CN205442960U - A landfill leachate treatment system - Google Patents

A landfill leachate treatment system Download PDF

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Publication number
CN205442960U
CN205442960U CN201521129404.7U CN201521129404U CN205442960U CN 205442960 U CN205442960 U CN 205442960U CN 201521129404 U CN201521129404 U CN 201521129404U CN 205442960 U CN205442960 U CN 205442960U
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tank
sedimentation tank
landfill leachate
treating system
liquid treating
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毛绪
岳昕
刘嵘
王纲
高亮
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Guangzhou Chuangneng Environmental Protection Technology Co ltd
Beijing Oriental Union Medical Biotechnology Co ltd
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Guangzhou Chuangneng Environmental Protection Technology Co ltd
Beijing Oriental Union Medical Biotechnology Co ltd
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Abstract

The utility model belongs to the effluent disposal system, concretely relates to landfill leachate treatment system. The landfill leachate treatment system comprises an active bacteria group bioreactor, a first regulating tank, a first dosing mixing tank, a first sedimentation tank, an aeration tank, a second regulating tank, a second dosing mixing tank and a second sedimentation tank which are connected in sequence; the landfill leachate treatment system also comprises a sludge dewatering device; the first sedimentation tank and the second sedimentation tank are respectively connected with a sludge dewatering device. The utility model discloses the system is simple, the treatment effect is reliable and stable, and the mud after the dehydration can reach the moisture content below 60%, and area is less, and processing cost is lower, and no secondary pollution produces.

Description

一种垃圾渗滤液处理系统A landfill leachate treatment system

技术领域 technical field

本实用新型属于废水处理系统,具体涉及一种垃圾渗滤液处理系统。 The utility model belongs to a waste water treatment system, in particular to a landfill leachate treatment system.

背景技术 Background technique

生活垃圾在堆放和填埋过程中由于压实、发酵等生物化学降解作用,同时在降水和地下水的渗流作用下产生了一种高浓度的有机或无机成份的液体,即被称为垃圾渗滤液。 During the stacking and landfilling of domestic waste, due to biochemical degradation such as compaction and fermentation, and at the same time, a liquid with a high concentration of organic or inorganic components is produced under the seepage of precipitation and groundwater, which is called landfill leachate. .

垃圾渗滤液污染物浓度高,CODcr、BOD5浓度最高值可达数千至几万,且水质复杂,含有多种有毒有害的无机物和有机物。垃圾渗滤液和城市污水相比,浓度高得多,所以渗滤液不经过严格的处理是不可以直接排入城市污水处理管道的。 Landfill leachate has a high concentration of pollutants, the highest concentration of CODcr and BOD5 can reach thousands to tens of thousands, and the water quality is complex, containing a variety of toxic and harmful inorganic and organic substances. Compared with urban sewage, landfill leachate has a much higher concentration, so leachate cannot be directly discharged into urban sewage treatment pipes without strict treatment.

目前垃圾渗滤液的处理方法主要是生物法和膜法结合、蒸发法。传统的物化法由于受制于药剂的使用量过大以及会造成二次污染问题而多用于垃圾渗滤液预处理方面。垃圾渗滤液的生物法耗能较大、而且由于垃圾渗滤液中的碳氮磷比例不合适会造成运行管理困难并增加运行成本;蒸发法耗能较大,且会产生臭气和氨气而造成二次污染。 At present, the treatment methods of landfill leachate are mainly the combination of biological method and membrane method, and evaporation method. The traditional physical and chemical method is mostly used in the pretreatment of landfill leachate due to the excessive use of chemicals and the problem of secondary pollution. The biological method of landfill leachate consumes a lot of energy, and because the ratio of carbon, nitrogen and phosphorus in landfill leachate is not suitable, it will cause difficulties in operation and management and increase operating costs; the evaporation method consumes a lot of energy, and will produce odor and ammonia. cause secondary pollution.

实用新型内容 Utility model content

为了克服现有技术的不足和缺点,本实用新型的目的在于提供一种垃圾渗滤液处理系统,该系统处理效果稳定可靠,脱水后的污泥能达到60%以下的含水率,占地面积较小,处理成本较低,无二次污染产生。 In order to overcome the deficiencies and shortcomings of the prior art, the purpose of this utility model is to provide a landfill leachate treatment system, the system has a stable and reliable treatment effect, and the dehydrated sludge can reach a moisture content below 60%, occupying a relatively small area Small, low processing cost, no secondary pollution.

本实用新型的目的通过下述技术方案实现: The purpose of this utility model is achieved through the following technical solutions:

一种垃圾渗滤液处理系统,包括依次连接的活性菌团生物反应器、第一调节池、第一加药混合池、第一沉淀池、曝气池、第二调节池、第二加药混合池、第二沉淀池; A landfill leachate treatment system, comprising sequentially connected active bacterial group bioreactors, a first regulating tank, a first dosing and mixing tank, a first sedimentation tank, an aeration tank, a second regulating tank, and a second dosing and mixing tank pool, the second sedimentation tank;

所述的垃圾渗滤液处理系统还包括污泥脱水装置;第一沉淀池、第二沉淀池分别与污泥脱水装置连接; The landfill leachate treatment system also includes a sludge dewatering device; the first sedimentation tank and the second sedimentation tank are respectively connected to the sludge dewatering device;

所述的垃圾渗滤液处理系统还包括格栅;格栅与活性菌团生物反应器连接; The landfill leachate treatment system also includes a grid; the grid is connected to the bioreactor of the active bacterial mass;

所述的垃圾渗滤液处理系统还包括第一污泥泵;第一沉淀池通过第一污泥泵与污泥脱水装置连接; The landfill leachate treatment system also includes a first sludge pump; the first sedimentation tank is connected to the sludge dewatering device through the first sludge pump;

所述的垃圾渗滤液处理系统还包括第二污泥泵;第二沉淀池通过第二污泥泵与污泥脱水装置连接; The landfill leachate treatment system also includes a second sludge pump; the second sedimentation tank is connected to the sludge dewatering device through the second sludge pump;

优选的,所述的第一沉淀池为斜板沉淀池; Preferably, the first sedimentation tank is a inclined plate sedimentation tank;

优选的,所述的第二沉淀池为斜板沉淀池; Preferably, the second sedimentation tank is an inclined plate sedimentation tank;

优选的,所述的污泥脱水装置为板框压滤机或离心脱水机; Preferably, the sludge dewatering device is a plate and frame filter press or a centrifugal dehydrator;

本实用新型的原理:垃圾渗滤液依次经过格栅、活性菌团生物反应器、第一调节池、第一加药混合池、第一沉淀池、曝气池、第二调节池、第二加药混合池、第二沉淀池进行处理;其中,活性菌团生物反应器内定期投加活性菌团对废水进行初步调节处理;在第一调节池和第二调节池加入酸、碱调节垃圾渗滤液的pH值;在第一加药混合池和第二加药混合池加入高效离子絮凝剂与垃圾渗滤液进行混合;对于第一沉淀池和第二沉淀池沉降下来的污泥,通过污泥泵输送,加入高效离子絮凝剂与污泥混合搅拌后,进入污泥脱水装置。 The principle of the utility model: the landfill leachate passes through the grid, the active bacterial group bioreactor, the first regulating tank, the first dosing mixing tank, the first sedimentation tank, the aeration tank, the second regulating tank, the second adding Medicine mixing tank and the second sedimentation tank for treatment; among them, active bacteria clusters are regularly added to the active bacteria cluster bioreactor for preliminary adjustment and treatment of wastewater; acid and alkali are added to the first adjustment tank and the second adjustment tank to adjust the landfill seepage The pH value of the filtrate; add high-efficiency ion flocculants in the first dosing mixing tank and the second dosing mixing tank to mix with landfill leachate; for the sludge settled in the first sedimentation tank and the second sedimentation tank, through the sludge After pumping, high-efficiency ionic flocculant is added to mix and stir the sludge, and then enter the sludge dewatering device.

本实用新型相对于现有技术,具有如下的优点及效果: Compared with the prior art, the utility model has the following advantages and effects:

(1)本实用新型对垃圾渗滤液的处理,采用先投加活性菌团,能够大幅去除可生物降解的污染物,然后采用高效离子絮凝剂将大多不可生物降解的污染物予以沉淀去除,这种方式能够减少高效离子絮凝剂的用量,保证高效离子絮凝剂的处理效果。 (1) For the treatment of landfill leachate in this utility model, the active bacteria group is added first, which can greatly remove biodegradable pollutants, and then the high-efficiency ion flocculant is used to precipitate and remove most non-biodegradable pollutants. This method can reduce the amount of high-efficiency ion flocculant and ensure the treatment effect of high-efficiency ion flocculant.

(2)沉淀污泥经过污泥脱水装置脱水后,含水率可降至60%以下,可直接填埋或焚烧处置,降低处理费用。 (2) After the sedimentation sludge is dehydrated by the sludge dehydration device, the water content can be reduced to below 60%, and it can be directly landfilled or incinerated to reduce the treatment cost.

(3)垃圾渗滤液在垃圾渗滤液处理系统的停留时间可设计在6小时以内,因此垃圾渗滤液处理系统所占空间较小,便于场地放置。 (3) The residence time of landfill leachate in the landfill leachate treatment system can be designed within 6 hours, so the landfill leachate treatment system occupies less space and is convenient for site placement.

附图说明 Description of drawings

图1是本实用新型垃圾渗滤液处理系统的结构示意图。 Fig. 1 is a structural schematic diagram of the landfill leachate treatment system of the present invention.

具体实施方式 detailed description

下面结合实施例及附图对本实用新型作进一步详细的描述,但本实用新型的实施方式不限于此。 The utility model will be further described in detail below in conjunction with the embodiments and accompanying drawings, but the implementation of the utility model is not limited thereto.

如图1所示,一种垃圾渗滤液处理系统,包括依次连接的活性菌团生物反应器2、第一调节池3、第一加药混合池4、第一沉淀池5、曝气池6、第二调节池7、第二加药混合池8、第二沉淀池9; As shown in Figure 1, a landfill leachate treatment system includes an active bacterial mass bioreactor 2, a first regulating tank 3, a first dosing mixing tank 4, a first sedimentation tank 5, and an aeration tank 6 connected in sequence , the second adjustment tank 7, the second dosing mixing tank 8, the second sedimentation tank 9;

所述的垃圾渗滤液处理系统还包括污泥脱水装置10;第一沉淀池5、第二沉淀池9分别与污泥脱水装置10连接; The landfill leachate treatment system also includes a sludge dewatering device 10; the first settling tank 5 and the second settling tank 9 are respectively connected to the sludge dewatering device 10;

所述的垃圾渗滤液处理系统还包括格栅1;格栅1与活性菌团生物反应器2连接; The landfill leachate treatment system also includes a grille 1; the grille 1 is connected to the bioreactor 2 of active bacterial mass;

所述的垃圾渗滤液处理系统还包括第一污泥泵11;第一沉淀池5通过第一污泥泵11与污泥脱水装置10连接; The landfill leachate treatment system also includes a first sludge pump 11; the first sedimentation tank 5 is connected to the sludge dewatering device 10 through the first sludge pump 11;

所述的垃圾渗滤液处理系统还包括第二污泥泵12;第二沉淀池9通过第二污泥泵12与污泥脱水装置10连接; The landfill leachate treatment system also includes a second sludge pump 12; the second sedimentation tank 9 is connected to the sludge dewatering device 10 through the second sludge pump 12;

优选的,所述的第一沉淀池5为斜板沉淀池; Preferably, the first settling tank 5 is a inclined plate settling tank;

优选的,所述的第二沉淀池9为斜板沉淀池; Preferably, the second settling tank 9 is an inclined plate settling tank;

优选的,所述的污泥脱水装置10为板框压滤机或离心脱水机; Preferably, the sludge dewatering device 10 is a plate and frame filter press or a centrifugal dehydrator;

运用上述垃圾渗滤液处理系统处理垃圾渗滤液的方法,包含如下步骤: The method for using the landfill leachate treatment system to treat landfill leachate includes the following steps:

(1)垃圾发电厂产生的高浓度垃圾渗滤液,先进入格栅1将较大的杂质去除后,然后进入活性菌团生物反应器2,在活性菌团生物反应器定期投加活性菌团(包含好氧菌和厌氧菌,加入量为0.5~1.0升/吨渗滤液)对垃圾渗滤液进行初步调节处理; (1) The high-concentration landfill leachate produced by the waste-to-energy plant first enters the grid 1 to remove larger impurities, and then enters the active bacterial mass bioreactor 2, and regularly adds active bacterial mass to the active bacterial mass bioreactor (including aerobic bacteria and anaerobic bacteria, the addition amount is 0.5-1.0 liters per ton of leachate) for preliminary adjustment of landfill leachate;

(2)经过初步调节处理的垃圾渗透液进入第一调节池3,加酸将垃圾渗透液pH值降低到4,然后再加碱将垃圾渗透液pH值调节到7,进而杀死污水里的细菌,避免对高效离子絮凝剂产生负作用;然后垃圾渗透液进入第一混合加药池4,并在第一混合加药池4中加入高效离子絮凝剂(主要由硅酸铝类混合物、氢氧化钙和核聚糖构成,加入量为50~100克/吨渗滤液),垃圾渗透液经过快速搅拌(1500转/分钟),再经过慢速搅拌(750转/分钟)后,进入第一沉淀池5;随后进入曝气池6进行曝气处理(曝气方式为连续曝气); (2) The garbage permeate through preliminary adjustment enters the first adjustment tank 3, and acid is added to reduce the pH value of the garbage permeate to 4, and then alkali is added to adjust the pH value of the garbage permeate to 7, thereby killing the sewage in the waste water. Bacteria, to avoid negative effects on the high-efficiency ion flocculant; then the garbage permeate enters the first mixed dosing pool 4, and the high-efficiency ion flocculant (mainly composed of aluminum silicate mixture, hydrogen Calcium oxide and nucleoside, the addition amount is 50-100 g/ton of leachate), the garbage permeate is stirred rapidly (1500 rpm), and then stirred slowly (750 rpm), and enters the first Sedimentation tank 5; Then enter the aeration tank 6 for aeration treatment (the aeration mode is continuous aeration);

(3)经过步骤(2)处理后的废水进入第二调节池7将pH值调节到7,再进入第二混合加药池8,并在第二混合加药池8加入高效离子絮凝剂;废水经过快速搅拌(1500转/分钟),再经过慢速搅拌(750转/分钟)后,然后进入第二沉淀池9,第二沉淀池9的出水能够达到《污水排入城镇下水道水质标准》(CJ343-2010)和污水综合排放三级标准排入城市污水管网; (3) The waste water after step (2) treatment enters the second regulating pond 7 and the pH value is adjusted to 7, then enters the second mixing and dosing pond 8, and adds high-efficiency ion flocculant in the second mixing and dosing pond 8; The waste water enters the second settling tank 9 after rapid stirring (1500 rpm) and slow stirring (750 rpm), and the effluent of the second settling tank 9 can reach the "Water Quality Standard for Sewage Discharged into Urban Sewers" (CJ343-2010) and the three-level comprehensive sewage discharge standard are discharged into the urban sewage pipe network;

(4)对于第一沉淀池5和第二沉淀池9沉降下来的污泥,通过第一污泥泵11和第二污泥泵12输送,加入高效离子絮凝剂与污泥混合搅拌后,进入污泥脱水装置10进行脱水处理。 (4) For the sludge settled in the first sedimentation tank 5 and the second sedimentation tank 9, it is transported by the first sludge pump 11 and the second sludge pump 12, and after adding high-efficiency ion flocculant and mixing with the sludge, it enters The sludge dehydrator 10 performs dehydration processing.

本实用新型系统简单、处理效果稳定可靠,脱水后的污泥能达到60%以下的含水率,垃圾渗滤液在垃圾渗滤液处理系统的停留时间可设计在6小时以内,占地面积较小,便于场地放置,处理成本较低,无二次污染产生。 The utility model has the advantages of simple system, stable and reliable treatment effect, the water content of the dehydrated sludge can reach below 60%, the residence time of the landfill leachate in the landfill leachate treatment system can be designed within 6 hours, and the occupied area is small. It is convenient to place on the site, the treatment cost is low, and there is no secondary pollution.

上述实施例为本实用新型较佳的实施方式,但本实用新型的实施方式并不受上述实施例的限制,其他的任何未背离本实用新型的精神实质与原理下所作的改变、修饰、替代、组合、简化,均应为等效的置换方式,都包含在本实用新型的保护范围之内。 The above-mentioned embodiment is a preferred implementation mode of the present utility model, but the implementation mode of the present utility model is not limited by the above-mentioned embodiment, and any other changes, modifications and substitutions made without departing from the spirit and principle of the present utility model , combination, and simplification, all should be equivalent replacement methods, and are all included in the protection scope of the present utility model.

Claims (8)

1. a garbage percolation liquid treating system, it is characterised in that: the active cenobium bioreactor that includes being sequentially connected with, the first regulating reservoir, the first dosing mixing pit, the first sedimentation tank, Aeration tank, the second regulating reservoir, the second dosing mixing pit, the second sedimentation tank.
Garbage percolation liquid treating system the most according to claim 1, it is characterised in that:
Described garbage percolation liquid treating system also includes grid;Grid is connected with activity cenobium bioreactor.
Garbage percolation liquid treating system the most according to claim 1, it is characterised in that:
Described garbage percolation liquid treating system also includes sludge dehydration device;First sedimentation tank, the second sedimentation tank are connected with sludge dehydration device respectively.
Garbage percolation liquid treating system the most according to claim 3, it is characterised in that:
Described garbage percolation liquid treating system also includes the first sludge pump;First sedimentation tank is connected with sludge dehydration device by the first sludge pump.
Garbage percolation liquid treating system the most according to claim 3, it is characterised in that:
Described garbage percolation liquid treating system also includes the second sludge pump;Second sedimentation tank is connected with sludge dehydration device by the second sludge pump.
Garbage percolation liquid treating system the most according to claim 1, it is characterised in that:
The first described sedimentation tank is inclined-plate clarifying basin.
Garbage percolation liquid treating system the most according to claim 1, it is characterised in that:
The second described sedimentation tank is inclined-plate clarifying basin.
Garbage percolation liquid treating system the most according to claim 3, it is characterised in that:
Described sludge dehydration device is filter press or centrifugal dehydrator.
CN201521129404.7U 2015-12-30 2015-12-30 A landfill leachate treatment system Expired - Fee Related CN205442960U (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111453925A (en) * 2020-04-20 2020-07-28 山东苏柯汉生物工程股份有限公司 Landfill leachate sewage treatment method
CN119176643A (en) * 2024-11-08 2024-12-24 重庆创绿环境保护有限公司 Biochemical treatment process for percolate

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111453925A (en) * 2020-04-20 2020-07-28 山东苏柯汉生物工程股份有限公司 Landfill leachate sewage treatment method
CN119176643A (en) * 2024-11-08 2024-12-24 重庆创绿环境保护有限公司 Biochemical treatment process for percolate

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