CN101306876A - A device for treating landfill leachate - Google Patents
A device for treating landfill leachate Download PDFInfo
- Publication number
- CN101306876A CN101306876A CNA2008100123218A CN200810012321A CN101306876A CN 101306876 A CN101306876 A CN 101306876A CN A2008100123218 A CNA2008100123218 A CN A2008100123218A CN 200810012321 A CN200810012321 A CN 200810012321A CN 101306876 A CN101306876 A CN 101306876A
- Authority
- CN
- China
- Prior art keywords
- landfill leachate
- bioreactor
- water tank
- treatment
- membrane
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Images
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
一种处理垃圾渗滤液的装置,涉及环境保护领域处理垃圾渗滤液的装置。包括有上流式厌氧生物反应器(2),虹吸管(3),中间水箱(4),膜生物反应器(5),曝气管(6),膜组件(7)构成,所述上流式厌氧生物反应器(2)经虹吸管(3)与中间水箱(4)相连;中间水箱(4)与膜生物反应器(5),曝气管(6),膜组件(7)相连至出水管(8)。该装置主要应用于处理城市垃圾渗滤液。同时应用于啤酒、饮料等轻工业、屠宰行业等高浓度废水的处理。
A device for treating landfill leachate relates to a device for treating landfill leachate in the field of environmental protection. Comprising an upflow anaerobic bioreactor (2), a siphon (3), an intermediate water tank (4), a membrane bioreactor (5), an aeration tube (6), and a membrane module (7), the upflow The anaerobic bioreactor (2) is connected to the intermediate water tank (4) through the siphon (3); the intermediate water tank (4) is connected to the membrane bioreactor (5), the aeration pipe (6), and the membrane module (7) to the outlet water pipe (8). The device is mainly used in the treatment of urban landfill leachate. At the same time, it is used in the treatment of high-concentration wastewater in light industries such as beer and beverages, and in slaughtering industries.
Description
技术领域 technical field
本发明涉及环境保护领域处理垃圾渗滤液的装置,特别是利用上流式厌氧生物反应器与膜生物反应器处理垃圾渗滤液的装置。The invention relates to a device for treating landfill leachate in the field of environmental protection, in particular to a device for treating landfill leachate by using an upflow anaerobic bioreactor and a membrane bioreactor.
背景技术 Background technique
随着工业的迅速发展、人民生活水平的不断提高,城市垃圾也呈线性增加,对垃圾渗滤液的处理势在必行。With the rapid development of industry and the continuous improvement of people's living standards, urban waste also increases linearly, and the treatment of landfill leachate is imperative.
生物处理是垃圾渗滤液的一种主体处理方法。生物处理法的具体技术装置形式有传统活性污泥法、稳定塘法、生物转盘法、SBR好氧处理技术装置、UASB厌氧处理技术装置、厌氧固定膜生物反应器等。其中活性污泥法、生物转盘和SBR好氧处理技术装置等,它们的处理效果好、水力停留时间较短、运行经验丰富、但工程投资大、能耗大、运行管理费用高;相对来说稳定塘法处理(好氧生物处理与厌氧生物处理的结合)比较简单、投资省、管理方便,但污水停留时间长、占地面积大、对粒径较大的有机分子去除效果差且净化能力随季节变化较大。单独采用上流式厌氧污泥床(UASB)可很大程度上的降低CODcr,但其出水CODcr值仍然很高,而且垃圾渗滤液里也含有大量的病源微生物,出水水质仍然达不到二级排放标准。目前城市垃圾渗滤液处理工艺,多采用厌氧-好氧生物处理技术装置。但国内已建成的城市垃圾填埋场的垃圾渗滤液污水处理厂普遍存在运行效果差的现象。其主要原因是这些垃圾渗滤液处理厂所采用的常规技术装置及其工艺参数不适合复杂多变的垃圾渗滤液废水;同时渗滤液本身存在C/N不协调的特点,采用一般的好氧活性污泥法处理技术装置,污泥培养困难、污泥活性差。Biological treatment is a main treatment method for landfill leachate. The specific technical device forms of biological treatment methods include traditional activated sludge method, stabilization pond method, biological turntable method, SBR aerobic treatment technology device, UASB anaerobic treatment technology device, anaerobic fixed film bioreactor, etc. Among them, activated sludge method, biological turntable and SBR aerobic treatment technology devices have good treatment effect, short hydraulic retention time and rich operation experience, but the project investment is large, energy consumption is large, and operation and management costs are high; relatively speaking Stabilized pond treatment (combination of aerobic biological treatment and anaerobic biological treatment) is relatively simple, low in investment, and convenient in management, but the residence time of sewage is long, the floor area is large, and the removal effect on organic molecules with large particle sizes is poor and the purification Capacity varies greatly with the seasons. Using upflow anaerobic sludge blanket (UASB) alone can greatly reduce CODcr, but the CODcr value of the effluent is still high, and the landfill leachate also contains a large number of pathogenic microorganisms, and the effluent quality is still not up to the second grade Emission Standards. At present, the treatment process of urban landfill leachate mostly adopts anaerobic-aerobic biological treatment technology devices. However, the landfill leachate sewage treatment plants that have been built in China generally have poor operation effects. The main reason is that the conventional technical devices and process parameters used by these landfill leachate treatment plants are not suitable for the complex and changeable landfill leachate wastewater; at the same time, the leachate itself has the characteristics of C/N inconsistency, and the general aerobic activity Sludge treatment technology equipment, sludge cultivation is difficult, and sludge activity is poor.
发明内容 Contents of the invention
本发明的目的在于提供一种垃圾渗滤液处理装置。利用上流式厌氧生物反应器与膜生物反应器联合处理垃圾渗滤液的装置,能有效的处理城市垃圾渗滤液,出水水质较好。The object of the present invention is to provide a landfill leachate treatment device. The device for combined treatment of landfill leachate by using an upflow anaerobic bioreactor and a membrane bioreactor can effectively treat urban landfill leachate, and the effluent water quality is good.
本发明的目的是通过以下技术方案实现的:The purpose of the present invention is achieved through the following technical solutions:
一种处理垃圾渗滤液的装置,包括有上流式厌氧生物反应器,虹吸管,中间水箱,膜生物反应器,曝气管,膜组件构成,所述上流式厌氧生物反应器经虹吸管与中间水箱相连;中间水箱与膜生物反应器,曝气管,膜组件相连至出水管。A device for treating landfill leachate, comprising an upflow anaerobic bioreactor, a siphon, an intermediate water tank, a membrane bioreactor, an aeration tube, and a membrane module, the upflow anaerobic bioreactor is connected to the middle through the siphon The water tanks are connected; the middle water tank is connected to the membrane bioreactor, the aeration pipe, and the membrane module to the outlet pipe.
本发明的有益效果是:The beneficial effects of the present invention are:
1.高效性:膜组件可以提高膜生物反应器中混合液浓度,使泥龄增长、剩余污泥量减少、出水水质显著提高;1. Efficiency: Membrane modules can increase the concentration of the mixed solution in the membrane bioreactor, increase the sludge age, reduce the amount of residual sludge, and significantly improve the quality of effluent water;
2.稳定性:膜组件的截留几乎可使SS的去除率达100%,同时对色度也有很好的去除效果;2. Stability: The interception of the membrane module can almost make the removal rate of SS reach 100%, and it also has a good removal effect on chroma;
3.经济性:UASB的高有机负荷特性可大大降低反应器的占地面积及动力消耗。3. Economy: The high organic load of UASB can greatly reduce the area occupied by the reactor and power consumption.
附图说明 Description of drawings
图1为本发明装置构成示意图。Fig. 1 is a schematic diagram of the structure of the device of the present invention.
图中标号:1.进水管,2.UASB,3.虹吸管,4.中间水箱,5.膜生物反应器,6.曝气管,7.膜组件,8.出水管。Labels in the figure: 1. Water inlet pipe, 2. UASB, 3. Siphon pipe, 4. Intermediate water tank, 5. Membrane bioreactor, 6. Aeration pipe, 7. Membrane module, 8. Water outlet pipe.
具体实施方式 Detailed ways
在图1中,垃圾渗滤液经过进水管1进入UASB(上流式厌氧生物反应器)2,进行预处理,UASB反应器内MLSS为5000~10000mg/L,由于垃圾渗滤液有机浓度很高,可以产生大量的甲烷气体,微小气体附着在颗粒污泥上上浮,在加上进水具有一定的流速,使底部污泥得以提升。到达三相分离器后进行气、液、固分离,气体逸出,颗粒污泥下沉,预处理液经过虹吸管3流入中间水箱4,中间水箱既有收集预处理液作用,还有对后续膜生物反应器5进水通过曝气管6起稳定流速的作用。从中间水箱出来的含有大量难降解有机物的水流入膜生物反应器5,由于膜生物反应器5中膜组件7有很强的固液分离功能,可使反应器中活性污泥一直保持较高水平,从而提高生物反应器的处理能力;其次是膜组件对水中大分子物质和生物难降解有机物质有截留作用,增加了它们在反应器内的停留时间,使它们发生水解酸化作用,大分子物质被水解成小分子物质,同时MBR有富集难降解有机物分解菌的作用,从而使处理后流出出水管8的垃圾渗滤液大大提高有机质去除率。UASB在常温条件下对高浓度的垃圾渗滤液进行预处理,对BOD去除率可大于90%。由于UASB的COD负荷可高达10kg·m-3d-1,反应过程中也无需能耗,因此与好氧工艺相比,可大大节约反应器的占地面积及动力消耗。对于UASB处理后的出水,由于膜生物反应器(MBR)中泥龄长,可富集了大量难降解有机物分解菌和硝化菌等增殖速度慢的微生物,能大大提高难降解有机物的去除率。In Figure 1, the landfill leachate enters the UASB (upflow anaerobic bioreactor) 2 through the
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNA2008100123218A CN101306876A (en) | 2008-07-15 | 2008-07-15 | A device for treating landfill leachate |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNA2008100123218A CN101306876A (en) | 2008-07-15 | 2008-07-15 | A device for treating landfill leachate |
Publications (1)
Publication Number | Publication Date |
---|---|
CN101306876A true CN101306876A (en) | 2008-11-19 |
Family
ID=40123587
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CNA2008100123218A Pending CN101306876A (en) | 2008-07-15 | 2008-07-15 | A device for treating landfill leachate |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN101306876A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101805095A (en) * | 2010-03-25 | 2010-08-18 | 深圳清华大学研究院 | Method for treating and recycling leachate in garbage transfer station |
-
2008
- 2008-07-15 CN CNA2008100123218A patent/CN101306876A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101805095A (en) * | 2010-03-25 | 2010-08-18 | 深圳清华大学研究院 | Method for treating and recycling leachate in garbage transfer station |
CN101805095B (en) * | 2010-03-25 | 2012-09-19 | 深圳清华大学研究院 | Leachate Treatment and Reuse Method of Garbage Transfer Station |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN103641272B (en) | High concentrated organic wastewater and percolate zero-discharge treatment system | |
CN103395937B (en) | Processing device and processing method applicable to high-ammonia-nitrogen agricultural wastewater | |
CN102557356B (en) | Semi-short-cut nitrification/anammox process and method for denitrification and phosphorus removal of urban sewage | |
CN101723559B (en) | Process for processing saccharin sodium wastewater | |
CN102101742A (en) | Method for treating organic wastewater containing high-concentration ammonia nitrogen | |
Ji et al. | Integrated ABR and UASB system for dairy wastewater treatment: Engineering design and practice | |
CN103359876A (en) | Harmless dimethylacetamide wastewater treatment method | |
CN102020402A (en) | Energy-saving sewage treatment method by membrane biological reactor (MBR) process | |
CN101817615A (en) | Anaerobic-sequencing batch biofilm reactor-artificial wetland method for treating piggery wastewater | |
CN101376553A (en) | Method for processing low temperature sewerage using low-intensity ultrasonic strengthened membrane bioreactor | |
CN102531269A (en) | Pig farm wastewater treatment method | |
CN201932982U (en) | Combined system using micro-electrolysis-MBR (membrane bio-reactor) combined technology to treat printing and dyeing wastewater | |
CN105645687A (en) | Sewage biological reaction device and process integrating PHAs synthesis and nitrogen and phosphorus removal | |
CN102249480A (en) | System and operating method for treating rubbish leachate and urban household sewage in combined way | |
CN204079721U (en) | A kind of sewage disposal device adopting pure oxygen aeration and remaining oxygen reuse | |
CN105417765B (en) | A kind of municipal sewage organic carbon enriching and recovering utilizes device and its application method | |
CN204138504U (en) | Garbage leachate treatment device | |
CN208345988U (en) | A kind of small-town sewage treatment system based on anaerobism MBR technology | |
CN204417278U (en) | Culturing wastewater processing system | |
CN201406361Y (en) | A landfill leachate wastewater treatment device | |
CN103466897B (en) | Waste water processing method | |
CN111362505A (en) | A process for treating pig farm wastewater | |
CN203144240U (en) | Biological reaction device for treating and recycling cultivation wastewater | |
CN205313331U (en) | Treatment of domestic sewage retrieval and utilization equipment | |
CN201753302U (en) | Experimental device for treating high ammonia nitrogen leachate with single-stage anoxic/anaerobic UASB - A/O process |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C12 | Rejection of a patent application after its publication | ||
RJ01 | Rejection of invention patent application after publication |
Open date: 20081119 |