CN1785846B - Leachate treatment method using ventilated landfill - Google Patents
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- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
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Abstract
利用通风填埋层进行渗滤液处理的方法,涉及一种城市生活垃圾填埋的渗滤液处理方法,是通过渗滤液在填埋场内专用通风填埋单元的循环回灌实现对其的处理,专用单元间歇性地进行强制通风,使该单元填埋层形成时序性交替的好氧、缺氧和厌氧环境条件,促使层内形成好氧、兼性和厌氧的混合微生物菌群,利用其对渗滤液中的耗氧性有机物进行好氧、兼性和厌氧代谢去除;同时,好氧的硝化菌群和兼性的反硝化菌群通过硝化/反硝化途径去除渗滤液中的氨氮。本发明的优点是:在同一填埋层内利用循环回灌同时净化渗滤液中的耗氧性有机物和氨氮,处理出水COD小于1g/L、氨氮小于0.005g/L,有效地降低了渗滤液污染控制的成本。本发明分别适用于在新建和已建在用的填埋场中实施。
The method for treating leachate by using a ventilated landfill layer relates to a leachate treatment method for municipal solid waste landfill, which is achieved by circulating and recharging the leachate in a special ventilated landfill unit in the landfill, The special unit is intermittently forced to ventilate, so that the landfill layer of the unit forms a sequentially alternating aerobic, anoxic, and anaerobic environmental conditions, which promotes the formation of aerobic, facultative, and anaerobic mixed microbial flora in the layer. It performs aerobic, facultative and anaerobic metabolic removal of oxygen-consuming organic matter in leachate; at the same time, aerobic nitrifying bacteria and facultative denitrifying bacteria remove ammonia nitrogen in leachate through nitrification/denitrification . The advantages of the present invention are: in the same landfill layer, the aerobic organic matter and ammonia nitrogen in the leachate are simultaneously purified by recycling and recharging, and the COD of the treated water is less than 1g/L, and the ammonia nitrogen is less than 0.005g/L, effectively reducing the amount of leachate The cost of pollution control. The present invention is suitable for implementation in newly built and existing landfills.
Description
技术领域technical field
本发明涉及一种城市生活垃圾填埋的渗滤液处理方法。 The invention relates to a leachate treatment method for landfill of municipal domestic garbage. the
背景技术Background technique
填埋是应用最为广泛的生活垃圾处置技术,而渗滤液是其处理过程中产生的最主要的二次污染物。这些生活垃圾填埋渗滤液主要是耗氧性有机物和氨氮。传统的处理方法是:生活垃圾填埋渗滤液收集后,在填埋堆体外进行处理(‘Landfill leachate treatment.’Keenan J.D.,R.L.Steiner,and A.A.Fungaroli.Journal of the Water Pollution Control Federation56,27-33,1984),但处理的成本很高。生物反应器填埋(Bioreactor landfill)技术,发展了上述方法,它是利用填埋堆体作为生物反应器,通过渗滤液在填埋堆体内的循环使渗滤液得到净化(′Landfill bioreactor:historical perspective,fundamental principles,and newhorizons in design and operations’.Pohland,F.G.,1995.In Landfill Bioreactor Designand Operation Sem.Proc.,EPA/600/R-95/146,9-24),但由于通常填埋堆体内的代谢环境是厌氧的,因此这种方式只能净化耗氧性有机物,而不能净化氨氮。Price等人(′Nitrogen management in bioreactor landfills‘Price,G.A.,M.A.Barlaz,and G.R.Hater,2003.Waste Management23,675-688.)将渗滤液先在填埋堆体外生物硝化,然后将含硝酸盐氮的渗滤液循环回灌至填埋堆体内,利用填埋堆体内的缺氧条件使硝酸盐氮反硝化为氮气的渗滤液脱氮,但这一方法仍然需要借助填埋堆体外的传统生物硝化装置完成对渗滤液中氨氮的脱氮处理,使渗滤液的循环回灌处理技术复杂化。 Landfill is the most widely used domestic waste disposal technology, and leachate is the main secondary pollutant produced during its treatment. These domestic waste landfill leachates are mainly oxygen-consuming organic matter and ammonia nitrogen. The traditional treatment method is: after the domestic waste landfill leachate is collected, it is treated outside the landfill pile ('Landfill leachate treatment.' Keenan J.D., R.L. Steiner, and A.A. Fungaroli. Journal of the Water Pollution Control Federation56, 27-33 , 1984), but the processing cost is high. Bioreactor landfill (Bioreactor landfill) technology has developed the above method. It uses the landfill as a bioreactor and purifies the leachate through the circulation of the leachate in the landfill ('Landfill bioreactor: historical perspective , fundamental principles, and new horizons in design and operations'. Pohland, F.G., 1995. In Landfill Bioreactor Design and Operation Sem.Proc., EPA/600/R-95/146, 9-24), but due to the usual landfill The metabolic environment is anaerobic, so this method can only purify oxygen-consuming organic matter, but not ammonia nitrogen. Price et al. (‘Nitrogen management in bioreactor landfills’ Price, G.A., M.A.Barlaz, and G.R.Hater, 2003. Waste Management23, 675-688.) biologically nitrify the leachate outside the landfill first, and then nitrate nitrogen The leachate is recirculated and refilled into the landfill pile, and the leachate denitrification of nitrate nitrogen into nitrogen gas is denitrified by using the anoxic condition in the landfill pile. However, this method still needs the traditional biological nitrification outside the landfill pile. The device completes the denitrification treatment of ammonia nitrogen in the leachate, which complicates the leachate circulation and recharge treatment technology. the
发明内容Contents of the invention
本发明的目的是提供一种工艺简单的渗滤液处理方法,本发明的方法可同时处理渗滤液中的二种主要污染物:耗氧性有机物和氨氮。 The object of the present invention is to provide a leachate treatment method with a simple process. The method of the present invention can simultaneously treat two main pollutants in the leachate: oxygen-consuming organic matter and ammonia nitrogen. the
为了达到上述目的,本发明利用生物脱氮原理去除渗滤液中的氨氮,而该原理包含由亚硝化和硝化细菌在好氧条件下对氨氮的氧化,以及氨氮氧化产生的硝态和亚硝态氮在缺氧条件下,由反硝化细菌还原为氮气这二个基本步骤。而这二 个步骤必须在不同的氧环境(好氧和缺氧或厌氧)条件下完成,因此,本发明解决的基本技术问题是在填埋堆体内形成交替的好氧与缺氧(或厌氧)环境满足生物脱氮需要。形成好氧与缺氧交替环境的技术关键则是填埋堆体内的通风方式及通风控制条件。由于填埋堆体通风具有一定的技术复杂性(增加设施与投资),从技术经济性考虑,需要将通风控制在填埋场内的一定范围内,由此,本发明的技术方案如下: In order to achieve the above object, the present invention uses the principle of biological denitrification to remove ammonia nitrogen in the leachate, and the principle includes the oxidation of ammonia nitrogen by nitrifying and nitrifying bacteria under aerobic conditions, and the nitrate and nitrous state produced by the oxidation of ammonia nitrogen Nitrogen is reduced to nitrogen by denitrifying bacteria in two basic steps under anoxic conditions. And these two steps must be completed under different oxygen environment (aerobic and anoxic or anaerobic) conditions, therefore, the basic technical problem that the present invention solves is to form alternate aerobic and anoxic (or anaerobic) in the landfill pile body Anaerobic) environment meets the needs of biological denitrification. The technical key to forming an aerobic and anoxic alternate environment is the ventilation method and ventilation control conditions in the landfill. Because the ventilation of the landfill pile has certain technical complexity (increasing facilities and investment), considering the technical economy, it is necessary to control the ventilation within a certain range in the landfill, thus, the technical scheme of the present invention is as follows:
第一步,在填埋场内设置专用的填埋单元:该填埋单元设有与填埋场其它部分相同的防渗层,以及与填埋场其它部分的水力相互独立的渗滤液收集层和渗滤液调蓄池。 The first step is to set up a dedicated landfill unit in the landfill: the landfill unit is equipped with the same anti-seepage layer as the rest of the landfill, and a leachate collection layer that is hydraulically independent from the rest of the landfill and leachate storage tanks. the
第二步,在该专用填埋单元设置强制通风设施:强制通风设施由铺设于单元渗滤液收集层上的通风管网,和为通风管网供气的鼓风机组成。 The second step is to set up forced ventilation facilities in the dedicated landfill unit: the forced ventilation facilities are composed of a ventilation pipe network laid on the leachate collection layer of the unit, and a blower for supplying air to the ventilation pipe network. the
第三步,在专用单元内填埋生活垃圾:单元内垃圾填埋深度应小于6m,一般3~6m。为避免生活垃圾中生物降解过程中释放的有机物和氨氮对渗滤液处理过程的影响,本单元内填埋的垃圾应优先选择已在填埋场的其他部分或其他填埋场中填埋3年以上,经生物降解基本稳定的垃圾。 The third step is to bury domestic garbage in the special unit: the depth of garbage landfill in the unit should be less than 6m, generally 3-6m. In order to avoid the impact of organic matter and ammonia nitrogen released during the biodegradation process of domestic waste on the leachate treatment process, the landfilled waste in this unit should preferably be buried in other parts of the landfill or other landfills for 3 years Above, basically stable garbage after biodegradation. the
如果实际应用中,无法获得符合上述要求的垃圾,或因采集运输成本过高,不宜使用此类垃圾,也可直接填入新鲜生活垃圾,但需对填入的垃圾作加速降解稳定化处理,具体的操作方法是:1)将本单元排出的渗滤液收集至单元的独立调蓄池;2)将该独立调蓄池内的渗滤液,按单元的横截面计,水量负荷30L/m2·d,每天分2次循环,每次一半水量,由渗滤液回灌泵输送至单元布水管网(参见下述第四步),在单元内循环;3)与渗滤液循环同时,每天对其进行2次强制通风,每次通风量按单元的横截面计为4~6m3/m2,每次通风时间不大于1小时;4)加速降解稳定化操作至该独立调蓄池内渗滤液水质同时达到COD小于3000mg/L和氨氮小于300mg/L时中止。 If in practical application, it is impossible to obtain garbage that meets the above requirements, or it is not suitable to use such garbage due to the high cost of collection and transportation, it can also be directly filled with fresh domestic garbage, but the filled garbage needs to be treated with accelerated degradation and stabilization. The specific operation method is: 1) Collect the leachate discharged from the unit to the independent storage tank of the unit; 2) The leachate in the independent storage tank, calculated according to the cross section of the unit, has a water load of 30L/m 2 · d, 2 cycles per day, half of the water volume each time, is transported to the water distribution pipe network of the unit by the leachate recharge pump (see the fourth step below), and circulates in the unit; Carry out 2 times of forced ventilation, the volume of each ventilation is 4~6m 3 /m 2 according to the cross-section of the unit, and the time of each ventilation is not more than 1 hour; 4) Accelerate the degradation and stabilization operation until the leachate water quality in the independent storage tank At the same time, stop when COD is less than 3000mg/L and ammonia nitrogen is less than 300mg/L.
第四步,在填埋垃圾层上设置渗滤液循环回灌布水层:在已填埋,并作平整后的填埋垃圾面上,铺设由干管和支管组成的渗滤液循环回灌布水管网,布水管网的干管与渗滤液回灌泵连接,以提供向管网供水的条件,管网间的空隙应以级配碎石填满、并整平。 The fourth step is to set up the leachate circulation backfill water distribution layer on the landfill garbage layer: on the landfill garbage surface that has been landfilled and leveled, lay the leachate circulation backfill cloth composed of main pipes and branch pipes The water pipe network and the main pipe of the water distribution pipe network are connected to the leachate recharge pump to provide the conditions for water supply to the pipe network. The gaps between the pipe networks should be filled with graded gravel and leveled. the
第五步,对该单元进行气密性覆盖:气密性覆盖采用合成土工膜,将覆盖的 合成土工膜与本单元的防渗层的合成土工膜焊接连接,实现气密性覆盖,但覆盖合成土工膜上留有集气管接口,以有组织地导出单元内生物降解产生的气体(生成气)。覆盖合成土工膜上加覆土予以保护。 The fifth step is to cover the unit with airtightness: synthetic geomembrane is used for airtight coverage, and the covered synthetic geomembrane is welded to the synthetic geomembrane of the anti-seepage layer of this unit to achieve airtight coverage, but the covering The synthetic geomembrane is left with a gas collection pipe interface to organize the discharge of the gas (generated gas) generated by biodegradation in the unit. Cover the synthetic geomembrane with cover soil for protection. the
第六步,单元内生成气的控制:单元覆盖后的各集气管接口与集气总管连通,总管上部敞开,生成气通过集气管接口集中到集气总管,在总管上部敞开处排气。排气处标高应高于周围地面10m以上。总管内设置甲烷气体检测器和燃气燃烧器。检测器对进入总管的气体的甲烷体积比进行持续监测,如气体中甲烷体积分数大于15%,即输出信号至控制器,控制器自动点燃燃烧器以燃烬气体中的甲烷,使排出气体不会引至爆炸。如气体中的甲烷体积分数小于15%,则无需启动燃烧器,由气体排放后的大气自然稀释可控制其爆炸危险。 The sixth step is the control of the generated gas in the unit: after the unit is covered, each gas collecting pipe interface is connected with the gas collecting main pipe. The elevation of the exhaust should be higher than the surrounding ground by more than 10m. A methane gas detector and a gas burner are arranged in the main pipe. The detector continuously monitors the methane volume ratio of the gas entering the main pipe. If the methane volume fraction in the gas is greater than 15%, it will output a signal to the controller, and the controller will automatically ignite the burner to burn the methane in the gas, so that the exhaust gas will not Will cause an explosion. If the volume fraction of methane in the gas is less than 15%, there is no need to start the burner, and the natural dilution of the atmosphere after the gas is discharged can control the risk of explosion. the
第七步,渗滤液处理操作:完成上述步骤的专用单元已具备处理渗滤液、净化其中的有机物和氨氮的能力,具体的处理操作为:1)布水,引自填埋场总调蓄池的渗滤液,每天2次,每次以按本单元横截面计10~20L/m2·d的水量负荷输送至本单元布水管网进行处理;2)通风,每天2次,每次以按本单元横截面计4~6m3/m2的气量对单元进行强制通风。此操作使垃圾层内同时存在好氧,兼性和厌氧的生物代谢活动,回灌渗滤液中的耗氧性有机物,氨氮和有机氮均可得到有效去除。 The seventh step, leachate treatment operation: the special unit that has completed the above steps has the ability to process leachate and purify organic matter and ammonia nitrogen in it. The specific treatment operations are: 1) Water distribution, which is drawn from the general storage tank of the landfill site The leachate, twice a day, is transported to the water distribution pipe network of the unit with a water volume load of 10-20L/m 2 ·d based on the cross section of the unit each time; 2) Ventilation, twice a day, each time at the The cross-section of the unit is 4~6m 3 /m 2 for forced ventilation of the unit. This operation makes aerobic, facultative and anaerobic biological metabolic activities exist in the garbage layer at the same time, and the aerobic organic matter, ammonia nitrogen and organic nitrogen in the recharge leachate can be effectively removed.
本发明的突出效果如下: The outstanding effects of the present invention are as follows:
1.本发明利用回灌方法同时净化渗滤液中的两类主要宏量污染物:耗氧性有机物(COD)和氨氮(处理出水COD小于1g/L、氨氮小于0.005g/L)。 1. The present invention utilizes the recharge method to simultaneously purify two types of main macro-pollutants in the leachate: oxygen-consuming organic matter (COD) and ammonia nitrogen (COD of treated effluent is less than 1g/L, ammonia nitrogen is less than 0.005g/L). the
2.通过对填埋层通风方式的优化,在填埋层内形成时序性的好氧、缺氧、厌氧环境条件交替变化,这一环境条件与回灌渗滤液在层内的流动延时特征结合,使本发明可在同一填埋层内对氨氮作硝化和反硝化,实现完整的脱氮过程。 2. By optimizing the ventilation mode of the landfill layer, a sequential change of aerobic, anoxic, and anaerobic environmental conditions is formed in the landfill layer. This environmental condition is related to the flow delay of the recharge leachate in the layer. The combination of features enables the present invention to perform nitrification and denitrification of ammonia nitrogen in the same landfill layer to realize a complete denitrification process. the
3.对处理渗滤液的填埋层的通风量作了有效控制,能与现有填埋工艺条件下的填埋层透气条件兼容,无需对现有填埋工艺进行专门的改造,使实施成本得到控制。 3. The ventilation volume of the landfill layer for treating leachate is effectively controlled, which is compatible with the ventilation conditions of the landfill layer under the existing landfill process conditions, and no special modification of the existing landfill process is required, reducing the implementation cost. get under control. the
4.利用专用填埋单元处理整个填埋场产生的渗滤液,避免了对整个填埋场作通风设施建设,既降低了实施成本,也提高了技术实施的可行性。 4. The leachate produced by the entire landfill is treated with a special landfill unit, which avoids the construction of ventilation facilities for the entire landfill, which not only reduces the implementation cost, but also improves the feasibility of technical implementation. the
附图说明Description of drawings
图1为本发明的工艺原理图 Fig. 1 is process schematic diagram of the present invention
图2为本发明的通风填埋层的剖面结构示意图 Fig. 2 is the sectional structure schematic diagram of ventilated landfill layer of the present invention
附图中的标号说明如下: The labels in the accompanying drawings are explained as follows:
1—填埋场基土层;2—地下水导排层;3—U形水封;4—防渗膜下粘土层;5—HDPE防渗膜;6—防渗膜保护层;7—渗滤液导排层;8—通风布气层;9—垃圾层;10—回灌布水层;11—覆盖封闭层;12—渗滤液回灌泵;13—生成气收集管;14—通风主管;15—鼓风机。 1—base soil layer of landfill; 2—groundwater drainage layer; 3—U-shaped water seal; 4—clay layer under anti-seepage membrane; 5—HDPE anti-seepage membrane; 6—protective layer of anti-seepage membrane; 7—seepage Filtrate drainage layer; 8—ventilation air distribution layer; 9—garbage layer; 10—recharge water distribution layer; 11—covering and sealing layer; 12—leachate recharge pump; 13—generated gas collection pipe; 14—ventilation supervisor ; 15—blower. the
具体实施方式Detailed ways
本发明分别在新建和已建在用的填埋场中实施。 The invention is implemented in newly built and existing landfills respectively. the
实施例1 Example 1
在新建填埋场中的实施方法如下: The implementation method in the new landfill is as follows:
第一步,选择填埋区内的首个填埋单元为通风的专用渗滤液处理单元,该单元的有效填埋深度应大于3m,但不宜大于6m;单元的平面面积(S)以该填埋场预期的渗滤液量最大产生年份的日均值(Vmax)确定,二者关系为Vmax/S=0.02~0.04。 The first step is to select the first landfill unit in the landfill area as a special ventilated leachate treatment unit. The effective landfill depth of this unit should be greater than 3m, but not greater than 6m; The daily average value (V max ) of the year in which the maximum amount of leachate is expected to be produced in the burial site is determined, and the relationship between the two is V max /S=0.02~0.04.
专用渗滤液处理单元平面面积小于4000m2时,单元内无需分区,若总面积大于4000m2时,则需对单元进行分区,但每个分区的面积不宜小于2000m2。分区的含义是:不同分区之间以防水衬垫材料覆盖的土坝分隔,每个区的渗滤液独立收集和回灌,通风和集气管系同样应相互独立。 When the planar area of the dedicated leachate treatment unit is less than 4000m 2 , there is no need for division within the unit. If the total area is greater than 4000m 2 , the unit needs to be divided into divisions, but the area of each division should not be less than 2000m 2 . The meaning of zoning is: different zones are separated by earth dams covered with waterproof cushioning materials, leachate in each zone is collected and recharged independently, and ventilation and gas collection piping systems should also be independent of each other.
专用渗滤液处理单元建设准备程序:首先,对新建填埋场的库区按卫生填埋场建设的常规进行清库、底部平整和侧坡修整。然后,建造填埋场渗滤液调蓄池,调蓄池应分隔为水力独立的两部分,分别作为填埋场的总调蓄区和渗滤液处理单元调蓄区。渗滤液处理单元调蓄区的容量不小于上述Vmax的3倍,总调蓄区的容量按常规卫生填埋场设计方法确定,即可进行专用渗滤液处理单元的建设。 Preparatory procedures for the construction of special leachate treatment units: firstly, the reservoir area of the newly built landfill should be cleaned, bottom leveled and side slope repaired according to the routine construction of sanitary landfills. Then, build the landfill leachate storage tank, which should be divided into two hydraulically independent parts, which are respectively used as the general storage area of the landfill and the storage area of the leachate treatment unit. The capacity of the storage area of the leachate treatment unit is not less than 3 times of the above V max , and the capacity of the total storage area is determined according to the design method of the conventional sanitary landfill, and the construction of the special leachate treatment unit can be carried out.
第二步,专用渗滤液处理单元的建设:参见附图2通风填埋层剖面结构。首先,在拟建的单元底部按卫生填埋场建设要求设置地下水导排层2,在导排层2中设置地下水导排管,并接入填埋场的地表径流排出系统。然后在地下水导排层2上设置防渗膜下粘土层4,保证其上铺设的合成膜(通常是高密度聚乙烯HDPE材质)具有合理的水力坡度,同时,应达到其他HDPE膜施工规范要求。其后, 即按规范铺设HDPE防渗膜5,再在膜上设防渗膜保护层6(粘土或土工布),保护层6上铺设渗滤液导排层7(通常为河卵石或碎石),层内埋设渗滤液导排管。以上的建设步骤及其参数要求,均可参照现行的卫生填埋场建设标准实施,而以下的建设步骤则由本专用填埋处理单元的功能要求决定。 The second step is the construction of a special leachate treatment unit: see the cross-sectional structure of the ventilated landfill layer in Figure 2. Firstly, a groundwater drainage layer 2 is set at the bottom of the proposed unit according to the construction requirements of the sanitary landfill, and a groundwater drainage pipe is set in the drainage layer 2, which is connected to the surface runoff drainage system of the landfill. Then set the clay layer 4 under the anti-seepage membrane on the groundwater drainage layer 2 to ensure that the synthetic membrane (usually made of high-density polyethylene HDPE) laid on it has a reasonable hydraulic gradient, and at the same time, it should meet the requirements of other HDPE membrane construction specifications . Thereafter, the HDPE anti-seepage membrane 5 is laid according to the specifications, and then the anti-seepage membrane protective layer 6 (clay or geotextile) is set on the membrane, and the leachate drainage layer 7 (usually river pebbles or gravels) is laid on the protective layer 6. ), and the leachate drainage pipe is buried in the layer. The above construction steps and their parameter requirements can be implemented with reference to the current sanitary landfill construction standards, while the following construction steps are determined by the functional requirements of this special landfill treatment unit. the
一.将渗滤液导排总管通过不小于500mm的U形水封3接入填埋场渗滤液调蓄池中的渗滤液处理单元调蓄区。 1. Connect the leachate drainage main pipe to the leachate treatment unit storage area in the landfill leachate storage tank through a U-shaped water seal 3 of not less than 500 mm. the
二.在渗滤液导排层7上铺设通风布气层8,通风布气层8由通气管网和对其起覆盖保护作用的填充碎石组成。通气管网包括干管和支管,每个单元分区设的通风主管14与离心式鼓风机15相联结,鼓风机在供风流量下输出风压不小于2500Pa。单元内干管与支管正交联结,管间间距5-10m,干管不开孔,仅起气流输送作用,支管开孔将通入气流释放至填埋层,优化的支管开孔方案是上半周以5~10%的开孔率、5~20mm孔径,开设均布孔,下半周则仅在底部间隔500mm开设孔径10-20mm的单排孔,覆盖通气管网的碎石直径为5-20mm的级配料,覆盖厚度保证直径最大的管道顶部之上至少有10cm的碎石层保护。 2. Lay a ventilation air distribution layer 8 on the leachate drainage layer 7. The ventilation air distribution layer 8 is composed of a ventilation pipe network and filled gravels that cover and protect it. The ventilation pipe network includes main pipes and branch pipes, and the ventilation main pipe 14 provided in each unit partition is connected with the centrifugal blower 15, and the output air pressure of the blower is not less than 2500Pa under the air supply flow rate. The main pipe and the branch pipe in the unit are connected orthogonally, and the distance between the pipes is 5-10m. In the half circle, holes are evenly distributed with an opening rate of 5-10% and a hole diameter of 5-20mm. In the second half circle, only a single row of holes with a diameter of 10-20mm is opened at the bottom at an interval of 500mm. The diameter of gravel covering the ventilation pipe network is 5-20mm. 20mm grading, covering thickness to ensure at least 10cm of gravel layer protection above the top of the pipe with the largest diameter. the
第三步,填入垃圾,为保护通风管系。在填入垃圾厚度小于2m时,只以推土机对垃圾作一次平整,不作碾压;填入垃圾厚度大于2m时,除以推土机作一次整平外,还可再以推土机对垃圾层9作2-3遍的碾压,以对不均匀沉降作一定的控制,但不应使用钢轮式压实机进行压实作业。垃圾作业的其他环节与常规卫生填埋相似,填埋直至本单元指定的垃圾层厚度时中止,以此形成垃圾层9。 The third step is to fill in garbage to protect the ventilation system. When the thickness of the filled garbage is less than 2m, the garbage is only leveled once with the bulldozer without rolling; -Three passes of rolling to control uneven settlement, but steel wheel compactors should not be used for compaction. The other links of the garbage operation are similar to the conventional sanitary landfill, and the landfill stops when the thickness of the garbage layer specified by this unit is reached, so as to form the garbage layer 9 . the
第四步,铺设回灌布水层10。在对垃圾层9表面进行平整后,首先铺设一层200mm厚的中粗粒径(1~4mm)的建筑砂,然后,在砂层上铺设回灌布水管网,管网由干管和支管组成,每个单元分区设干管与设于填埋场总调蓄区的渗滤液回灌泵12联结,向管网供水。干管与支管正交联结,管间距5-10m。干管不开孔,支管开孔进行回灌布水。开孔方案为:上半周不开孔,下半周以8%的开孔率,均布直径5-15mm的孔。布水管网管底直接设置于垃圾层上,管间空隙以粒径6-30mm碎石覆盖,覆盖厚度保证直径最大的管道顶部之上有至少10cm的碎石层保护。 The fourth step is to lay the back irrigation water distribution layer 10 . After leveling the surface of the garbage layer 9, first lay a layer of 200mm-thick construction sand with a medium-coarse particle size (1-4mm), and then lay a water distribution pipe network on the sand layer. The pipe network consists of main pipes and branch pipes. Composition, each unit partition is provided with a main pipe to connect with the leachate recharge pump 12 located in the general storage area of the landfill to supply water to the pipe network. The main pipe and the branch pipe are connected orthogonally, and the distance between the pipes is 5-10m. The main pipe is not perforated, and the branch pipe is perforated for refilling and water distribution. The hole opening scheme is: no holes are opened in the first half of the circle, and holes with a diameter of 5-15mm are evenly distributed in the second half of the circle with an opening rate of 8%. The bottom of the water distribution pipe network is directly placed on the garbage layer, and the gap between the pipes is covered with gravel with a particle size of 6-30mm. The covering thickness ensures that the top of the pipe with the largest diameter is protected by a layer of gravel at least 10cm above. the
第五步,单元覆盖、导气与气体处理。首先对已完成回灌布水层10铺设的单元分区进行覆盖封闭层11,由下至上为:最下层400g/m2土工布,其上为1mm 厚的低密度聚乙烯(LDPE)膜,再上为200g/m2的土工布,然后是0.3m厚的压实粘土,最上是0.1m厚的碎石导水层(10-30mm粒径级配)。对于本单元之上仍需进行垃圾填埋的情况,导水层之上即可作常规的填埋作业,对于本单元之上不再作填埋(即为最终覆盖)的情况,导水层之上应按卫生填埋最终覆盖层构筑要求再进行耕作(营养)土覆盖和植被垦复。与覆盖封闭层11相配合的导气系统主要由垂直布置的单元导气管和其后的气体处理装置组成,单元导气管以正方形网格状均匀分布(管间距20-30m)于单元覆盖封闭层11上,下端插入回灌布水层10的碎石覆盖层中约10cm,管道材质为HDPE,直径10-20cm,管道与LDPE膜交会处以焊接方式密封。导气管的长度与单元覆盖面上是否再进行填埋有关,继续填埋的,各垂直的的单元导气管应在前述的压实粘土层中与水平向的导气收集支管相联通,支管引出填埋层后与导气干管联结,最终接入气体处理装置;不继续填埋的,各垂直导气管向上延伸至最终覆盖面之上,然后再与水平的导气支管和干管相联通,同样将气体引至气体处理装置。 The fifth step is unit covering, gas conduction and gas treatment. Firstly, cover the unit partitions that have completed the laying of the recharge water distribution layer 10 and cover the sealing layer 11, from bottom to top: the lowest layer of 400g/m 2 geotextile, on which is a 1mm thick low-density polyethylene (LDPE) film, and then The top is 200g/m 2 geotextile, then 0.3m thick compacted clay, and the top is 0.1m thick gravel aquifer (10-30mm particle size gradation). For the situation where landfill still needs to be carried out above the unit, conventional landfill operations can be carried out above the aquifer. On top of that, farming (nutrient) soil covering and vegetation reclamation should be carried out according to the construction requirements of the final covering layer of the sanitary landfill. The gas guide system matched with the covering and sealing layer 11 is mainly composed of vertically arranged unit air guiding pipes and subsequent gas treatment devices. The unit air guiding pipes are evenly distributed in a square grid (tube spacing 20-30m) on the unit covering and sealing layer 11 The upper and lower ends are inserted into the crushed stone cover layer of the refilling water distribution layer 10 for about 10cm. The pipe is made of HDPE with a diameter of 10-20cm. The intersection of the pipe and the LDPE film is sealed by welding. The length of the air guide pipe is related to whether landfill is carried out on the unit coverage surface. If the landfill continues, each vertical unit air guide pipe should be connected with the horizontal air guide collection branch pipe in the aforementioned compacted clay layer, and the branch pipe leads to the filling After the layer is buried, it is connected with the main gas pipe, and finally connected to the gas treatment device; if the landfill is not continued, the vertical air pipes extend upward to the final covering surface, and then connect with the horizontal gas branch pipes and main pipes. The gas is directed to a gas processing unit.
第六步,气体处理:气体处理装置为直径0.5-1m的垂直排气筒,筒顶与所安装地面的高差≥10m;导气管中的气体由空压机通过气体燃烧喷嘴在筒底部引入筒内,燃烧喷嘴前设气体浓度监测点,在线监测气体中的甲烷浓度,当甲烷体积浓度小于15%时,直接排放气体;甲烷体积浓度大于15%时,自动开启筒底另设的一个辅助燃油烧嘴点燃气体,燃烧后再排出。专用渗滤液回灌处理单元建设、填埋、覆盖和气体导气与处理装置设置完毕后,应进行单元内新鲜垃圾的加速稳定化操作。 The sixth step, gas treatment: the gas treatment device is a vertical exhaust tube with a diameter of 0.5-1m, and the height difference between the top of the tube and the installed ground is ≥10m; the gas in the air duct is introduced at the bottom of the tube by the air compressor through the gas combustion nozzle In the barrel, a gas concentration monitoring point is set in front of the combustion nozzle to monitor the methane concentration in the gas online. When the methane volume concentration is less than 15%, the gas will be discharged directly; The fuel burner ignites the gas, burns it and then discharges it. After the construction of the special leachate recharge treatment unit, landfill, covering and installation of gas guide and treatment devices, the accelerated stabilization operation of fresh garbage in the unit should be carried out. the
单元内新鲜垃圾的加速稳定化操作:每天从渗滤液处理单元调蓄区向单元内回灌2次渗滤液,回灌水量负荷每次10-20L/m2;同时,每天2次对单元进行强制通风,每次的通风量为4~6m3/(m2单元水平截面积),但每次通风时间不超过1小时;期间,处理单元调蓄区,原则上不外排渗滤液,至单元排出渗滤液的COD小于3000mg/L,氨氮小于300mg/L时,即表示单元内垃圾已基本稳定化,单元可进入正常的渗滤液处理阶段,用于处理填埋场其他部分产生的渗滤液。 Accelerated stabilization operation of fresh waste in the unit: refill the leachate twice a day from the storage area of the leachate treatment unit to the unit, and the refill water load is 10-20L/m 2 each time; Forced ventilation, each ventilation volume is 4-6m 3 /(m 2 unit horizontal cross-sectional area), but each ventilation time does not exceed 1 hour; When the COD of the leachate discharged from the unit is less than 3000mg/L, and the ammonia nitrogen is less than 300mg/L, it means that the garbage in the unit has been basically stabilized, and the unit can enter the normal leachate treatment stage, which is used to treat the leachate produced by other parts of the landfill .
第七步,正常的渗滤液处理操作:每天2次从渗滤液总调蓄区向本单元,按每次10-20L/m2的水量负荷回灌渗滤液;同时每天2次,每次时间不超过1小时,向单元通入4~6m3/m2的空气。处理后单元内排出的渗滤液通过处理单元调 蓄区,直接排入城市污水管网,或进一步以物化方法深度处理后排入地表水体。 The seventh step, normal leachate treatment operation: 2 times a day from the leachate general storage area to this unit, according to the water load of 10-20L/m 2 each time, refill the leachate; at the same time 2 times a day, each time In no more than 1 hour, 4-6m 3 /m 2 of air is introduced into the unit. After treatment, the leachate discharged from the unit passes through the storage area of the treatment unit, and is directly discharged into the urban sewage pipe network, or is further treated by physical and chemical methods and then discharged into the surface water body.
实施例2 Example 2
在已建填埋场中的实施方法: Implementation methods in established landfills:
首先应对调蓄池进行分隔或改建,形成容量达到要求(具体与实施例1相同)的总调蓄区和处理单元调蓄区。然后,构筑专用通风处理单元,如单元设置于场内尚未填埋的区域,则其建设方式与前述的新建填埋场中实施例1一致,仅在填入垃圾时,应将场内已填埋3年以上的陈垃圾挖出后,重新填入此单元,这样可无需对本单元内的垃圾做加速稳定化处理,而可以直接用于处理场内产生的渗滤液;如单元必须设置于场内已填埋的垃圾层之上,则除了在垃圾层上应铺设1层厚0.1m的级配碎石(5-15mm),代替前述的地下水导排层2,且同时在单元内填入已填埋3年以上的垃圾外,其余均与在新填埋场中的实施方式,即实施例1相同。Firstly, the storage pool should be separated or rebuilt to form a general storage area and a processing unit storage area with a capacity that meets the requirements (specifically the same as in Embodiment 1). Then, build a special-purpose ventilation treatment unit. If the unit is arranged in an area that has not yet been landfilled in the site, its construction method is consistent with Embodiment 1 in the aforementioned new landfill. After excavating old garbage that has been buried for more than 3 years, it will be refilled into this unit, so that the garbage in this unit does not need to be accelerated and stabilized, but can be directly used to treat the leachate generated in the site; if the unit must be installed in the site In addition to laying a layer of graded gravel (5-15mm) with a thickness of 0.1m on the garbage layer, instead of the aforementioned groundwater drainage layer 2, and at the same time fill in the unit Except the rubbish that has been buried for more than 3 years, all the others are the same as the implementation mode in the new landfill, i.e. embodiment 1.
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CN101164926B (en) * | 2007-08-17 | 2010-05-26 | 浙江大学 | A domestic waste landfill treatment technology and bioreactor with in-situ denitrification function |
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