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CN106673362A - Combined treatment process of landfill leachate - Google Patents

Combined treatment process of landfill leachate Download PDF

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Publication number
CN106673362A
CN106673362A CN201611260081.4A CN201611260081A CN106673362A CN 106673362 A CN106673362 A CN 106673362A CN 201611260081 A CN201611260081 A CN 201611260081A CN 106673362 A CN106673362 A CN 106673362A
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treatment
advanced oxidation
biochemical
landfill leachate
effluent
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胡兆吉
胡义亮
陈建新
孙洋
欧阳二明
王白杨
冯斐
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Nanchang University
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Nanchang University
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00Multistage treatment of water, waste water or sewage
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/20Treatment of water, waste water, or sewage by degassing, i.e. liberation of dissolved gases
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/30Treatment of water, waste water, or sewage by irradiation
    • C02F1/32Treatment of water, waste water, or sewage by irradiation with ultraviolet light
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/72Treatment of water, waste water, or sewage by oxidation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/72Treatment of water, waste water, or sewage by oxidation
    • C02F1/722Oxidation by peroxides
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/72Treatment of water, waste water, or sewage by oxidation
    • C02F1/78Treatment of water, waste water, or sewage by oxidation with ozone
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/06Contaminated groundwater or leachate
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2305/00Use of specific compounds during water treatment
    • C02F2305/02Specific form of oxidant
    • C02F2305/026Fenton's reagent
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/02Aerobic processes
    • C02F3/12Activated sludge processes
    • C02F3/1236Particular type of activated sludge installations
    • C02F3/1257Oxidation ditches
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/28Anaerobic digestion processes
    • C02F3/284Anaerobic digestion processes using anaerobic baffled reactors
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/28Anaerobic digestion processes
    • C02F3/2846Anaerobic digestion processes using upflow anaerobic sludge blanket [UASB] reactors
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/30Aerobic and anaerobic processes

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  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Treatment Of Water By Oxidation Or Reduction (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

一种垃圾渗滤液的组合处理工艺,采用传统的以物化处理为主的一级和以生化处理为主的二级处理组合工艺,这一处理阶段能够采用成熟、应用广泛且经济性较好的传统处理工艺对垃圾渗滤液进行第一阶段的处理,以去除垃圾渗滤液中大部分能够通过传统处理方法去除的污染物;二级出水排出后进入高级氧化处理阶段,通过高级氧化工艺的强氧化能力对二级出水中污染物的主要成分,即难降解大分子有机物进行有效的降解,在这一阶段通过对难降解大分子有机物有效降解的同时大幅提高水质的可生化性;经高级氧化处理后的出水再次进入经济性优异的生化处理阶段,再通过生化处理使出水水质达到GB16889‑2008《国家生活垃圾填埋场污染控制标准》的排放标准。

A combination treatment process of landfill leachate, which adopts the traditional combination process of primary treatment mainly based on physical and chemical treatment and secondary treatment mainly based on biochemical treatment. This treatment stage can adopt mature, widely used and economical The traditional treatment process performs the first-stage treatment on the landfill leachate to remove most of the pollutants in the landfill leachate that can be removed by traditional treatment methods; after the secondary effluent is discharged, it enters the advanced oxidation treatment stage, through the strong oxidation of the advanced oxidation process Ability to effectively degrade the main components of pollutants in the secondary effluent, that is, refractory macromolecular organic matter. At this stage, the biodegradability of water quality is greatly improved by effectively degrading refractory macromolecular organic matter; after advanced oxidation treatment The final effluent enters the stage of biochemical treatment with excellent economy again, and then through biochemical treatment, the effluent quality reaches the discharge standard of GB16889‑2008 "National Domestic Waste Landfill Pollution Control Standard".

Description

一种垃圾渗滤液的组合处理工艺A combined treatment process for landfill leachate

技术领域technical field

本发明涉及一种垃圾渗滤液的“双生化”+“高级氧化”组合处理工艺,尤其涉及一种以生化处理+高级氧化处理+生化处理为核心的垃圾渗滤液组合处理工艺,属于污水处理技术与工艺领域。The invention relates to a combination treatment process of "biochemical" + "advanced oxidation" of landfill leachate, in particular to a combined treatment process of landfill leachate with biochemical treatment + advanced oxidation treatment + biochemical treatment as the core, which belongs to sewage treatment technology and craft areas.

背景技术Background technique

随着我国城市人口的增加、城市规模的扩大和广大人民生活水平的提高,我国的城市生活垃圾产量每年都在急剧的增加。目前城市生活垃圾的处理方法主要有焚烧处理,高温堆肥和卫生填埋,其中卫生填埋由于其技术简单且具有优异的经济优势,使得其得到了广泛的应用。但是这一处理方法会产生大量的垃圾渗滤液。目前我国对垃圾渗滤液主要采用的是以物化为主的一级和生化为主的二级处理组合工艺。但是由于垃圾渗滤液中含有大量的难降解大分子有机物,使得这一传统得到广泛应用的处理工艺处理后的水质无法满足GB16889-2008《国家生活垃圾填埋场污染控制标准》中的排放要求。With the increase of my country's urban population, the expansion of city scale and the improvement of people's living standards, the output of urban domestic waste in my country is increasing sharply every year. At present, the treatment methods of municipal solid waste mainly include incineration, high-temperature composting and sanitary landfill. Among them, sanitary landfill has been widely used because of its simple technology and excellent economic advantages. However, this treatment method will produce a large amount of landfill leachate. At present, my country's landfill leachate mainly adopts a combined process of physical and chemical primary treatment and biochemical secondary treatment. However, because landfill leachate contains a large amount of refractory macromolecular organic matter, the water quality after treatment by this traditional and widely used treatment process cannot meet the discharge requirements in GB16889-2008 "National Domestic Waste Landfill Pollution Control Standards".

针对这一情况,我国城市生活垃圾渗滤液处理工程领域出现了以“双膜法”,即膜生物反应器(MBR)+纳虑反渗透(NF/RO)为主体工艺路线的大量工程实例。该工艺具有很好的处理效果,但是其存在初期一次性投资成本过高,运行费用高。尤其是纳虑反渗透(NF/RO)属于典型的膜过滤,本质上为污染物的“转移”过程,并未从根本上去除掉污染物,存在浓缩液量大且难以处置等突出问题。针对这一突出问题,在传统的生物处理工艺的基础上,将高级氧化技术与之组合形成垃圾渗滤液的处理“双生化”+“高级氧化”组合处理工艺,通过处理工艺的合理组合,既解决了对渗滤液污染物的去除问题,又能够获得很好的经济性和可操作性。In response to this situation, there have been a large number of engineering examples in the field of municipal solid waste leachate treatment engineering in my country with the "double-membrane method", that is, membrane bioreactor (MBR) + nanofiltration reverse osmosis (NF/RO) as the main process route. This process has a good treatment effect, but its initial one-time investment cost is too high and the operating cost is high. In particular, nano-reverse osmosis (NF/RO) is a typical membrane filtration, which is essentially a "transfer" process of pollutants. It has not fundamentally removed pollutants, and there are prominent problems such as large volume of concentrated liquid and difficult disposal. In response to this outstanding problem, on the basis of traditional biological treatment processes, advanced oxidation technology is combined with it to form a "dual biochemical" + "advanced oxidation" combined treatment process for landfill leachate. Through a reasonable combination of treatment processes, both The problem of removing the leachate pollutants is solved, and good economy and operability can be obtained.

高级氧化技术主要是通过氧化剂在一定的反应条件下产生具有强氧化能力的羟基自由基(•OH),与废水中的大分子难降解有机物发生反应,破坏有机物的分子结构,将其降解成小分子物质,甚至彻底降解为二氧化碳和水,实现污染物的有效“转化”。因此,经过高级氧化技术处理后的垃圾渗滤液二级出水其可生化性能够得到显著的提升,从而使得整个“双生化”+高级氧化工艺能够得到顺利的实施。The advanced oxidation technology is mainly to generate hydroxyl radicals (•OH) with strong oxidizing ability through oxidants under certain reaction conditions, which react with macromolecular refractory organic substances in wastewater, destroy the molecular structure of organic substances, and degrade them into small Molecular substances are even completely degraded into carbon dioxide and water to achieve effective "transformation" of pollutants. Therefore, the biodegradability of the secondary effluent of landfill leachate treated by advanced oxidation technology can be significantly improved, so that the entire "twin biochemical" + advanced oxidation process can be implemented smoothly.

发明内容Contents of the invention

本发明的目的是针对现有技术不足提供一种以生化处理+高级氧化处理+生化处理为核心的垃圾渗滤液组合处理工艺。The purpose of the present invention is to provide a combined landfill leachate treatment process with biochemical treatment + advanced oxidation treatment + biochemical treatment as the core to solve the deficiencies of the prior art.

所述一种垃圾渗滤液的“双生化”+“高级氧化”组合处理工艺其处理过程包括:物化预处理,一次生化处理,高级氧化处理,二次生化处理,工艺步骤如下:The "dual biochemical" + "advanced oxidation" combined treatment process of landfill leachate includes: physical and chemical pretreatment, primary biochemical treatment, advanced oxidation treatment, and secondary biochemical treatment. The process steps are as follows:

垃圾渗滤液经调节池经水泵一次通过物化预处理阶段的初沉淀池和氨吹脱塔,之后进入一次生化处理装置即膜生物反应器,垃圾渗滤液经过上述处理后其可生化性已大幅度降低,水中主要污染物为大分子难降解有机物,再将生化出水导入高级氧化处理装置即UV+Fenton高级氧化处理装置,经高级氧化处理后,提高水质可生化性,最后再次采用膜生物反应器,即二次生化处理技术使得出水最终符合排放标准。The landfill leachate passes through the adjustment tank and the water pump once through the primary sedimentation tank and ammonia stripping tower in the physical and chemical pretreatment stage, and then enters the primary biochemical treatment device, namely the membrane bioreactor. After the above treatment, the biochemical properties of the landfill leachate have been greatly improved. The main pollutants in the water are macromolecular refractory organic substances, and then the biochemical effluent is introduced into the advanced oxidation treatment device, that is, the UV+Fenton advanced oxidation treatment device. After advanced oxidation treatment, the biodegradability of the water quality is improved, and finally the membrane bioreactor is used again , that is, the secondary biochemical treatment technology makes the effluent finally meet the discharge standard.

所述物化预处理是以混凝沉淀、吹脱等物理化学方法为主体的预处理工艺;The physical and chemical pretreatment is a pretreatment process based on physical and chemical methods such as coagulation, precipitation, and stripping;

所述一次生化处理是以UASB(上流式厌氧污泥床)、ABR(厌氧折流板反应器)工艺等厌氧工艺和以接触氧化、氧化沟、A/O工艺等好氧工艺为主体的生化处理工艺;The primary biochemical treatment is based on anaerobic processes such as UASB (upflow anaerobic sludge bed) and ABR (anaerobic baffle reactor) processes and aerobic processes such as contact oxidation, oxidation ditch, and A/O processes. The main biochemical treatment process;

所述高级氧化处理工艺是以UV+Fenton、O3高级氧化技术为其主体的高级氧化处理工艺;The advanced oxidation treatment process is an advanced oxidation treatment process based on UV+Fenton and O3 advanced oxidation technology;

所述二次生化处理是以膜生物反应器(MBR)、曝气生物滤池(BAF)工艺等为主体的后续生化处理工艺;The secondary biochemical treatment is a follow-up biochemical treatment process based on membrane bioreactor (MBR), biological aerated filter (BAF) process, etc.;

所述一种垃圾渗滤液的“双生化”+“高级氧化”组合处理工艺,其物化预处理和一次生化处理阶段可灵活的根据具体水质情况设置具体的处理工艺,以通过经济性优异的二级处理组合工艺去除垃圾渗滤液中绝大部分能够通过该技术去除的污染物;The "dual biochemical" + "advanced oxidation" combined treatment process of landfill leachate, its physical and chemical pretreatment and primary biochemical treatment stages can flexibly set specific treatment processes according to specific water quality conditions, so as to pass through the secondary oxidation process with excellent economical efficiency. The combined process of multi-stage treatment removes most of the pollutants in landfill leachate that can be removed by this technology;

所述一种垃圾渗滤液的“双生化”+“高级氧化”组合处理工艺,其高级氧化处理和二次生化处理之间可以根据二级出水水质的具体情况,通过调整高级氧化处理和二次生化处理之间的协同关系,使得在保证处理效果的同时,具有更高的综合经济效益。The "dual biochemical" + "advanced oxidation" combined treatment process of landfill leachate, the advanced oxidation treatment and the secondary biochemical treatment can be adjusted according to the specific conditions of the secondary effluent water quality by adjusting the advanced oxidation treatment and the secondary biochemical treatment. The synergistic relationship between biochemical treatments enables higher comprehensive economic benefits while ensuring the treatment effect.

本发明的有益效果是:通过上述方案,能够继续采用传统的物化预处理和一次生化处理技术对垃圾渗滤液进行前期的处理,利用这一应用广泛且经济效益良好的工艺去除垃圾渗滤液中绝大部分的污染物,再针对这一传统工艺处理后的垃圾渗滤液出水水质可生化性极差的特点,采用高级氧化技术进行下一步的处理,利用高级氧化技术对二级出水中所含有的大量难降解大分子有机物进行有效的氧化降解,并大幅提高水质的可生化性,之后再利用生化处理技术对高级氧化处理后的出水进行二次生化处理,从而使得最终的出水水质能够达到GB16889-2008《国家生活垃圾填埋场污染控制标准》中的排放要求。上述过程中,可以针对具体水质情况,对高级氧化和二次生化这两部分处理工艺进行合理的搭配,以在最终出水水质满足排放要求的前提下,最大限度的降低综合处理成本。此外上述方案还能够十分方便地针对目前大量存在的以物化预处理和一次生化处理技术为核心的处理设施进行相应的技术改造工作。The beneficial effects of the present invention are: through the above scheme, the traditional physical and chemical pretreatment and primary biochemical treatment technology can be used to carry out the preliminary treatment of the landfill leachate, and this widely used and economically beneficial process can be used to remove the absolute Most of the pollutants, in view of the characteristics of extremely poor biodegradability of the landfill leachate effluent treated by this traditional process, advanced oxidation technology is used for the next step of treatment, and advanced oxidation technology is used to treat the pollutants contained in the secondary effluent A large number of refractory macromolecular organics are effectively oxidized and degraded, and the biodegradability of the water quality is greatly improved, and then the biochemical treatment technology is used to perform secondary biochemical treatment on the effluent after advanced oxidation treatment, so that the final effluent quality can reach GB16889- Discharge requirements in the 2008 "National Domestic Waste Landfill Pollution Control Standards". In the above process, according to the specific water quality, the advanced oxidation and secondary biochemical treatment processes can be reasonably matched to minimize the comprehensive treatment cost on the premise that the final effluent quality meets the discharge requirements. In addition, the above-mentioned scheme can also be very convenient for carrying out corresponding technical transformation work for a large number of treatment facilities currently existing with physicochemical pretreatment and primary biochemical treatment technology as the core.

附图说明Description of drawings

图1是本发明处理方法的工艺流程图;Fig. 1 is the process flow sheet of processing method of the present invention;

图2是本发明实施方案1的工艺流程图;Fig. 2 is the process flow sheet of embodiment 1 of the present invention;

图3是本发明实施方案2的工艺流程图;Fig. 3 is the process flow chart of embodiment 2 of the present invention;

图中:1.调节池 2. 初沉淀池 3. 氨吹脱塔 4. 膜生物反应器 5. 臭氧高级氧化处理装置6. 膜生物反应器 A.为回收为燃烧 B.为回收为排放 C.为空气 D.为臭氧。In the figure: 1. Regulating tank 2. Primary sedimentation tank 3. Ammonia stripping tower 4. Membrane bioreactor 5. Ozone advanced oxidation treatment device 6. Membrane bioreactor A. for recovery as combustion B. for recovery as emission C . For air D. For ozone.

具体实施方式detailed description

下述内容将结合附图对本发明的相关特性进行进一步的阐述说明,但这并不因此将本发明限制在所述的实施案例范围当中。The following content will further illustrate the relevant characteristics of the present invention in conjunction with the accompanying drawings, but this does not limit the present invention to the scope of the described embodiments.

实施方案1:垃圾渗滤液的“双生化”+“高级氧化”组合处理工艺,包括物化预处理,一次生化处理,高级氧化处理,二次生化处理。垃圾渗滤液经调节池(1)经水泵一次通过物化预处理阶段的初沉淀池(2)和氨吹脱塔(3),之后进入一次生化处理装置即膜生物反应器(4),垃圾渗滤液经过上述处理后其可生化性已大幅度降低,水中主要污染物为大分子难降解有机物,此时将生化出水导入高级氧化处理装置即UV+Fenton高级氧化处理装置(5),经高级氧化处理后,大幅提高水质可生化性,最后再次采用膜生物反应器(6),即二次生化处理技术使得出水最终符合排放标准,该方案所采用的工艺流程图参见图2。Embodiment 1: The "dual biochemical" + "advanced oxidation" combined treatment process of landfill leachate, including physical and chemical pretreatment, primary biochemical treatment, advanced oxidation treatment, and secondary biochemical treatment. The landfill leachate passes through the adjustment tank (1) and the water pump once through the primary sedimentation tank (2) and the ammonia stripping tower (3) in the physical and chemical pretreatment stage, and then enters the primary biochemical treatment device, namely the membrane bioreactor (4). After the above-mentioned treatment, the biochemical properties of the filtrate have been greatly reduced. The main pollutants in the water are macromolecular refractory organic substances. After treatment, the biodegradability of the water quality is greatly improved, and finally the membrane bioreactor (6) is used again, that is, the secondary biochemical treatment technology makes the effluent finally meet the discharge standard. The process flow chart adopted in this scheme is shown in Figure 2.

采用本发明对南昌某垃圾填埋场的垃圾渗滤液进行处理,处理效果见下表所示:Adopt the present invention to treat the landfill leachate in Nanchang, and the treatment effect is shown in the following table:

从表中得到的检测数据可知,经本发明处理后的垃圾渗滤液其最终出水水质能够满足GB16889-2008《国家生活垃圾填埋场污染控制标准》中的排放要求。From the test data obtained in the table, it can be seen that the final effluent quality of the landfill leachate treated by the present invention can meet the discharge requirements in GB16889-2008 "National Domestic Waste Landfill Pollution Control Standard".

实施方案2:垃圾渗滤液的“双生化”+“高级氧化”组合处理工艺,包括物化预处理,一次生化处理,高级氧化处理,二次生化处理。垃圾渗滤液经调节池(1)经水泵一次通过物化预处理阶段的初沉淀池(2)和氨吹脱塔(3),之后进入一次生化处理装置即膜生物反应器(4),垃圾渗滤液经过上述处理后其可生化性已大幅度降低,水中主要污染物为难降解大分子有机物,此时将生化出水通入高级氧化处理装置即臭氧高级氧化处理装置(5),经高级氧化处理后,大幅提高水质可生化性,最后再次采用膜生物反应器(6),即二次生化处理技术使得出水最终符合排放标准,该方案所采用的工艺流程图参见图3。Embodiment 2: The "dual biochemical" + "advanced oxidation" combined treatment process of landfill leachate, including physical and chemical pretreatment, primary biochemical treatment, advanced oxidation treatment, and secondary biochemical treatment. The landfill leachate passes through the adjustment tank (1) and the water pump once through the primary sedimentation tank (2) and the ammonia stripping tower (3) in the physical and chemical pretreatment stage, and then enters the primary biochemical treatment device, namely the membrane bioreactor (4). After the above treatment, the biodegradability of the filtrate has been greatly reduced, and the main pollutants in the water are refractory macromolecular organic substances. At this time, the biochemical effluent is passed into the advanced oxidation treatment device, that is, the ozone advanced oxidation treatment device (5). , greatly improve the biodegradability of water quality, and finally use the membrane bioreactor (6) again, that is, the secondary biochemical treatment technology to make the effluent finally meet the discharge standard. The process flow chart adopted in this scheme is shown in Figure 3.

采用本发明对南昌某垃圾填埋场的垃圾渗滤液进行处理,处理效果见下表所示:Adopt the present invention to treat the landfill leachate in Nanchang, and the treatment effect is shown in the following table:

从表中得到的检测数据可知,经本发明处理后的垃圾渗滤液其最终出水水质能够满足GB16889-2008《国家生活垃圾填埋场污染控制标准》中的排放要求。From the test data obtained in the table, it can be seen that the final effluent quality of the landfill leachate treated by the present invention can meet the discharge requirements in GB16889-2008 "National Domestic Waste Landfill Pollution Control Standard".

Claims (1)

1.一种垃圾渗滤液的组合处理工艺,其特征在于:所述组合处理工艺过程包括:物化预处理,一次生化处理,高级氧化处理,二次生化处理;具体步骤为:1. A combined treatment process of landfill leachate, characterized in that: said combined treatment process comprises: physical and chemical pretreatment, primary biochemical treatment, advanced oxidation treatment, secondary biochemical treatment; concrete steps are: 垃圾渗滤液经调节池经水泵一次通过物化预处理阶段的初沉淀池和氨吹脱塔,之后进入一次生化处理装置即膜生物反应器,垃圾渗滤液经过上述处理后其可生化性已大幅度降低,水中主要污染物为大分子难降解有机物,再将生化出水导入高级氧化处理装置即UV+Fenton高级氧化处理装置,经高级氧化处理后,提高水质可生化性,最后再次采用膜生物反应器,即二次生化处理技术使得出水最终符合排放标准;The landfill leachate passes through the adjustment tank and the water pump once through the primary sedimentation tank and ammonia stripping tower in the physical and chemical pretreatment stage, and then enters the primary biochemical treatment device, namely the membrane bioreactor. After the above treatment, the biochemical properties of the landfill leachate have been greatly improved. The main pollutants in the water are macromolecular refractory organic substances, and then the biochemical effluent is introduced into the advanced oxidation treatment device, that is, the UV+Fenton advanced oxidation treatment device. After advanced oxidation treatment, the biodegradability of the water quality is improved, and finally the membrane bioreactor is used again , that is, the secondary biochemical treatment technology makes the effluent finally meet the discharge standard; 所述物化预处理是以混凝沉淀、吹脱物理化学方法为主体的预处理工艺;The physical and chemical pretreatment is a pretreatment process mainly based on coagulation precipitation and stripping physical and chemical methods; 所述一次生化处理是以UASB即上流式厌氧污泥床、ABR即厌氧折流板反应器工艺厌氧工艺和以接触氧化、氧化沟、A/O工艺好氧工艺为主体的生化处理工艺;The primary biochemical treatment is a biochemical treatment based on UASB (upflow anaerobic sludge bed), ABR (anaerobic baffle reactor process anaerobic process) and contact oxidation, oxidation ditch, A/O process aerobic process. process; 所述高级氧化处理工艺是以UV+Fenton、O3高级氧化技术为其主体的高级氧化处理工艺;The advanced oxidation treatment process is an advanced oxidation treatment process based on UV+Fenton and O3 advanced oxidation technology; 所述二次生化处理是以膜生物反应器即MBR、曝气生物滤池即BAF工艺为主体的后续生化处理工艺。The secondary biochemical treatment is a follow-up biochemical treatment process mainly composed of membrane bioreactor (MBR) and biological aerated filter (BAF).
CN201611260081.4A 2016-12-30 2016-12-30 Combined treatment process of landfill leachate Pending CN106673362A (en)

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CN107416962A (en) * 2017-07-12 2017-12-01 连云港亿尚景水务有限公司 A kind of advanced oxidation equipment and sewage disposal system
CN109052806A (en) * 2018-07-23 2018-12-21 安吉钰禾环保科技有限公司 A kind of garbage leachate treatment device and method based on A/O- electrochemical oxidation-BAF group technology
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CN111675447A (en) * 2020-07-17 2020-09-18 苏州中环建科环境科技有限公司 Treatment process of waste permeating filtrate of small and medium kitchen waste treatment station

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