN102491583A (en) * | 2011-11-16 | 2012-06-13 | 温州大学 | Constructed wetland with sewage treatment function |
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