CN207671790U - A kind of landfill leachate advanced treatment system - Google Patents

A kind of landfill leachate advanced treatment system Download PDF

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CN207671790U
CN207671790U CN201721642150.8U CN201721642150U CN207671790U CN 207671790 U CN207671790 U CN 207671790U CN 201721642150 U CN201721642150 U CN 201721642150U CN 207671790 U CN207671790 U CN 207671790U
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water
membrane
water outlet
treatment system
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喻本宏
甘栋平
王佳洪
王晓华
吴太军
陶学问
杨智恒
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Chongqing Sanfeng Covanta Environmental Industry Co ltd
Chongqing Sanfeng Environment Group Co ltd
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Chongqing Three Peak Technology Co Ltd
CHONGQING SANFENG ENVIRONMENTAL INDUSTRY GROUP CO LTD
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Abstract

本实用新型涉及一种垃圾渗滤液深度处理系统,属于污水资源化利用技术领域。该系统包括原水罐单元、过滤单元、高压泵(组)单元、在线增压泵单元、膜组单元、仪表单元、产水罐单元和清洗单元;所述原水罐单元的进水口与渗滤液处理系统的出水口连接,原水罐单元的出水口与过滤单元的进水口连接,过滤单元的出水口与高压泵单元的进水口连接,高压泵单元的出水口与在线增压泵单元的进水口连接,在线增压泵单元的出水口与膜组单元的进水口连接,膜组单元的出水口分别与产水罐单元、仪表单元连接,仪表单元还与清洗单元连接,清洗单元与过滤单元连接。本实用新型结构紧凑,产水水质好且连续稳定,运行维护方便,出水可回用于垃圾焚烧发电厂。

The utility model relates to a garbage leachate advanced treatment system, which belongs to the technical field of sewage resource utilization. The system includes a raw water tank unit, a filter unit, a high-pressure pump (group) unit, an online booster pump unit, a membrane unit, an instrument unit, a produced water tank unit and a cleaning unit; the water inlet of the raw water tank unit and the leachate treatment The water outlet of the system is connected, the water outlet of the raw water tank unit is connected with the water inlet of the filter unit, the water outlet of the filter unit is connected with the water inlet of the high-pressure pump unit, and the water outlet of the high-pressure pump unit is connected with the water inlet of the online booster pump unit , the water outlet of the online booster pump unit is connected to the water inlet of the membrane unit, the water outlet of the membrane unit is respectively connected to the water production tank unit and the instrument unit, the instrument unit is also connected to the cleaning unit, and the cleaning unit is connected to the filter unit. The utility model has the advantages of compact structure, good and continuous and stable water quality, convenient operation and maintenance, and the effluent can be reused for waste incineration power plants.

Description

一种垃圾渗滤液深度处理系统A landfill leachate advanced treatment system

技术领域technical field

本实用新型涉及污水资源化利用技术领域,具体涉及一种垃圾渗滤液深度处理系统。The utility model relates to the technical field of sewage resource utilization, in particular to an advanced treatment system for landfill leachate.

背景技术Background technique

目前,我国城市生活垃圾的处理主要采用填埋技术或焚烧技术,无论在填埋或焚烧处理过程中都会产生垃圾渗滤液。垃圾渗滤液中CODcr浓度约6000-70000mg/L,NH3-N浓度约1000-2500mg/L,同时含有大量溶解性固体(钠、钙、氯化物、硫酸盐等),是一种水质水量变化大、成分极其复杂、污染物浓度高的有机废水,并伴有极重的腐败臭味,如不妥善处理,会对周围的水体和土壤造成严重污染,对周边人民群众的身体健康产生严重威胁。At present, landfill technology or incineration technology is mainly used for the treatment of municipal solid waste in my country, and landfill leachate will be generated in the process of landfill or incineration treatment. The concentration of CODcr in landfill leachate is about 6000-70000mg/L, and the concentration of NH 3 -N is about 1000-2500mg/L. It also contains a large amount of dissolved solids (sodium, calcium, chloride, sulfate, etc.), which is a change in water quality and water quantity. Organic wastewater with large volume, extremely complex composition and high concentration of pollutants, accompanied by a very heavy odor of corruption, if not properly treated, will cause serious pollution to the surrounding water and soil, and pose a serious threat to the health of the surrounding people .

随着社会的进步与发展,环境容量逐渐减小,环境承载力逐渐降低及随经济的发展带来的水资源的日益短缺,迫切要求开发污水资源化技术。目前垃圾渗滤液资源化利用所采用的主流工艺为生化处理+深度处理,由于垃圾渗滤液中含有较多的难降解有机物,常规的生化出水需通过深度处理技术进一步处理方可达标回用;膜技术和Fenton氧化、臭氧氧化等高级氧化技术相比,具有稳定达标的显著优势,因此,目前仍是深度处理的主流技术。然而,纳滤膜、卷式反渗透膜等低压膜系统由于污染物去除率低、产水率低而不能直接用于垃圾渗滤液资源化利用的深度处理。With the progress and development of the society, the environmental capacity is gradually reduced, the environmental carrying capacity is gradually reduced, and the water resources are increasingly scarce with the development of the economy, which urgently requires the development of sewage resource technology. At present, the mainstream process adopted for resource utilization of landfill leachate is biochemical treatment + advanced treatment. Since landfill leachate contains more refractory organic matter, conventional biochemical effluent needs to be further treated by advanced treatment technology before it can meet the standard for reuse; Compared with advanced oxidation technologies such as Fenton oxidation and ozone oxidation, this technology has a significant advantage of being stable and up to standard. Therefore, it is still the mainstream technology for advanced treatment. However, low-pressure membrane systems such as nanofiltration membranes and roll-type reverse osmosis membranes cannot be directly used for advanced treatment of landfill leachate resource utilization due to low pollutant removal rate and low water production rate.

实用新型内容Utility model content

有鉴于此,本实用新型的目的在于提供一种垃圾渗滤液深度处理系统,通过该系统对渗滤液处理超滤出水、生活污水、生产污水进行深度处理达标后回用,从而实现垃圾焚烧发电厂污水资源化利用。In view of this, the purpose of this utility model is to provide a landfill leachate advanced treatment system, through which the leachate treatment ultrafiltration effluent, domestic sewage, and production sewage can be reused after advanced treatment reaches the standard, so as to realize the waste incineration power plant Utilization of sewage resources.

为达到上述目的,本实用新型提供如下技术方案:In order to achieve the above object, the utility model provides the following technical solutions:

一种垃圾渗滤液深度处理系统,所述渗滤液深度处理系统包括原水罐单元、过滤单元、高压泵单元、在线增压泵单元、膜组单元、仪表单元、产水罐单元和清洗单元;所述原水罐单元的进水口与渗滤液处理系统的出水口连接,原水罐单元的出水口与过滤单元的进水口连接,过滤单元的出水口与高压泵单元的进水口连接,高压泵单元的出水口与在线增压泵单元的进水口连接,在线增压泵单元的出水口与膜组单元的进水口连接,膜组单元的出水口分别与产水罐单元、仪表单元连接,仪表单元还与清洗单元连接,清洗单元与过滤单元连接。A landfill leachate advanced treatment system, the leachate advanced treatment system includes a raw water tank unit, a filter unit, a high-pressure pump unit, an online booster pump unit, a membrane unit, an instrument unit, a produced water tank unit, and a cleaning unit; The water inlet of the raw water tank unit is connected to the water outlet of the leachate treatment system, the water outlet of the raw water tank unit is connected to the water inlet of the filter unit, the water outlet of the filter unit is connected to the water inlet of the high-pressure pump unit, and the outlet of the high-pressure pump unit The water port is connected to the water inlet of the online booster pump unit, the water outlet of the online booster pump unit is connected to the water inlet of the membrane unit, the water outlet of the membrane unit is respectively connected to the water production tank unit and the instrument unit, and the instrument unit is also connected to the The cleaning unit is connected, and the cleaning unit is connected with the filter unit.

进一步,还包括加酸单元,所述加酸单元与原水罐单元连接。Further, an acid addition unit is also included, and the acid addition unit is connected with the raw water tank unit.

进一步,还包括阻垢剂单元,所述阻垢剂单元连接于原水罐单元与过滤单元之间的管道上。Further, a scale inhibitor unit is also included, and the scale inhibitor unit is connected to the pipeline between the raw water tank unit and the filter unit.

进一步,还包括加碱单元,所述加碱单元与产水罐单元连接。Further, an alkali addition unit is also included, and the alkali addition unit is connected with the produced water tank unit.

进一步,所述膜组单元由多支膜元件按特定方式排列组成,其中每支膜元件包括原水进水管、浓缩水出水管、中心管和缠绕中心管上的特殊反渗透膜层,中心管的上端设置有上端盖和唇型密封环,中心管的下端设置有下端盖和唇型密封环,所述中心管上设置有若干小孔,中心管的下端设置有纯水出水口。Further, the membrane group unit is composed of multiple membrane elements arranged in a specific way, wherein each membrane element includes a raw water inlet pipe, a concentrated water outlet pipe, a central pipe and a special reverse osmosis membrane layer wound on the central pipe, and the center pipe The upper end is provided with an upper end cover and a lip-shaped sealing ring, and the lower end of the central tube is provided with a lower end cover and a lip-shaped sealing ring. The central tube is provided with several small holes, and the lower end of the central tube is provided with a pure water outlet.

进一步,所述膜组件还包括导流分配盘,所述导流分配盘设置于反渗透膜组进料端面。Further, the membrane module further includes a diversion distribution plate, and the diversion distribution plate is arranged on the feed end surface of the reverse osmosis membrane group.

进一步,所述反渗透膜组的内部导流网格为梯形结构。Further, the internal guide grid of the reverse osmosis membrane group has a trapezoidal structure.

本实用新型的有益效果在于:本实用新型结构紧凑,产水水质好且连续稳定,运行维护方便,出水可回用于垃圾焚烧发电厂。The beneficial effects of the utility model are that the utility model has compact structure, good and continuous and stable water quality, convenient operation and maintenance, and the effluent can be reused for waste incineration power plants.

附图说明Description of drawings

为了使本实用新型的目的、技术方案和优点更加清楚,下面将结合附图对本实用新型作进一步的详细描述,其中:In order to make the purpose, technical solutions and advantages of the utility model more clear, the utility model will be further described in detail below in conjunction with the accompanying drawings, wherein:

图1为本实用新型的结构框图;Fig. 1 is a block diagram of the utility model;

图2为膜组单元的结构简图。Figure 2 is a schematic diagram of the structure of the membrane unit.

具体实施方式Detailed ways

下面将结合附图,对本实用新型的优选实施例进行详细的描述。The preferred embodiments of the present utility model will be described in detail below in conjunction with the accompanying drawings.

在本实施例中,所述的深度处理系统如图1所示,包括原水罐单元、过滤单元、高压泵单元、在线增压泵单元、膜组单元、仪表单元、产水罐单元和清洗单元;所述原水罐单元的进水口与渗滤液处理系统的出水口连接,原水罐单元的出水口与过滤单元的进水口连接,过滤单元的出水口与高压泵单元的进水口连接,高压泵单元的出水口与在线增压泵单元的进水口连接,在线增压泵单元的出水口与膜组单元的进水口连接,膜组单元的出水口分别与产水罐单元、仪表单元连接,仪表单元还与清洗单元连接,清洗单元与过滤单元连接。In this embodiment, the advanced treatment system as shown in Figure 1 includes a raw water tank unit, a filter unit, a high-pressure pump unit, an online booster pump unit, a membrane unit, an instrument unit, a produced water tank unit, and a cleaning unit The water inlet of the raw water tank unit is connected with the water outlet of the leachate treatment system, the water outlet of the raw water tank unit is connected with the water inlet of the filter unit, the water outlet of the filter unit is connected with the water inlet of the high-pressure pump unit, and the high-pressure pump unit The water outlet of the online booster pump unit is connected to the water inlet of the online booster pump unit, the water outlet of the online booster pump unit is connected to the water inlet of the membrane unit, the water outlet of the membrane unit is respectively connected to the water production tank unit and the instrument unit, and the instrument unit It is also connected with the cleaning unit, and the cleaning unit is connected with the filter unit.

原水罐单元,具有缓冲、均质、调节作用,用于储存一定量的原水,在系统工作时利用加酸单元加酸调节进水pH值。加酸单元由酸储罐和酸添加计量泵组成,对原水pH动态调节、保证进水pH处于弱酸性,以防止无机盐离子结垢。The raw water tank unit has the functions of buffering, homogenizing and regulating, and is used to store a certain amount of raw water. When the system is working, the acid adding unit is used to add acid to adjust the pH value of the incoming water. The acid addition unit consists of an acid storage tank and an acid addition metering pump, which dynamically adjusts the pH of the raw water to ensure that the pH of the incoming water is weakly acidic to prevent scaling of inorganic salt ions.

过滤单元,用于滤出进水中残余微粒、保护系统膜元件。The filter unit is used to filter out residual particles in the feed water and protect the membrane elements of the system.

高压泵单元,提供能量、使系统内水压升高至渗透压以上,通过对高压泵的变频控制可调节系统的处理能力。The high-pressure pump unit provides energy to raise the water pressure in the system above the osmotic pressure, and the processing capacity of the system can be adjusted through the frequency conversion control of the high-pressure pump.

在线增压单元,系统内增压、补充压力损失。污水在膜组单元中循环过滤,通过膜组单元后管道内压力下降、为保持各段膜单元的循环压力需要对损失的压力进行补充;同时增加内循环提高膜系统产水率。Online pressurization unit, pressurization in the system, make up for pressure loss. Sewage is circulated and filtered in the membrane unit, and the pressure in the pipeline drops after passing through the membrane unit. In order to maintain the circulation pressure of each section of the membrane unit, the lost pressure needs to be supplemented; at the same time, increasing the internal circulation increases the water production rate of the membrane system.

膜组单元,用于分离污水中的盐分离子和其他各类杂质,当高于各组分渗透压的污水在膜管内侧流动时水分子透过膜层到另一侧,去除水中的污染物。The membrane unit is used to separate the salt ions and other impurities in the sewage. When the sewage with the osmotic pressure higher than each component flows inside the membrane tube, the water molecules pass through the membrane layer to the other side to remove the pollutants in the water. .

仪表单元,调节系统压力、pH、调节系统产水率,通过仪表单元上各类传感器的信息反馈自动调节阀,可实现系统运行压力的调节、改变透过膜层的水量比例,以达到设定的产水率要求。The instrument unit can adjust the system pressure, pH, and adjust the water production rate of the system. Through the information feedback of various sensors on the instrument unit, the automatic adjustment valve can realize the adjustment of the system operating pressure and change the proportion of water passing through the membrane layer to achieve the set value. water production rate requirements.

产水罐单元,储存产水、调节均衡产水pH。产水罐能存储缓冲一定量的产水,因产水偏酸性,需要经加碱单元在产水罐单元里加碱调节pH至中性后达标排放。加碱单元,由碱液储罐和碱添加剂计量泵组成,在产水罐内加碱对产水pH进行调节。The product water tank unit stores the product water and adjusts the pH of the product water. The produced water tank can store and buffer a certain amount of produced water. Because the produced water is acidic, it is necessary to add alkali to the produced water tank unit through the alkali adding unit to adjust the pH to neutral before discharge. The alkali adding unit is composed of an alkali liquid storage tank and an alkali additive metering pump. Add alkali in the produced water tank to adjust the pH of the produced water.

阻垢剂单元,连接于原水罐单元与过滤单元之间的管道上,由阻垢剂罐和阻垢剂计量泵组成,阻垢剂可以防止污水中的盐分在膜层或管道内壁形成污垢、延长膜使用寿命。The antiscalant unit is connected to the pipeline between the raw water tank unit and the filter unit. It is composed of an antiscalant tank and an antiscalant metering pump. The antiscalant can prevent the salt in the sewage from forming dirt on the film layer or the inner wall of the pipeline. Extend membrane life.

清洗单元,实现膜组单元定期在线清洗。膜深度处理系统进水中含有有机污染物以及钙、镁离子等易结垢组份,在处理中易造成膜的污染和结垢,当膜系统的产水量下降或运行压力上升时,通过开启在线清洗单元对膜进行化学清洗,以保持膜层的性能,延长膜使用寿命。清洗用水可采用系统产水或工业水。The cleaning unit realizes regular on-line cleaning of the membrane unit. The influent of the membrane advanced treatment system contains organic pollutants and components that are prone to scaling such as calcium and magnesium ions. During the treatment, it is easy to cause membrane pollution and scaling. When the water production of the membrane system decreases or the operating pressure increases, by opening The online cleaning unit performs chemical cleaning on the membrane to maintain the performance of the membrane layer and prolong the service life of the membrane. Cleaning water can be system produced water or industrial water.

如图2所示,所述膜组单元包括原水进水管1、浓缩水出水管2、中心管3和缠绕中心管设置的特殊反渗透膜层4,中心管的上端设置有上端盖和唇型密封环5,中心管的下端设置有下端盖和唇型密封环6,所述中心管上设置有若干小孔7,中心管的下端设置有纯水出水口8。所述膜组件还包括导流分配盘9,所述导流分配盘设置于反渗透膜组进料端面。所述反渗透膜组的格网为梯形结构。As shown in Figure 2, the membrane unit includes a raw water inlet pipe 1, a concentrated water outlet pipe 2, a central pipe 3 and a special reverse osmosis membrane layer 4 wound around the central pipe. The upper end of the central pipe is provided with an upper end cover and a lip A sealing ring 5, a lower end cover and a lip-shaped sealing ring 6 are provided at the lower end of the central tube, a plurality of small holes 7 are provided on the central tube, and a pure water outlet 8 is provided at the lower end of the central tube. The membrane module also includes a diversion distribution plate 9, and the diversion distribution plate is arranged on the feed end surface of the reverse osmosis membrane group. The grid of the reverse osmosis membrane group is a trapezoidal structure.

在本实用新型中,反渗透膜组的格网采用梯形结构,废水/料液在格网形成的通道内流动,如同在管式膜内流动,阻力小,同时内部横向的加强筋可以增加料液流动时候的紊流,降低膜的浓差极化作用,从而使得STRO膜组件的耐污染能力得到提高。In the utility model, the grid of the reverse osmosis membrane group adopts a trapezoidal structure, and the waste water/feed liquid flows in the channel formed by the grid, just like flowing in a tubular membrane, with small resistance, and at the same time, the internal transverse ribs can increase the flow rate of the material. The turbulent flow when the liquid flows reduces the concentration polarization of the membrane, thereby improving the pollution resistance of the STRO membrane module.

膜组单元的工作原理:废水从端头直接进水,经过一个导流分配盘将废水均匀的分配到膜组件进料端面,在压力作用下,透析液通过格网流入中间透析液收集管,其余截留废水通过平行格网流出浓水管。STRO膜组件以串联方式实现水回收率的提高和能耗的降低。The working principle of the membrane unit: the waste water is directly fed from the end, and the waste water is evenly distributed to the feed end surface of the membrane module through a diversion distribution plate. Under the pressure, the dialysate flows into the middle dialysate collection pipe through the grid. The rest of the retained wastewater flows out of the concentrated water pipe through the parallel grid. STRO membrane modules are connected in series to increase water recovery and reduce energy consumption.

膜组单元的工作原理:污水在原水罐单元加酸调节pH至6.5以后,经过过滤单元后去除原水中大于10微米的颗粒物,原水继续进入到高压泵单元,通过高压泵单元的增压使系统内水压升高,在高压力作用下污水通过膜组单元(STRO反渗透膜)后使其中的水分子透过膜层分离出来形成反渗透产水,内部循环的污水流经膜组件后压力降低后再经过在线增压泵增压送至膜组件入口反复循环,随着产水的排出、膜层内侧污水浓度升高、最终循环浓缩后通过压力控制阀排出。The working principle of the membrane unit: After the sewage is added to the raw water tank unit to adjust the pH to 6.5, the particulate matter larger than 10 microns in the raw water is removed after passing through the filter unit, and the raw water continues to enter the high-pressure pump unit, and the system is boosted by the high-pressure pump unit. The internal water pressure rises, and under the action of high pressure, the sewage passes through the membrane unit (STRO reverse osmosis membrane), and the water molecules in it are separated through the membrane layer to form reverse osmosis water. After the internal circulating sewage flows through the membrane module, the pressure After the reduction, it is boosted by the online booster pump and sent to the inlet of the membrane module for repeated circulation. With the discharge of the produced water, the concentration of the sewage inside the membrane layer increases, and the final cycle is concentrated and then discharged through the pressure control valve.

本实用新型采用的是STRO膜组件,与其他膜组件相比,有以下优势:1、可直接处理中低COD浓度的渗滤液,2、抗污染性能好,膜寿命长,3、水回收率高,The utility model adopts the STRO membrane module. Compared with other membrane modules, it has the following advantages: 1. It can directly treat the leachate with medium and low COD concentration; 2. It has good anti-pollution performance and long membrane life; 3. Water recovery rate high,

而其他膜系统,比如常规卷式膜系统对预处理要求高,容易堵塞,水回收率胝,需要多级组合。而碟管式膜系统的组件结构复杂,系统投资大,只适合于小规模应用。However, other membrane systems, such as conventional roll-type membrane systems, have high requirements for pretreatment, are easy to clog, and have low water recovery rates, requiring multi-stage combinations. However, the component structure of the disc-tube membrane system is complex, and the system investment is large, so it is only suitable for small-scale applications.

STRO膜组件具下述的特点STRO membrane modules have the following characteristics

当其他类型RO系统的性能(经常)受到膜污染和结垢问题限制时,ST膜系统依靠自身优化的流体动力学系统,很好地消减了这些问题所带来的麻烦。While the performance of other types of RO systems is (often) limited by membrane fouling and fouling issues, the ST membrane system relies on its own optimized hydrodynamic system to reduce the troubles caused by these problems.

简化了预处理:拥有了开放式的通道(结构),ST反渗透组件可对SDI指数高达20的海水或渗滤液直接处理,而不产生问题。其他RO系统一般对SDI指数的要求是≦3。(因此)简单的砂滤和保安过滤器就可以达到ST膜系统的SDI指数要求,而要达到其他系统的要求,只能通过更为复杂的过滤和化学处理。Simplified pretreatment: With an open channel (structure), ST reverse osmosis modules can directly treat seawater or leachate with an SDI index up to 20 without problems. Other RO systems generally require the SDI index to be ≦3. (Therefore) simple sand filter and security filter can meet the SDI index requirements of ST membrane system, but to meet the requirements of other systems, only through more complex filtration and chemical treatment.

回收率高能耗低:海水的回收率高达30-60%,产水能耗仅为6-10kWh/m3。High recovery rate and low energy consumption: the recovery rate of seawater is as high as 30-60%, and the energy consumption of water production is only 6-10kWh/m3.

渗滤液处理的回收率高达80-90%(TDS=5.000ppm),产水能耗为4-10kWh/m3。以上数据均指的是在标准体系情况下,因此假如考虑到浓水能量回收,则海水脱盐的能耗将可再减50%。The recovery rate of leachate treatment is as high as 80-90% (TDS=5.000ppm), and the energy consumption of water production is 4-10kWh/m3. The above data refer to the standard system, so if the concentrated water energy recovery is considered, the energy consumption of seawater desalination can be reduced by another 50%.

极少的化学操作费用:不像其它RO系统,ST膜组件无须长期的进水预处理,渗滤液处理时适当加酸即可。Very little chemical operation cost: Unlike other RO systems, ST membrane modules do not require long-term influent pretreatment, and only need to add acid when leachate is treated.

膜使用寿命长:低膜污染结垢率、高稳定性,以及拥有简单有效的内置清洗系统,使得ROCHEM系统膜的预期寿命一般不受进水水质的影响。数据表明,膜的实际使用寿命在5年以上。Long membrane service life: low membrane fouling scaling rate, high stability, and a simple and effective built-in cleaning system make the life expectancy of ROCHEM system membrane generally not affected by the quality of influent water. The data show that the actual service life of the membrane is more than 5 years.

膜更换简便:相比与DTRO或PTRO,组件更换和维护更加容易。Easy Membrane Replacement: Compared with DTRO or PTRO, component replacement and maintenance are easier.

出水质量高:ROCHEM的RO系统使用技术最新、化学性能最稳定的工业分离膜,而非一般的水处理膜。此外,(由于)使用的是平板膜,(因此)所安装膜的质量也能精确地选择和控制,以确保盐分通过率最低,产水质量高且出水连续。High effluent quality: ROCHEM's RO system uses industrial separation membranes with the latest technology and the most stable chemical properties, rather than general water treatment membranes. In addition (due to) the use of flat sheet membranes, (therefore) the quality of the installed membranes can also be precisely selected and controlled to ensure minimum salt passage, high quality and continuous water production.

最后说明的是,以上优选实施例仅用以说明本实用新型的技术方案而非限制,尽管通过上述优选实施例已经对本实用新型进行了详细的描述,但本领域技术人员应当理解,可以在形式上和细节上对其作出各种各样的改变,而不偏离本实用新型权利要求书所限定的范围。Finally, it is noted that the above preferred embodiments are only used to illustrate the technical solutions of the present utility model without limitation. Although the utility model has been described in detail through the above preferred embodiments, those skilled in the art should understand that it can be described in the form Various changes can be made in the above and in the details without departing from the scope defined by the claims of the present invention.

Claims (7)

1. a kind of landfill leachate advanced treatment system, it is characterised in that:The percolate advanced treatment system includes raw water tank Unit, high-pressure pumping unit, is pressurized pump unit, film group unit, instrument pack, production water pot unit and cleaning list at filter element online Member;The water inlet of the raw water tank unit and the water outlet of percolation liquid treating system connect, the water outlet and mistake of raw water tank unit The water inlet connection of unit is filtered, the water outlet of filter element and the water inlet of high-pressure pumping unit connect, the water outlet of high-pressure pumping unit Mouth is connect with the water inlet of online supercharging pump unit, and the online water outlet for being pressurized pump unit is connect with the water inlet of film group unit, The water outlet of film group unit is connect with production water pot unit, instrument pack respectively, and instrument pack is also connect with cleaning unit, and cleaning is single Member is connect with filter element.
2. a kind of landfill leachate advanced treatment system according to claim 1, it is characterised in that:It further include acid adding list Member, the acid adding unit are connect with raw water tank unit.
3. a kind of landfill leachate advanced treatment system according to claim 2, it is characterised in that:It further include antisludging agent list Member, the antisludging agent unit are connected on the pipeline between raw water tank unit and filter element.
4. a kind of landfill leachate advanced treatment system according to claim 3, it is characterised in that:Further include adding alkali list Member, described plus alkali unit are connect with production water pot unit.
5. a kind of landfill leachate advanced treatment system according to claim 4, it is characterised in that:The film group unit by Branched membrane component is rearranged by certain way, wherein every membrane component includes raw water water inlet pipe, condensed water outlet pipe, central tube With the reverse osmosis film layer on winding central tube, the upper end of central tube is provided with upper end cover and lip-type seal ring, the lower end of central tube It is provided with bottom end cover and lip-type seal ring, several apertures are provided on the central tube, the lower end of central tube is provided with pure water and goes out The mouth of a river.
6. a kind of landfill leachate advanced treatment system according to claim 5, it is characterised in that:The membrane component also wraps Flow guide distribution disk is included, the flow guide distribution disk is set to reverse osmosis membrane group charging end face.
7. a kind of landfill leachate advanced treatment system according to claim 6, it is characterised in that:The reverse osmosis membrane group Internal diversion grid be trapezium structure.
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