CN115448556A - Remediation system and remediation method for heavy metal polluted bottom mud - Google Patents

Remediation system and remediation method for heavy metal polluted bottom mud Download PDF

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CN115448556A
CN115448556A CN202211142217.7A CN202211142217A CN115448556A CN 115448556 A CN115448556 A CN 115448556A CN 202211142217 A CN202211142217 A CN 202211142217A CN 115448556 A CN115448556 A CN 115448556A
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cleaning
bottom mud
housing
fixed
mud
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CN115448556B (en
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姜登登
丁达
徐东
夏菲洋
周艳
邓绍坡
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Nanjing Institute of Environmental Sciences MEP
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Nanjing Institute of Environmental Sciences MEP
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00Treatment of sludge; Devices therefor
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00Treatment of sludge; Devices therefor
    • C02F11/02Biological treatment
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/10Inorganic compounds
    • C02F2101/20Heavy metals or heavy metal compounds

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  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
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  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
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Abstract

The invention discloses a restoration system and a restoration method for heavy metal polluted bottom mud, which comprises a pretreatment filtering and washing mechanism, a biological enrichment treatment mechanism, a fine filtering and washing mechanism and a bottom mud porosity preparation mechanism; the pretreatment filtering and washing mechanism comprises a washing tank, a bottom sediment conveying pipe is fixedly arranged in the washing tank, a dispersing output ring is fixedly arranged at the lower end of the bottom sediment conveying pipe, and a plurality of bottom sediment output holes are formed in the dispersing output ring; the method comprises the steps that firstly, a pretreatment filtering and washing mechanism and a fine filtering and washing mechanism are utilized to treat bottom mud, so that partial heavy metals and most organic impurities in the bottom mud can be removed, the biological enrichment treatment mechanism with a double-layer design can more accurately control the humidity and the temperature of the bottom mud soil and can carry out controllable ventilation treatment on the bottom mud soil, the heavy metals in the bottom mud are effectively transferred and solidified in plants under the enrichment effect of the plants, and finally, the plants rich in the heavy metals are subjected to pyrolysis.

Description

一种用于重金属污染底泥的修复系统及修复方法A repair system and repair method for heavy metal contaminated sediment

技术领域technical field

本发明涉及底泥修复技术领域,具体为一种用于重金属污染底泥的修复系统及修复方法。The invention relates to the technical field of bottom mud restoration, in particular to a restoration system and method for heavy metal contaminated bottom mud.

背景技术Background technique

上覆水、水体底部的沉积物以及周围各种环境条件组成了完整的水体,河道污染包含外源污染和内源污染两方面,在水处理领域深入发展的背景下,我国在流域治理、工业废水处理、生活污水处理等众多领域上的发展迅速,外源污染得到控制,而对于河道底泥无害化处理的重视远不及污水治理,污染物质进入水体后,通过沉淀、吸附、生物吸收等途径最终沉积于底泥中并逐渐积累,一旦环境条件发生改变污染物质就会通过解吸、扩散、扰动等方式重新释放污染上覆水水质,继而影响整个水体。Overlying water, sediments at the bottom of the water body and various surrounding environmental conditions constitute a complete water body. River pollution includes two aspects: external source pollution and internal source pollution. Treatment, domestic sewage treatment and many other fields have developed rapidly, and external pollution has been controlled. However, the emphasis on the harmless treatment of river sediment is far less than that of sewage treatment. After pollutants enter the water body, they pass through precipitation, adsorption, biological absorption, etc. Finally, it is deposited in the bottom mud and gradually accumulates. Once the environmental conditions change, the pollutants will be re-released to pollute the water quality of the overlying water through desorption, diffusion, disturbance, etc., and then affect the entire water body.

发明内容Contents of the invention

本发明的目的在于提供一种用于重金属污染底泥的修复系统及修复方法,能够较为彻底的清除底泥中的重金属污染。The purpose of the present invention is to provide a repair system and repair method for heavy metal-contaminated bottom mud, which can thoroughly remove heavy metal pollution in bottom mud.

为实现上述目的,本发明提供如下技术方案:To achieve the above object, the present invention provides the following technical solutions:

一种用于重金属污染底泥的修复系统,包括预处理滤洗机构、生物富集处理机构、精细化滤洗机构以及底泥孔隙化制备机构;A remediation system for heavy metal-contaminated sediment, including a pretreatment and filtration mechanism, a biological enrichment treatment mechanism, a refined filtration and washing mechanism, and a sediment porosity preparation mechanism;

预处理滤洗机构包括开口朝上的清洗罐,清洗罐内固定设有上下延伸的底泥输送管,底泥输送管上端具有底泥输入接口,清洗罐顶部安装有清洗罐顶盖;The pretreatment filtering and washing mechanism includes a cleaning tank with an opening facing upwards. A bottom sludge conveying pipe extending up and down is fixed inside the cleaning tank. The upper end of the bottom sludge conveying pipe has a bottom sludge input interface, and the top of the cleaning tank is equipped with a cleaning tank top cover;

清洗罐内侧壁靠近顶部位置固定有搅拌机构支撑架,搅拌机构支撑架上安装有搅拌机构,搅拌机构包括转动配合连接在搅拌机构支撑架上的搅拌轴,搅拌轴为上下延伸布置,搅拌轴下端固定设有多个搅拌叶片;A stirring mechanism support frame is fixed on the inner wall of the cleaning tank near the top, and a stirring mechanism is installed on the stirring mechanism support frame. The stirring mechanism includes a stirring shaft that is rotated and connected to the stirring mechanism support frame. fixedly equipped with multiple stirring blades;

精细化滤洗机构包括开口朝上的清洗容纳壳以及固定在清洗容纳壳内的清洗斜板,清洗斜板上侧面具有多个前后延伸的旋转清洗槽;The refined filtering and washing mechanism includes a cleaning container with an opening facing upwards and a cleaning swash plate fixed in the cleaning container. The side of the cleaning swash plate has a plurality of rotating cleaning tanks extending forward and backward;

清洗容纳壳外侧靠近清洗斜板较高的一端固定设有与清洗容纳壳内相连通的底泥输入壳,清洗容纳壳外侧靠近清洗斜板较低的一端固定设有与清洗容纳壳内相连通的清洗排出壳;The outer side of the cleaning containment shell close to the higher end of the cleaning slant plate is fixed with a sediment input shell connected to the inside of the cleaning containment shell, and the outer side of the cleaning containment shell close to the lower end of the cleaning slant plate is fixedly provided with a bottom mud input shell connected to the inside of the cleaning containment shell. cleaning discharge shell;

清洗容纳壳内固定设有多根前后延伸的清洗水管,多个清洗水管一对一设置在旋转清洗槽上方,清洗水管下侧具有多个清洗喷头;A plurality of cleaning water pipes extending forward and backward are fixed in the cleaning container, and the plurality of cleaning water pipes are arranged one by one above the rotating cleaning tank, and the lower side of the cleaning water pipes has a plurality of cleaning nozzles;

底泥孔隙化制备机构用于将底泥制备成多孔隙的泥土,多孔隙的泥土用于生物富集处理机构进行植物种植;The bottom mud porosity preparation mechanism is used to prepare the bottom mud into porous soil, and the porous soil is used for plant planting by the biological enrichment treatment mechanism;

生物富集处理机构包括开口朝上的种植容纳壳体,种植容纳壳体外侧包围设有培育养护壳体,培育养护壳体上端与种植容纳壳体上端密封连接;The bio-enrichment treatment mechanism includes a planting housing with an opening facing upwards, a cultivation and maintenance housing is surrounded on the outside of the planting housing, and the upper end of the cultivation and maintenance housing is sealed and connected to the upper end of the planting housing;

种植容纳壳体侧壁为镂空结构,种植容纳壳体内壁铺设有多层无纺布;The side wall of the planting housing is a hollow structure, and the inner wall of the planting housing is covered with multi-layer non-woven fabrics;

培育养护壳体外侧固定设有湿度调节接口,培育养护壳体外侧固定设有加压通风接口,培育养护壳体外侧固定设有平衡排气接口,平衡排气接口上具有泄压阀。The outer side of the cultivation and maintenance housing is fixed with a humidity adjustment interface, the outer side of the cultivation and maintenance housing is fixed with a pressurized ventilation interface, and the outer side of the cultivation and maintenance housing is fixed with a balanced exhaust interface, and the balanced exhaust interface is provided with a pressure relief valve.

优选地,清洗罐内侧壁固定设有环形的清水输送管,上述清水输送管上具有多个排水接口;Preferably, the inner wall of the cleaning tank is fixed with an annular clear water delivery pipe, and the above-mentioned clear water delivery pipe has multiple drainage interfaces;

底泥输送管下端固定设有分散输出环,分散输出环内部为中空结构且与底泥输送管内部相连通,分散输出环上具有多个与自身内部相连通的底泥输出孔。The lower end of the sediment conveying pipe is fixed with a dispersing output ring. The dispersing output ring has a hollow structure inside and communicates with the sediment conveying pipe. The dispersing output ring has a plurality of sediment output holes communicating with itself.

说明:分散输出环能够将底泥更加均匀的排放到清洗罐。Description: The dispersing output ring can discharge the sediment to the cleaning tank more evenly.

优选地,搅拌机构支撑架上固定设有第一电机容纳壳,第一电机容纳壳内固定设有第一电机,搅拌轴的上端延伸至第一电机容纳壳内部,第一电机用于驱动搅拌轴转动。Preferably, the support frame of the stirring mechanism is fixed with a first motor housing, and the first motor housing is fixed with a first motor. The upper end of the stirring shaft extends to the inside of the first motor housing, and the first motor is used to drive the stirring The shaft turns.

优选地,清洗罐外侧壁固定设有多个输送泵容纳壳,输送泵容纳壳内固定设有第一输送泵,第一输送泵的输入端与清洗罐内部相连通,第一输送泵的输出端通过管道与底泥输入壳相连通。Preferably, the outer wall of the cleaning tank is fixed with a plurality of delivery pump housings, and the first delivery pump is fixed inside the delivery pump housing. The input end of the first delivery pump communicates with the inside of the cleaning tank, and the output of the first delivery pump The end is connected with the sediment input shell through a pipeline.

说明:多个第一输送泵有利于将清洗罐中泥水混合物更加快速均匀的排出。Description: Multiple first delivery pumps are beneficial to discharge the muddy water mixture in the cleaning tank more quickly and evenly.

优选地,旋转清洗槽内设有前后延伸的倾转清洗管,倾转清洗管上具有清洗管开槽,倾转清洗管前后两端转动配合连接在清洗容纳壳侧壁上;Preferably, a tilting cleaning tube extending forward and backward is provided in the rotating cleaning tank, the tilting cleaning tube is provided with slots for the cleaning tube, and the front and rear ends of the tilting cleaning tube are rotatably connected to the side wall of the cleaning container;

清洗容纳壳外侧壁上固定设有多个第二电机容纳壳,多个上述第二电机容纳壳与多个倾转清洗管的位置相对应,第二电机容纳壳内固定设有第二电机,倾转清洗管其中一端的转轴延伸至第二电机容纳壳内,第二电机用于驱动倾转清洗管转动。A plurality of second motor housings are fixed on the outer wall of the cleaning housing. The positions of the multiple second motor housings correspond to the positions of the plurality of tilting cleaning pipes. The second motor housings are fixed with a second motor. The rotating shaft at one end of the tilting cleaning pipe extends into the housing of the second motor, and the second motor is used to drive the tilting cleaning pipe to rotate.

说明:底泥自上而下在清洗斜板上流通时,倾转清洗管能够截留一定的底泥使得底泥在倾转清洗管中暂存,此过程中有利于对底泥进行更加彻底的冲洗,然后利用电机驱动倾转清洗管旋转,将倾转清洗管中暂存的底泥倾倒。Explanation: When the sediment flows on the cleaning sloping plate from top to bottom, the tilting cleaning pipe can retain a certain amount of sediment so that the sediment can be temporarily stored in the tilting cleaning pipe. This process is conducive to more thorough cleaning of the sediment Rinse, and then use the motor to drive the tilting cleaning tube to rotate, and dump the sediment temporarily stored in the tilting cleaning tube.

优选地,清洗容纳壳内位于清洗斜板较低一端转动配合设有前后延伸的吸附滚筒,吸附滚筒由电机驱动转动,清洗容纳壳内位于吸附滚筒右侧固定设有排渣刮板,清洗容纳壳内位于排渣刮板右侧固定设有排渣输送带,排渣输送带另一端延伸至清洗容纳壳外部,清洗容纳壳外侧位于排渣输送带下方固定设有滤渣容纳壳。Preferably, the lower end of the cleaning slant plate is rotated in the cleaning container and is equipped with an adsorption roller extending forward and backward. The adsorption roller is driven by a motor to rotate, and a slag discharge scraper is fixed on the right side of the adsorption roller in the cleaning container. A slag discharge conveyor belt is fixed inside the shell on the right side of the slag discharge scraper, the other end of the slag discharge conveyor belt extends to the outside of the cleaning housing, and the outside of the cleaning housing is below the slag discharge conveyor belt.

说明:吸附滚筒具有磁性,能够吸附去除底泥中的磁性微粒杂质。Description: The adsorption roller is magnetic and can absorb and remove magnetic particle impurities in the sediment.

优选地,底泥孔隙化制备机构包括开口朝上的固化制备桶,固化制备桶内底部固定设有曝气输出壳,曝气输出壳顶部固定设有与自身内部相连通的上下延伸的曝气输送管,曝气输出壳顶部具有多个曝气小孔;Preferably, the sediment porosity preparation mechanism includes a solidification preparation barrel with an opening facing upwards, the bottom of the solidification preparation barrel is fixed with an aeration output shell, and the top of the aeration output shell is fixed with an aeration barrel extending up and down that communicates with itself. Conveying pipe, the top of the aeration output shell has a plurality of small aeration holes;

固化制备桶包括支撑板,支撑板顶部边缘处连接设有环形的侧向支撑围挡,侧向支撑围挡由多个侧面支撑板组合而成,侧面支撑板下端通过活动铰链与支撑板连接,侧向支撑围挡顶部密封安装有第二顶盖。The curing preparation barrel includes a support plate, and an annular lateral support enclosure is connected to the top edge of the support plate. The lateral support enclosure is composed of a plurality of side support plates, and the lower end of the side support plate is connected to the support plate through a movable hinge. The top of the lateral support enclosure is sealed with a second top cover.

说明:利用底泥孔隙化制备机构能够将底泥制备成孔隙结构丰富的土壤,便于进行后续的植物种植。Explanation: The bottom mud porosity preparation mechanism can be used to prepare the bottom mud into soil with rich pore structure, which is convenient for subsequent planting.

优选地,侧面支撑板内侧壁上具有上下延伸的第一破碎凸棱,曝气输送管外侧壁上具有上下延伸的第二破碎凸棱。Preferably, there are first crushing ribs extending up and down on the inner side wall of the side support plate, and second crushing ribs extending up and down on the outer wall of the aeration delivery pipe.

说明:第一破碎凸棱和第二破碎凸棱能够在固化的底泥块上形成凹槽,便于固化的底泥块从固化制备桶中破碎取出。Description: The first broken rib and the second broken rib can form grooves on the solidified bottom mud block, which is convenient for the solidified bottom mud block to be broken and taken out from the solidification preparation barrel.

优选地,如上述的一种用于重金属污染底泥的修复系统进行重金属污染底泥的修复方法,包括以下步骤:Preferably, as above-mentioned a kind of repairing system for heavy metal contaminated bottom mud carries out the repair method of heavy metal contaminated bottom mud, comprises the following steps:

S1、将重金属污染底泥从河道中采挖出后进行晒干,将晒干的底泥破碎,再将破碎后的底泥过100~200目的筛滤;S1. Excavating the heavy metal-contaminated bottom mud from the river, drying it in the sun, crushing the dried bottom mud, and then passing the broken bottom mud through a 100-200 mesh sieve;

S2、将步骤S1中筛滤后的底泥输送到预处理滤洗机构的清洗罐中,并向清洗罐中注入清水,利用电机驱动搅拌轴并使得搅拌叶片对清洗罐中的泥水混合物不断地搅拌滤洗30~90min,然后利用第一输送泵将清洗罐中的泥水混合物输送到沉淀池中沉淀2~3h;S2, transport the bottom mud after screening in step S1 to the cleaning tank of the pretreatment filter washing mechanism, and inject clear water into the cleaning tank, use the motor to drive the stirring shaft and make the stirring blades constantly shake the mud-water mixture in the cleaning tank Stir and filter for 30-90 minutes, and then use the first delivery pump to transport the mud-water mixture in the cleaning tank to the sedimentation tank for 2-3 hours;

S3、将步骤S2沉淀池中的沉淀底泥输送到精细化滤洗机构的底泥输入壳中,底泥沿清洗斜板流下的过程中,利用清洗喷头喷射出的高速水流对底泥进行冲洗;S3. Transport the sedimented sediment in the sedimentation tank in step S2 to the sediment input shell of the fine filtration and washing mechanism. During the process of the sediment flowing down the cleaning inclined plate, the sediment is washed by the high-speed water jetted from the cleaning nozzle ;

S4、步骤S3经过冲洗后的底泥从清洗排出壳中排出,然后利用烘干设备对底泥进行除水处理,将底泥的含水率控制在70%~85%;S4. The bottom sludge washed in step S3 is discharged from the cleaning and discharging shell, and then the bottom sludge is dewatered by drying equipment, and the moisture content of the bottom sludge is controlled at 70% to 85%;

S5、将步骤S4处理后的底泥输送到底泥孔隙化制备机构的固化制备桶中,利用曝气输出壳向底泥中曝入大量的微型气泡并对整个固化制备桶进行加热升温,温度控制在150℃~300℃,对固化制备桶中的底泥进行干燥固化,得到多孔隙底泥;S5. Transport the bottom sludge treated in step S4 to the solidification preparation tank of the bottom sludge porosity preparation mechanism, use the aeration output shell to expose a large number of micro air bubbles into the bottom sludge, and heat up the entire solidification preparation tank to control the temperature. Dry and solidify the bottom sludge in the solidification preparation tank at 150°C to 300°C to obtain porous bottom sludge;

S6、将步骤S5制备的多孔隙底泥破碎成0.1~1mm的颗粒,并加入相对于多孔隙底泥体积10%~20%比例的沙粒混合均匀,沙粒的粒径为0.5~2mm,将混合有沙粒的底泥盛放在生物富集处理机构的种植容纳壳体中,在底泥中种植植物对底泥中的重金属进行富集;S6, breaking the porous bottom mud prepared in step S5 into particles of 0.1 to 1 mm, and adding sand particles in a ratio of 10% to 20% relative to the volume of the porous bottom mud and mixing evenly, the particle size of the sand particles is 0.5 to 2 mm, The bottom mud mixed with sand is placed in the planting container of the biological enrichment treatment mechanism, and plants are planted in the bottom mud to enrich the heavy metals in the bottom mud;

将富含水汽的空气从湿度调节接口中注入,富含水汽的空气透过种植容纳壳体中的土壤,对土壤进行补充水分,将普通空气通过加压通风接口注入,空气流经种植容纳壳体中的土壤起到透气作用;Inject air rich in water vapor from the humidity adjustment interface, the air rich in water vapor passes through the soil in the planting container to replenish moisture to the soil, inject ordinary air through the pressurized ventilation port, and the air flows through the planting container The soil in the body acts as a breather;

当种植容纳壳体中的土壤透气性过差时,平衡排气接口上的泄压阀能够及时将注入的空气泄压排出;When the air permeability of the soil in the planting container is too poor, the pressure relief valve on the balance exhaust port can discharge the injected air in time;

S7、将植物富集处理后的底泥在室外温度大于25℃的条件下暴晒10~15天,在暴晒过程中每隔2~3小时进行翻搅一次,然后利用滤网将底泥中混合的沙粒进行过滤分离。S7. Expose the bottom mud after the plant enrichment treatment to the sun for 10-15 days under the condition that the outdoor temperature is higher than 25°C, stir once every 2-3 hours during the sun exposure process, and then use a filter to mix the bottom mud The sand particles are filtered and separated.

优选地,步骤S5向底泥中曝入大量的微型气泡的过程中,开始时保持固化制备桶中的气压为1.2~1.8个标准大气压,在150℃~300℃的条件下对固化制备桶中的底泥进行干燥固化,待固化制备桶中底泥的含水率降至45%~60%时,调节固化制备桶中的气压在10~30s内均匀降低至于外界气压平衡。Preferably, in step S5, during the process of exposing a large number of micro-bubbles into the bottom mud, the air pressure in the solidification preparation barrel is kept at 1.2 to 1.8 standard atmospheres at the beginning, and the solidification preparation barrel is treated under the condition of 150°C to 300°C. The bottom sludge is dried and solidified. When the water content of the bottom sludge in the solidification preparation tank drops to 45% to 60%, the air pressure in the solidification preparation tank is adjusted to be uniformly reduced within 10 to 30 seconds until the external air pressure is balanced.

说明:利用气压变化,有利于在底泥中制造出更加丰富的孔隙结构,将底泥与沙粒混合作为土壤种植植物时,有利于植物根系进行一定的透气。Explanation: Using air pressure changes is beneficial to create a richer pore structure in the bottom mud. When mixing bottom mud and sand as soil for planting plants, it is beneficial for the plant roots to have a certain degree of ventilation.

与现有技术相比,本发明的有益效果是:本发明结构设计合理,操作方便,首先利用预处理滤洗机构以及精细化滤洗机构对底泥进行处理能够去除底泥中的部分重金属以及绝大部分有机杂质,方便后续进行进一步处理,双层设计的生物富集处理机构能够更加精准的控制底泥土壤的湿度、温度以及能够对底泥土壤进行可控的通风处理,利用植物的富集作用将底泥中的重金属有效转移固化在植物中,最后对这些富含重金属的植物进行高温分解即可。Compared with the prior art, the beneficial effects of the present invention are: the present invention has reasonable structural design and convenient operation. Firstly, the sediment is treated by using the pretreatment filtering mechanism and the fine filtering mechanism, which can remove part of the heavy metals in the sediment and Most of the organic impurities are convenient for subsequent further processing. The double-layer design of the bio-concentration treatment mechanism can more accurately control the humidity and temperature of the bottom mud soil, as well as controllable ventilation treatment of the bottom mud soil. The heavy metals in the sediment can be effectively transferred and solidified in the plants through the collection effect, and finally these heavy metal-rich plants can be pyrolyzed.

附图说明Description of drawings

图1是本发明中预处理滤洗机构的结构示意图;Fig. 1 is the structural representation of pretreatment filtering and washing mechanism among the present invention;

图2是图1的俯视图;Fig. 2 is the top view of Fig. 1;

图3是本发明中精细化滤洗机构的结构示意图;Fig. 3 is the structure schematic diagram of refinement filtering and washing mechanism in the present invention;

图4是图3的俯视图;Fig. 4 is the top view of Fig. 3;

图5是本发明中生物富集处理机构的结构示意图;Fig. 5 is the structural representation of biological enrichment treatment mechanism in the present invention;

图6是图5的俯视图;Figure 6 is a top view of Figure 5;

图7是本发明中底泥孔隙化制备机构的结构示意图;Fig. 7 is a schematic structural view of the bottom mud porosity preparation mechanism in the present invention;

图8是图7的俯视图。FIG. 8 is a top view of FIG. 7 .

图中,10-预处理滤洗机构、11-清洗罐、111-清洗罐顶盖、12-底泥输送管、121-底泥输入接口、122-分散输出环、13-清水输送管、131-排水接口、14-搅拌机构支撑架、15-搅拌机构、151-搅拌轴、152-搅拌叶片、153-第一电机容纳壳、154-第一电机、16-第一输送泵、161-输送泵容纳壳、30-生物富集处理机构、31-种植容纳壳体、32-培育养护壳体、321-湿度调节接口、322-加压通风接口、323-平衡排气接口、40-精细化滤洗机构、41-清洗容纳壳、42-清洗斜板、421-旋转清洗槽、43-倾转清洗管、431-清洗管开槽、44-第二电机、441-第二电机容纳壳、45-底泥输入壳、46-清洗排出壳、47-清洗水管、471-清洗喷头、48-吸附滚筒、481-排渣刮板、482-排渣输送带、483-滤渣容纳壳、50-底泥孔隙化制备机构、51-固化制备桶、511-支撑板、512-侧向支撑围挡、513-侧面支撑板、514-第一破碎凸棱、52-曝气输出壳、53-曝气输送管、531-第二破碎凸棱、54-第二顶盖。In the figure, 10-pretreatment filtering mechanism, 11-cleaning tank, 111-top cover of cleaning tank, 12-bottom sludge delivery pipe, 121-bottom sludge input interface, 122-dispersion output ring, 13-clean water delivery tube, 131 -drainage interface, 14-stirring mechanism support frame, 15-stirring mechanism, 151-stirring shaft, 152-stirring blade, 153-first motor housing, 154-first motor, 16-first delivery pump, 161-delivery Pump housing, 30-biological enrichment treatment mechanism, 31-planting housing, 32-cultivation and maintenance housing, 321-humidity adjustment interface, 322-pressurized ventilation interface, 323-balanced exhaust interface, 40-refinement Filtration and washing mechanism, 41-cleaning housing, 42-cleaning inclined plate, 421-rotary cleaning tank, 43-tilting cleaning pipe, 431-cleaning pipe slotting, 44-second motor, 441-second motor housing, 45-bottom sludge input shell, 46-cleaning and discharging shell, 47-cleaning water pipe, 471-cleaning nozzle, 48-adsorption drum, 481-slag discharge scraper, 482-slag discharge conveyor belt, 483-filter residue containing shell, 50- Bottom mud porosity preparation mechanism, 51-solidification preparation barrel, 511-support plate, 512-lateral support enclosure, 513-side support plate, 514-first broken rib, 52-aeration output shell, 53-aeration Air delivery pipe, 531-the second crushing rib, 54-the second top cover.

具体实施方式detailed description

下面结合图1-图8对本发明进行详细说明,为叙述方便,现对下文所说的方位规定如下:下文所说的上下左右前后方向与各自结构示意图本身投影关系的上下左右前后方向一致。Below in conjunction with Fig. 1-Fig. 8 the present invention is described in detail, for the convenience of narration, the orientation mentioned below is stipulated as follows now: the up, down, left, right, front and back directions mentioned below are consistent with the up, down, left, right, front and back directions of the projection relationship of the respective structural schematic diagrams themselves.

实施例1:Example 1:

一种用于重金属污染底泥的修复系统,如图1、图3、图5以及图7所示,包括预处理滤洗机构10、生物富集处理机构30、精细化滤洗机构40以及底泥孔隙化制备机构50;A repair system for heavy metal-contaminated sediment, as shown in Figure 1, Figure 3, Figure 5 and Figure 7, includes a pretreatment and filtration mechanism 10, a biological enrichment treatment mechanism 30, a refined filtration and Mud porosity preparation mechanism 50;

如图1所示,预处理滤洗机构10包括开口朝上的清洗罐11,清洗罐11内固定设有上下延伸的底泥输送管12,底泥输送管12上端具有底泥输入接口121,清洗罐11顶部安装有清洗罐顶盖111;As shown in Figure 1, the pretreatment filter washing mechanism 10 includes a cleaning tank 11 with an opening facing upwards, and a bottom mud delivery pipe 12 extending up and down is fixed in the cleaning tank 11, and the bottom mud delivery pipe 12 upper end has a bottom mud input interface 121, A cleaning tank top cover 111 is installed on the top of the cleaning tank 11;

清洗罐11内侧壁固定设有环形的清水输送管13,上述清水输送管13上具有多个排水接口131;The inner wall of the cleaning tank 11 is fixed with an annular clear water delivery pipe 13, and the above-mentioned clear water delivery pipe 13 has a plurality of drainage interfaces 131;

底泥输送管12下端固定设有分散输出环122,分散输出环122内部为中空结构且与底泥输送管12内部相连通,分散输出环122上具有多个与自身内部相连通的底泥输出孔1221。The lower end of the sediment conveying pipe 12 is fixed with a dispersion output ring 122. The interior of the dispersion output ring 122 is a hollow structure and communicates with the interior of the sediment conveyance pipe 12. The dispersion output ring 122 has a plurality of sediment outputs connected with itself. Hole 1221.

清洗罐11内侧壁靠近顶部位置固定有搅拌机构支撑架14,搅拌机构支撑架14上安装有搅拌机构15,搅拌机构15包括转动配合连接在搅拌机构支撑架14上的搅拌轴151,搅拌轴151为上下延伸布置,搅拌轴151下端固定设有多个搅拌叶片152;Cleaning tank 11 inner side walls are fixed with stirring mechanism support frame 14 near the top position, and stirring mechanism support frame 14 is equipped with stirring mechanism 15, and stirring mechanism 15 comprises the stirring shaft 151 that is connected to the stirring mechanism support frame 14 in rotation, and stirring shaft 151 Arranged to extend up and down, the lower end of the stirring shaft 151 is fixed with a plurality of stirring blades 152;

搅拌机构支撑架14上固定设有第一电机容纳壳153,第一电机容纳壳153内固定设有第一电机154,搅拌轴151的上端延伸至第一电机容纳壳153内部,第一电机154用于驱动搅拌轴151转动。The stirring mechanism supporting frame 14 is fixedly provided with a first motor housing 153, and the first motor housing 153 is fixed with a first motor 154. The upper end of the stirring shaft 151 extends to the inside of the first motor housing 153. The first motor 154 Used to drive the stirring shaft 151 to rotate.

清洗罐11外侧壁固定设有多个输送泵容纳壳161,输送泵容纳壳161内固定设有第一输送泵16,第一输送泵16的输入端与清洗罐11内部相连通。The outer wall of the cleaning tank 11 is fixed with a plurality of delivery pump housings 161 , and the first delivery pump 16 is fixed inside the delivery pump housing 161 , and the input end of the first delivery pump 16 communicates with the inside of the cleaning tank 11 .

如图3所示,精细化滤洗机构40包括开口朝上的清洗容纳壳41以及固定在清洗容纳壳41内的清洗斜板42,清洗斜板42上侧面具有多个前后延伸的旋转清洗槽421;As shown in FIG. 3 , the refined filtering and washing mechanism 40 includes a cleaning housing 41 with an opening facing upward and a cleaning swash plate 42 fixed in the cleaning housing 41 . The upper side of the cleaning swash plate 42 has a plurality of rotating cleaning tanks extending forward and backward. 421;

旋转清洗槽421内设有前后延伸的倾转清洗管43,倾转清洗管43上具有清洗管开槽431,倾转清洗管43前后两端转动配合连接在清洗容纳壳41侧壁上;The rotating cleaning tank 421 is provided with a tilting cleaning pipe 43 extending forward and backward. The tilting cleaning pipe 43 has a cleaning pipe slot 431.

如图4所示,清洗容纳壳41外侧壁上固定设有多个第二电机容纳壳441,多个上述第二电机容纳壳441与多个倾转清洗管43的位置相对应,第二电机容纳壳441内固定设有第二电机44,倾转清洗管43其中一端的转轴延伸至第二电机容纳壳441内,第二电机44用于驱动倾转清洗管43转动。As shown in Figure 4, a plurality of second motor housings 441 are fixedly arranged on the outer wall of the cleaning housing 41, and the positions of the multiple second motor housings 441 correspond to the positions of the plurality of tilting cleaning pipes 43, and the second motors A second motor 44 is fixed inside the containing case 441 , and the rotating shaft at one end of the tilting cleaning pipe 43 extends into the second motor containing case 441 , and the second motor 44 is used to drive the tilting cleaning pipe 43 to rotate.

清洗容纳壳41外侧靠近清洗斜板42较高的一端固定设有与清洗容纳壳41内相连通的底泥输入壳45,第一输送泵16的输出端通过管道与底泥输入壳45相连通,清洗容纳壳41外侧靠近清洗斜板42较低的一端固定设有与清洗容纳壳41内相连通的清洗排出壳46;The outer side of the cleaning housing 41, which is close to the higher end of the cleaning swash plate 42, is fixed with a sediment input housing 45 which communicates with the cleaning housing 41, and the output end of the first delivery pump 16 communicates with the sediment input housing 45 through a pipeline. The outer side of the cleaning housing 41 is fixed with a cleaning discharge housing 46 connected to the cleaning housing 41 at the lower end of the cleaning swash plate 42;

清洗容纳壳41内固定设有多根前后延伸的清洗水管47,多个清洗水管47一对一设置在旋转清洗槽421上方,清洗水管47下侧具有多个清洗喷头471;A plurality of cleaning water pipes 47 extending forward and backward are fixed inside the cleaning housing 41, and the plurality of cleaning water pipes 47 are arranged one-to-one above the rotating cleaning tank 421, and the lower side of the cleaning water pipe 47 has a plurality of cleaning nozzles 471;

如图3所示,清洗容纳壳41内位于清洗斜板42较低一端转动配合设有前后延伸的吸附滚筒48,吸附滚筒48由电机驱动转动,清洗容纳壳41内位于吸附滚筒48右侧固定设有排渣刮板481,清洗容纳壳41内位于排渣刮板481右侧固定设有排渣输送带482,排渣输送带482另一端延伸至清洗容纳壳41外部,清洗容纳壳41外侧位于排渣输送带482下方固定设有滤渣容纳壳483。As shown in Figure 3, the lower end of the cleaning swash plate 42 in the cleaning housing 41 rotates and is equipped with an adsorption roller 48 extending forward and backward. A slag discharge scraper 481 is provided, and a slag discharge conveyor belt 482 is fixed on the right side of the slag discharge scraper 481 in the cleaning housing 41. Below the slag discharge conveyor belt 482 is fixedly provided with a filter residue containing case 483 .

底泥孔隙化制备机构50用于将底泥制备成多孔隙的泥土,多孔隙的泥土用于生物富集处理机构30进行植物种植;The bottom mud porosity preparation mechanism 50 is used to prepare the bottom mud into porous soil, and the porous soil is used in the biological enrichment treatment mechanism 30 for planting;

如图5所示,生物富集处理机构30包括开口朝上的种植容纳壳体31,种植容纳壳体31外侧包围设有培育养护壳体32,培育养护壳体32上端与种植容纳壳体31上端密封连接;As shown in FIG. 5 , the biological enrichment treatment mechanism 30 includes a planting housing 31 with an opening facing upwards. The outside of the planting housing 31 is surrounded by a cultivation and maintenance housing 32 . Sealed connection at the upper end;

种植容纳壳体31侧壁为镂空结构,种植容纳壳体31内壁铺设有多层无纺布;The side wall of the planting housing 31 is a hollow structure, and the inner wall of the planting housing 31 is covered with multi-layer non-woven fabrics;

如图6所示,培育养护壳体32外侧固定设有湿度调节接口321,培育养护壳体32外侧固定设有加压通风接口322,培育养护壳体32外侧固定设有平衡排气接口323,,平衡排气接口323上具有泄压阀,。As shown in Figure 6, a humidity adjustment interface 321 is fixed on the outside of the cultivation and maintenance housing 32, a pressurized ventilation interface 322 is fixed on the outside of the cultivation and maintenance housing 32, and a balance exhaust interface 323 is fixed on the outside of the cultivation and maintenance housing 32. , There is a pressure relief valve on the balance exhaust port 323 .

如图7所示,底泥孔隙化制备机构50包括开口朝上的固化制备桶51,固化制备桶51内底部固定设有曝气输出壳52,曝气输出壳52顶部固定设有与自身内部相连通的上下延伸的曝气输送管53,曝气输出壳52顶部具有多个曝气小孔;As shown in Figure 7, the sediment porosity preparation mechanism 50 includes a solidification preparation barrel 51 with the opening facing upwards, the bottom of the solidification preparation barrel 51 is fixed with an aeration output shell 52, and the top of the aeration output shell 52 is fixed with a The connected aeration delivery pipe 53 extends up and down, and the top of the aeration output shell 52 has a plurality of small aeration holes;

固化制备桶51包括支撑板511,支撑板511顶部边缘处连接设有环形的侧向支撑围挡512,侧向支撑围挡512由多个侧面支撑板513组合而成,侧面支撑板513下端通过活动铰链与支撑板511连接,侧向支撑围挡52顶部密封安装有第二顶盖54。The curing preparation barrel 51 includes a support plate 511, and the top edge of the support plate 511 is connected with an annular lateral support enclosure 512. The lateral support enclosure 512 is composed of a plurality of side support plates 513, and the lower end of the side support plate 513 passes through The living hinge is connected with the support plate 511 , and the top of the lateral support enclosure 52 is sealed with a second top cover 54 .

侧面支撑板513内侧壁上具有上下延伸的第一破碎凸棱514,曝气输送管53外侧壁上具有上下延伸的第二破碎凸棱531。The inner wall of the side support plate 513 has a first crushing rib 514 extending up and down, and the outer wall of the aeration delivery pipe 53 has a second crushing rib 531 extending up and down.

实施例2:Example 2:

如上述的一种用于重金属污染底泥的修复系统进行重金属污染底泥的修复方法,包括以下步骤:A method for repairing heavy metal-contaminated bottom mud as described above in a repair system for heavy metal-contaminated bottom mud, comprising the following steps:

S1、将重金属污染底泥从河道中采挖出后进行晒干,将晒干的底泥破碎,再将破碎后的底泥过200目的筛滤;S1. Excavate the heavy metal-contaminated bottom mud from the river course and then dry it in the sun, crush the dried bottom mud, and then pass the broken bottom mud through a 200-mesh sieve;

S2、将步骤S1中筛滤后的底泥输送到预处理滤洗机构10的清洗罐11中,并向清洗罐11中注入清水,利用电机驱动搅拌轴151并使得搅拌叶片152对清洗罐11中的泥水混合物不断地搅拌滤洗30min,然后利用第一输送泵16将清洗罐11中的泥水混合物输送到沉淀池中沉淀2h;S2, transport the bottom mud after screening in step S1 to the cleaning tank 11 of the pretreatment filter washing mechanism 10, and inject clear water into the cleaning tank 11, utilize the motor to drive the stirring shaft 151 and make the stirring blade 152 opposite to the cleaning tank 11 The mud-water mixture in the tank is continuously stirred and filtered for 30 minutes, and then the mud-water mixture in the cleaning tank 11 is transported to the sedimentation tank for 2 hours by using the first delivery pump 16;

S3、将步骤S2沉淀池中的沉淀底泥输送到精细化滤洗机构40的底泥输入壳45中,底泥沿清洗斜板42流下的过程中,利用清洗喷头471喷射出的高速水流对底泥进行冲洗;S3. Transport the sedimented sediment in the sedimentation tank in step S2 to the sediment input shell 45 of the refined filter washing mechanism 40. During the process of the sediment flowing down the cleaning inclined plate 42, the high-speed water jetted by the cleaning nozzle 471 is used to Bottom mud is washed;

S4、步骤S3经过冲洗后的底泥从清洗排出壳46中排出,然后利用烘干设备对底泥进行除水处理,将底泥的含水率控制在85%;S4. The bottom sludge after washing in step S3 is discharged from the cleaning and discharging shell 46, and then the bottom sludge is dewatered by using a drying device to control the moisture content of the bottom sludge at 85%;

S5、将步骤S4处理后的底泥输送到底泥孔隙化制备机构50的固化制备桶51中,利用曝气输出壳52向底泥中曝入大量的微型气泡并对整个固化制备桶51进行加热升温,温度控制在150℃,对固化制备桶51中的底泥进行干燥固化,得到多孔隙底泥;S5. Transport the bottom sludge treated in step S4 to the solidification preparation bucket 51 of the bottom sludge porosity preparation mechanism 50, use the aeration output shell 52 to expose a large amount of micro air bubbles into the bottom sludge and heat the entire solidification preparation bucket 51 Heating up, the temperature is controlled at 150°C, drying and solidifying the bottom sludge in the solidification preparation tank 51 to obtain porous bottom sludge;

S6、将步骤S5制备的多孔隙底泥破碎成1mm的颗粒,并加入相对于多孔隙底泥体积20%比例的沙粒混合均匀,沙粒的粒径为2mm,将混合有沙粒的底泥盛放在生物富集处理机构30的种植容纳壳体31中,在底泥中种植杜鹃对底泥中的重金属进行富集;S6. Break the porous bottom mud prepared in step S5 into 1mm particles, and add sand particles with a ratio of 20% of the volume of the porous bottom mud to mix evenly. The particle size of the sand particles is 2mm. The mud is contained in the planting container 31 of the biological enrichment treatment mechanism 30, and rhododendrons are planted in the bottom mud to enrich the heavy metals in the bottom mud;

将富含水汽的空气从湿度调节接口321中注入,富含水汽的空气透过种植容纳壳体31中的土壤,对土壤进行补充水分,将普通空气通过加压通风接口322注入,空气流经种植容纳壳体31中的土壤起到透气作用;Inject air rich in water vapor from the humidity adjustment interface 321, the air rich in water vapor passes through the soil in the planting housing 31 to replenish moisture to the soil, inject ordinary air through the pressurized ventilation interface 322, and the air flows through The soil in the planting housing 31 acts as a breather;

当种植容纳壳体31中的土壤透气性过差时,平衡排气接口323上的泄压阀能够及时将注入的空气泄压排出;When the air permeability of the soil in the planting housing 31 is too poor, the pressure relief valve on the balance exhaust port 323 can discharge the injected air in time;

S7、将植物富集处理后的底泥在室外温度大于25℃的条件下暴晒10天,在暴晒过程中每隔3小时进行翻搅一次,然后利用滤网将底泥中混合的沙粒进行过滤分离。S7. Expose the bottom mud after the plant enrichment treatment for 10 days under the condition that the outdoor temperature is greater than 25° C., stir once every 3 hours during the exposure process, and then use a filter to filter the mixed sand particles in the bottom mud. Separated by filtration.

步骤S5向底泥中曝入大量的微型气泡的过程中,开始时保持固化制备桶51中的气压为1.2个标准大气压,在150℃的条件下对固化制备桶51中的底泥进行干燥固化,待固化制备桶51中底泥的含水率降至60%时,调节固化制备桶51中的气压在10s内均匀降低至于外界气压平衡。In step S5, during the process of exposing a large number of micro-bubbles into the bottom mud, keep the air pressure in the solidification preparation tank 51 at 1.2 standard atmospheric pressure at the beginning, and dry and solidify the bottom mud in the solidification preparation tank 51 under the condition of 150°C , when the water content of the bottom mud in the solidification preparation barrel 51 drops to 60%, adjust the air pressure in the solidification preparation barrel 51 to decrease evenly within 10 seconds to the outside air pressure balance.

实施例3:Example 3:

如上述的一种用于重金属污染底泥的修复系统进行重金属污染底泥的修复方法,包括以下步骤:A method for repairing heavy metal-contaminated bottom mud as described above in a repair system for heavy metal-contaminated bottom mud, comprising the following steps:

S1、将重金属污染底泥从河道中采挖出后进行晒干,将晒干的底泥破碎,再将破碎后的底泥过100目的筛滤;S1. Excavate the heavy metal contaminated bottom mud from the river course and then dry it in the sun, crush the dried bottom mud, and then pass the broken bottom mud through a 100-mesh sieve;

S2、将步骤S1中筛滤后的底泥输送到预处理滤洗机构10的清洗罐11中,并向清洗罐11中注入清水,利用电机驱动搅拌轴151并使得搅拌叶片152对清洗罐11中的泥水混合物不断地搅拌滤洗90min,然后利用第一输送泵16将清洗罐11中的泥水混合物输送到沉淀池中沉淀3h;S2, transport the bottom mud after screening in step S1 to the cleaning tank 11 of the pretreatment filter washing mechanism 10, and inject clear water into the cleaning tank 11, utilize the motor to drive the stirring shaft 151 and make the stirring blade 152 opposite to the cleaning tank 11 The mud-water mixture in the tank is continuously stirred and filtered for 90 minutes, and then the mud-water mixture in the cleaning tank 11 is transported to the sedimentation tank for 3 hours by using the first delivery pump 16;

S3、将步骤S2沉淀池中的沉淀底泥输送到精细化滤洗机构40的底泥输入壳45中,底泥沿清洗斜板42流下的过程中,利用清洗喷头471喷射出的高速水流对底泥进行冲洗;S3. Transport the sedimented sediment in the sedimentation tank in step S2 to the sediment input shell 45 of the refined filter washing mechanism 40. During the process of the sediment flowing down the cleaning inclined plate 42, the high-speed water jetted by the cleaning nozzle 471 is used to Bottom mud is washed;

S4、步骤S3经过冲洗后的底泥从清洗排出壳46中排出,然后利用烘干设备对底泥进行除水处理,将底泥的含水率控制在70%;S4. The washed bottom sludge in step S3 is discharged from the cleaning and discharging shell 46, and then the bottom sludge is dewatered by using a drying device, and the moisture content of the bottom sludge is controlled at 70%;

S5、将步骤S4处理后的底泥输送到底泥孔隙化制备机构50的固化制备桶51中,利用曝气输出壳52向底泥中曝入大量的微型气泡并对整个固化制备桶51进行加热升温,温度控制在300℃,对固化制备桶51中的底泥进行干燥固化,得到多孔隙底泥;S5. Transport the bottom sludge treated in step S4 to the solidification preparation bucket 51 of the bottom sludge porosity preparation mechanism 50, use the aeration output shell 52 to expose a large amount of micro air bubbles into the bottom sludge and heat the entire solidification preparation bucket 51 Heating up, controlling the temperature at 300°C, drying and solidifying the bottom sludge in the solidification preparation tank 51 to obtain porous bottom sludge;

S6、将步骤S5制备的多孔隙底泥破碎成0.1mm的颗粒,并加入相对于多孔隙底泥体积10%比例的沙粒混合均匀,沙粒的粒径为0.5mm,将混合有沙粒的底泥盛放在生物富集处理机构30的种植容纳壳体31中,在底泥中种植冬青对底泥中的重金属进行富集;S6. Break the porous bottom mud prepared in step S5 into 0.1mm particles, and add sand particles with a ratio of 10% of the volume of the porous bottom mud to mix evenly. The particle size of the sand particles is 0.5mm, and the sand particles will be mixed with The bottom mud is contained in the planting housing 31 of the biological enrichment treatment mechanism 30, and the heavy metals in the bottom mud are enriched by planting holly in the bottom mud;

将富含水汽的空气从湿度调节接口321中注入,富含水汽的空气透过种植容纳壳体31中的土壤,对土壤进行补充水分,将普通空气通过加压通风接口322注入,空气流经种植容纳壳体31中的土壤起到透气作用;Inject air rich in water vapor from the humidity adjustment interface 321, the air rich in water vapor passes through the soil in the planting housing 31 to replenish moisture to the soil, inject ordinary air through the pressurized ventilation interface 322, and the air flows through The soil in the planting housing 31 acts as a breather;

当种植容纳壳体31中的土壤透气性过差时,平衡排气接口323上的泄压阀能够及时将注入的空气泄压排出;When the air permeability of the soil in the planting housing 31 is too poor, the pressure relief valve on the balance exhaust port 323 can discharge the injected air in time;

S7、将植物富集处理后的底泥在室外温度大于25℃的条件下暴晒15天,在暴晒过程中每隔3小时进行翻搅一次,然后利用滤网将底泥中混合的沙粒进行过滤分离。S7. Expose the bottom mud after the plant enrichment treatment for 15 days under the condition that the outdoor temperature is greater than 25° C., stir once every 3 hours during the exposure process, and then use a filter to filter the mixed sand particles in the bottom mud. Separated by filtration.

步骤S5向底泥中曝入大量的微型气泡的过程中,开始时保持固化制备桶51中的气压为1.8个标准大气压,在300℃的条件下对固化制备桶51中的底泥进行干燥固化,待固化制备桶51中底泥的含水率降至45%时,调节固化制备桶51中的气压在30s内均匀降低至于外界气压平衡。In step S5, during the process of exposing a large number of micro-bubbles into the bottom mud, keep the air pressure in the solidification preparation tank 51 at 1.8 standard atmospheric pressure at the beginning, and dry and solidify the bottom mud in the solidification preparation tank 51 under the condition of 300°C , when the water content of the bottom mud in the solidification preparation barrel 51 drops to 45%, the air pressure in the solidification preparation barrel 51 is adjusted to decrease uniformly within 30 seconds until the external air pressure is balanced.

实施例4:Example 4:

如上述的一种用于重金属污染底泥的修复系统进行重金属污染底泥的修复方法,包括以下步骤:A method for repairing heavy metal-contaminated bottom mud as described above in a repair system for heavy metal-contaminated bottom mud, comprising the following steps:

S1、将重金属污染底泥从河道中采挖出后进行晒干,将晒干的底泥破碎,再将破碎后的底泥过100目的筛滤;S1. Excavate the heavy metal contaminated bottom mud from the river course and then dry it in the sun, crush the dried bottom mud, and then pass the broken bottom mud through a 100-mesh sieve;

S2、将步骤S1中筛滤后的底泥输送到预处理滤洗机构10的清洗罐11中,并向清洗罐11中注入清水,利用电机驱动搅拌轴151并使得搅拌叶片152对清洗罐11中的泥水混合物不断地搅拌滤洗60min,然后利用第一输送泵16将清洗罐11中的泥水混合物输送到沉淀池中沉淀3h;S2, transport the bottom mud after screening in step S1 to the cleaning tank 11 of the pretreatment filter washing mechanism 10, and inject clear water into the cleaning tank 11, utilize the motor to drive the stirring shaft 151 and make the stirring blade 152 opposite to the cleaning tank 11 The mud-water mixture in the tank is continuously stirred and filtered for 60 minutes, and then the mud-water mixture in the cleaning tank 11 is transported to the sedimentation tank for 3 hours by using the first delivery pump 16;

S3、将步骤S2沉淀池中的沉淀底泥输送到精细化滤洗机构40的底泥输入壳45中,底泥沿清洗斜板42流下的过程中,利用清洗喷头471喷射出的高速水流对底泥进行冲洗;S3. Transport the sedimented sediment in the sedimentation tank in step S2 to the sediment input shell 45 of the refined filter washing mechanism 40. During the process of the sediment flowing down the cleaning inclined plate 42, the high-speed water jetted by the cleaning nozzle 471 is used to Bottom mud is washed;

S4、步骤S3经过冲洗后的底泥从清洗排出壳46中排出,然后利用烘干设备对底泥进行除水处理,将底泥的含水率控制在75%;S4. The washed bottom sludge in step S3 is discharged from the cleaning and discharging shell 46, and then the bottom sludge is dewatered by using a drying device to control the moisture content of the bottom sludge at 75%;

S5、将步骤S4处理后的底泥输送到底泥孔隙化制备机构50的固化制备桶51中,利用曝气输出壳52向底泥中曝入大量的微型气泡并对整个固化制备桶51进行加热升温,温度控制在200℃,对固化制备桶51中的底泥进行干燥固化,得到多孔隙底泥;S5. Transport the bottom sludge treated in step S4 to the solidification preparation bucket 51 of the bottom sludge porosity preparation mechanism 50, use the aeration output shell 52 to expose a large amount of micro air bubbles into the bottom sludge and heat the entire solidification preparation bucket 51 Heating up, controlling the temperature at 200°C, drying and solidifying the bottom sludge in the solidification preparation tank 51 to obtain porous bottom sludge;

S6、将步骤S5制备的多孔隙底泥破碎成0.5mm的颗粒,并加入相对于多孔隙底泥体积15%比例的沙粒混合均匀,沙粒的粒径为1mm,将混合有沙粒的底泥盛放在生物富集处理机构30的种植容纳壳体31中,在底泥中种植杜鹃和香菜对底泥中的重金属进行富集;S6, the porous bottom mud prepared in step S5 is broken into particles of 0.5mm, and the sand particles with a ratio of 15% of the volume of the porous bottom mud are added to mix evenly, the particle size of the sand particles is 1mm, and the sand particles mixed with the sand particles are mixed. The bottom mud is contained in the planting housing 31 of the bio-enrichment treatment mechanism 30, and Rhododendron and coriander are planted in the bottom mud to enrich the heavy metals in the bottom mud;

将富含水汽的空气从湿度调节接口321中注入,富含水汽的空气透过种植容纳壳体31中的土壤,对土壤进行补充水分,将普通空气通过加压通风接口322注入,空气流经种植容纳壳体31中的土壤起到透气作用;Inject air rich in water vapor from the humidity adjustment interface 321, the air rich in water vapor passes through the soil in the planting housing 31 to replenish moisture to the soil, inject ordinary air through the pressurized ventilation interface 322, and the air flows through The soil in the planting housing 31 acts as a breather;

当种植容纳壳体31中的土壤透气性过差时,平衡排气接口323上的泄压阀能够及时将注入的空气泄压排出;When the air permeability of the soil in the planting housing 31 is too poor, the pressure relief valve on the balance exhaust port 323 can discharge the injected air in time;

S7、将植物富集处理后的底泥在室外温度大于25℃的条件下暴晒12天,在暴晒过程中每隔2小时进行翻搅一次,然后利用滤网将底泥中混合的沙粒进行过滤分离。S7. Expose the bottom mud after the plant enrichment treatment for 12 days under the condition that the outdoor temperature is greater than 25° C., stir once every 2 hours during the exposure process, and then use a filter to filter the mixed sand particles in the bottom mud. Separated by filtration.

步骤S5向底泥中曝入大量的微型气泡的过程中,开始时保持固化制备桶51中的气压为1.5个标准大气压,在200℃的条件下对固化制备桶51中的底泥进行干燥固化,待固化制备桶51中底泥的含水率降至50%时,调节固化制备桶51中的气压在20s内均匀降低至于外界气压平衡。In step S5, during the process of exposing a large number of micro-bubbles into the bottom mud, keep the air pressure in the solidification preparation tank 51 at 1.5 standard atmospheres at the beginning, and dry and solidify the bottom mud in the solidification preparation tank 51 at 200°C , when the water content of the bottom mud in the solidification preparation barrel 51 drops to 50%, the air pressure in the solidification preparation barrel 51 is adjusted to decrease uniformly within 20 seconds until the external air pressure is balanced.

Claims (10)

1.一种用于重金属污染底泥的修复系统,其特征在于,包括预处理滤洗机构(10)、生物富集处理机构(30)、精细化滤洗机构(40)以及底泥孔隙化制备机构(50);1. A repair system for heavy metal contaminated bottom mud, characterized in that it comprises a pretreatment filter washing mechanism (10), a biological enrichment treatment mechanism (30), a refined filter washing mechanism (40) and bottom mud porosity preparation mechanism (50); 所述预处理滤洗机构(10)包括开口朝上的清洗罐(11),所述清洗罐(11)内固定设有上下延伸的底泥输送管(12),所述底泥输送管(12)上端具有底泥输入接口(121),所述清洗罐(11)顶部安装有清洗罐顶盖(111);The pretreatment filtering and washing mechanism (10) comprises a cleaning tank (11) with an opening facing upwards, and a bottom mud delivery pipe (12) extending up and down is fixedly installed in the cleaning tank (11), and the bottom mud delivery pipe ( 12) The upper end has a sediment input interface (121), and the top of the cleaning tank (11) is equipped with a cleaning tank top cover (111); 所述清洗罐(11)内侧壁靠近顶部位置固定有搅拌机构支撑架(14),所述搅拌机构支撑架(14)上安装有搅拌机构(15),所述搅拌机构(15)包括转动配合连接在所述搅拌机构支撑架(14)上的搅拌轴(151),所述搅拌轴(151)为上下延伸布置,所述搅拌轴(151)下端固定设有多个搅拌叶片(152);The inside wall of the cleaning tank (11) is fixed with a stirring mechanism support frame (14) near the top position, and a stirring mechanism (15) is installed on the described stirring mechanism support frame (14), and the described stirring mechanism (15) includes a rotating fit The stirring shaft (151) connected to the support frame (14) of the stirring mechanism, the stirring shaft (151) is arranged to extend up and down, and the lower end of the stirring shaft (151) is fixedly provided with a plurality of stirring blades (152); 所述精细化滤洗机构(40)包括开口朝上的清洗容纳壳(41)以及固定在所述清洗容纳壳(41)内的清洗斜板(42),所述清洗斜板(42)上飞有多个前后延伸的旋转清洗槽(421);The refined filtering and washing mechanism (40) includes a cleaning housing (41) with an opening facing upwards and a cleaning swash plate (42) fixed in the cleaning housing (41), on the cleaning swash plate (42) There are multiple rotating cleaning tanks (421) extending forward and backward; 所述清洗容纳壳(41)外侧靠近所述清洗斜板(42)较高的一端固定设有与所述清洗容纳壳(41)内相连通的底泥输入壳(45),所述清洗容纳壳(41)外侧靠近所述清洗斜板(42)较低的一端固定设有与所述清洗容纳壳(41)内相连通的清洗排出壳(46);The outer side of the cleaning housing (41) close to the higher end of the cleaning swash plate (42) is fixed with a sediment input housing (45) connected to the cleaning housing (41). The outer side of the shell (41) close to the lower end of the cleaning inclined plate (42) is fixed with a cleaning discharge shell (46) communicating with the inside of the cleaning housing shell (41); 所述清洗容纳壳(41)内固定设有多根前后延伸的清洗水管(47),多个所述清洗水管(47)一对一设置在所述旋转清洗槽(421)上方,所述清洗水管(47)下侧具有多个清洗喷头(471);The cleaning container (41) is fixed with a plurality of cleaning water pipes (47) extending back and forth, and the plurality of cleaning water pipes (47) are arranged one by one above the rotary cleaning tank (421). The lower side of the water pipe (47) has a plurality of cleaning nozzles (471); 所述底泥孔隙化制备机构(50)用于将底泥制备成多孔隙的泥土,多孔隙的所述泥土用于生物富集处理机构(30)进行植物种植;The bottom mud porosity preparation mechanism (50) is used to prepare the bottom mud into porous soil, and the porous soil is used for plant planting by the biological enrichment treatment mechanism (30); 所述生物富集处理机构(30)包括开口朝上的种植容纳壳体(31),所述种植容纳壳体(31)外侧包围设有培育养护壳体(32),所述培育养护壳体(32)上端与所述种植容纳壳体(31)上端密封连接;The bio-enrichment treatment mechanism (30) includes a planting housing (31) with an opening facing upwards, and the outside of the planting housing (31) is surrounded by a cultivation and maintenance housing (32), and the cultivation and maintenance housing (32) The upper end is sealingly connected with the upper end of the planting housing (31); 所述种植容纳壳体(31)侧壁为镂空结构,所述种植容纳壳体(31)内壁铺设有多层无纺布;The side wall of the planting housing (31) is a hollow structure, and the inner wall of the planting housing (31) is covered with multi-layer non-woven fabrics; 所述培育养护壳体(32)外侧固定设有湿度调节接口(321),所述培育养护壳体(32)外侧固定设有加压通风接口(322),所述培育养护壳体(32)外侧固定设有平衡排气接口(323),所述平衡排气接口(323)上具有泄压阀。The outside of the cultivation and maintenance housing (32) is fixed with a humidity adjustment interface (321), and the outside of the cultivation and maintenance housing (32) is fixed with a pressurized ventilation interface (322). A balanced exhaust port (323) is fixed on the outer side, and a pressure relief valve is provided on the balanced exhaust port (323). 2.根据权利要求1所述的一种用于重金属污染底泥的修复系统,其特征在于:所述清洗罐(11)内侧壁固定设有环形的清水输送管(13),上述清水输送管(13)上具有多个排水接口(131);2. A kind of repairing system for heavy metal polluted bottom mud according to claim 1, it is characterized in that: the inner wall of the cleaning tank (11) is fixedly provided with an annular clear water delivery pipe (13), and the above-mentioned clear water delivery pipe (13) has multiple drainage interfaces (131); 所述底泥输送管(12)下端固定设有分散输出环(122),所述分散输出环(122)内部为中空结构且与所述底泥输送管(12)内部相连通,所述分散输出环(122)上具有多个与自身内部相连通的底泥输出孔(1221)。The lower end of the bottom mud delivery pipe (12) is fixedly provided with a dispersion output ring (122), the interior of the dispersion output ring (122) is hollow and communicated with the interior of the bottom mud delivery pipe (12), The output ring (122) has a plurality of sediment output holes (1221) communicating with its interior. 3.根据权利要求1所述的一种用于重金属污染底泥的修复系统,其特征在于:所述搅拌机构支撑架(14)上固定设有第一电机容纳壳(153),所述第一电机容纳壳(153)内固定设有第一电机(154),所述搅拌轴(151)的上端延伸至所述第一电机容纳壳(153)内部,所述第一电机(154)用于驱动所述搅拌轴(151)转动。3. A repair system for heavy metal-contaminated sediment according to claim 1, characterized in that: a first motor housing (153) is fixed on the support frame (14) of the stirring mechanism, and the second A first motor (154) is fixedly arranged in a motor housing (153), and the upper end of the stirring shaft (151) extends to the inside of the first motor housing (153), and the first motor (154) uses To drive the stirring shaft (151) to rotate. 4.根据权利要求1所述的一种用于重金属污染底泥的修复系统,其特征在于:所述清洗罐(11)外侧壁固定设有多个输送泵容纳壳(161),所述输送泵容纳壳(161)内固定设有第一输送泵(16),所述第一输送泵(16)的输入端与所述清洗罐(11)内部相连通,所述第一输送泵(16)的输出端通过管道与所述底泥输入壳(45)相连通。4. A repair system for heavy metal-contaminated bottom sludge according to claim 1, characterized in that: the outer wall of the cleaning tank (11) is fixedly provided with a plurality of conveying pump housings (161), and the conveying A first delivery pump (16) is fixed inside the pump housing (161), the input end of the first delivery pump (16) communicates with the inside of the cleaning tank (11), and the first delivery pump (16) ) output end communicates with the bottom mud input shell (45) through a pipeline. 5.根据权利要求1所述的一种用于重金属污染底泥的修复系统,其特征在于:所述旋转清洗槽(421)内设有前后延伸的倾转清洗管(43),所述倾转清洗管(43)上具有清洗管开槽(431),所述倾转清洗管(43)前后两端转动配合连接在所述清洗容纳壳(41)侧壁上;5. A repair system for heavy metal-contaminated sediment according to claim 1, characterized in that: said rotary cleaning tank (421) is provided with a tilting cleaning pipe (43) extending forward and backward, and said tilting cleaning pipe (43) The cleaning pipe (43) is provided with a cleaning pipe slot (431), and the front and rear ends of the tilting cleaning pipe (43) are rotationally fitted and connected to the side wall of the cleaning housing (41); 所述清洗容纳壳(41)外侧壁上固定设有多个第二电机容纳壳(441),多个上述第二电机容纳壳(441)与多个所述倾转清洗管(43)的位置相对应,所述第二电机容纳壳(441)内固定设有第二电机(44),所述倾转清洗管(43)其中一端的转轴延伸至所述第二电机容纳壳(441)内,所述第二电机(44)用于驱动所述倾转清洗管(43)转动。The outer wall of the cleaning housing (41) is fixed with multiple second motor housings (441), the positions of the multiple second motor housings (441) and the multiple tilting cleaning pipes (43) Correspondingly, a second motor (44) is fixed inside the second motor housing (441), and the rotating shaft at one end of the tilting cleaning pipe (43) extends into the second motor housing (441). , the second motor (44) is used to drive the tilting cleaning pipe (43) to rotate. 6.根据权利要求1所述的一种用于重金属污染底泥的修复系统,其特征在于:所述清洗容纳壳(41)内位于所述清洗斜板(42)较低一端转动配合设有前后延伸的吸附滚筒(48),所述吸附滚筒(48)由电机驱动转动,所述清洗容纳壳(41)内位于所述吸附滚筒(48)右侧固定设有排渣刮板(481),所述清洗容纳壳(41)内位于所述排渣刮板(481)右侧固定设有排渣输送带(482),所述排渣输送带(482)另一端延伸至所述清洗容纳壳(41)外部,所述清洗容纳壳(41)外侧位于所述排渣输送带(482)下方固定设有滤渣容纳壳(483)。6. The repairing system for heavy metal-contaminated sediment according to claim 1, characterized in that: the lower end of the cleaning swash plate (42) in the cleaning housing (41) is rotated and fitted with a The adsorption drum (48) extending forward and backward, the adsorption drum (48) is driven by a motor to rotate, and the slag discharge scraper (481) is fixed on the right side of the adsorption drum (48) in the cleaning housing (41) A slag discharge conveyor belt (482) is fixed on the right side of the slag discharge scraper (481) in the cleaning housing (41), and the other end of the slag discharge conveyor belt (482) extends to the cleaning container Outside the shell (41), the filter residue containing shell (483) is fixed on the outside of the cleaning containing shell (41) below the slag discharge conveyor belt (482). 7.根据权利要求1所述的一种用于重金属污染底泥的修复系统,其特征在于:所述底泥孔隙化制备机构(50)包括开口朝上的固化制备桶(51),所述固化制备桶(51)内底部固定设有曝气输出壳(52),所述曝气输出壳(52)顶部固定设有与自身内部相连通的上下延伸的曝气输送管(53),所述曝气输出壳(52)顶部具有多个曝气小孔;7. The repair system for heavy metal-contaminated bottom mud according to claim 1, characterized in that: the bottom mud porosity preparation mechanism (50) includes a solidification preparation bucket (51) with an opening facing upwards, the The bottom of the curing preparation barrel (51) is fixed with an aeration output shell (52), and the top of the aeration output shell (52) is fixed with an aeration delivery pipe (53) extending up and down that communicates with the inside of itself. The top of the aeration output shell (52) has a plurality of small aeration holes; 所述固化制备桶(51)包括支撑板(511),所述支撑板(511)顶部边缘处连接设有环形的侧向支撑围挡(512),所述侧向支撑围挡(512)由多个侧面支撑板(513)组合而成,所述侧面支撑板(513)下端通过活动铰链与所述支撑板(511)连接,所述侧向支撑围挡(52)顶部密封安装有第二顶盖(54)。The curing preparation bucket (51) includes a support plate (511), and the top edge of the support plate (511) is connected with an annular lateral support enclosure (512), and the lateral support enclosure (512) is composed of A plurality of side support plates (513) are combined, the lower ends of the side support plates (513) are connected to the support plates (511) through living hinges, and the top of the side support enclosure (52) is sealed with a second top cover (54). 8.根据权利要求1所述的一种用于重金属污染底泥的修复系统,其特征在于:所述侧面支撑板(513)内侧壁上具有上下延伸的第一破碎凸棱(514),所述曝气输送管(53)外侧壁上具有上下延伸的第二破碎凸棱(531)。8. A kind of repairing system for heavy metal contaminated bottom mud according to claim 1, characterized in that: there is a first broken rib (514) extending up and down on the inner side wall of the side support plate (513), the The outer wall of the aeration delivery pipe (53) has a second crushing rib (531) extending up and down. 9.根据权利要求1~8任意一项所述的一种用于重金属污染底泥的修复系统进行重金属污染底泥的修复方法,其特征在于包括以下步骤:9. According to any one of claims 1 to 8, a repair system for heavy metal-contaminated bottom mud carries out a method for repairing heavy metal-contaminated bottom mud, which is characterized in that it comprises the following steps: S1、将重金属污染底泥从河道中采挖出后进行晒干,将晒干的底泥破碎,再将破碎后的底泥过100~200目的筛滤;S1. Excavating the heavy metal-contaminated bottom mud from the river, drying it in the sun, crushing the dried bottom mud, and then passing the broken bottom mud through a 100-200 mesh sieve; S2、将步骤S1中筛滤后的底泥输送到预处理滤洗机构(10)的清洗罐(11)中,并向清洗罐(11)中注入清水,利用电机驱动搅拌轴(151)并使得搅拌叶片(152)对清洗罐(11)中的泥水混合物不断地搅拌滤洗30~90min,然后利用第一输送泵(16)将清洗罐(11)中的泥水混合物输送到沉淀池中沉淀2~3h;S2, transport the bottom mud after screening in step S1 to the cleaning tank (11) of the pretreatment filter washing mechanism (10), and inject clear water into the cleaning tank (11), utilize the motor to drive the stirring shaft (151) and Make the stirring blade (152) continuously stir and filter the mud-water mixture in the cleaning tank (11) for 30-90 minutes, and then use the first delivery pump (16) to transport the mud-water mixture in the cleaning tank (11) to the sedimentation tank for sedimentation 2~3h; S3、将步骤S2沉淀池中的沉淀底泥输送到精细化滤洗机构(40)的底泥输入壳(45)中,底泥沿清洗斜板(42)流下的过程中,利用清洗喷头(471)喷射出的高速水流对底泥进行冲洗;S3, the sedimentation bottom mud in the sedimentation tank of step S2 is transported in the bottom mud input shell (45) of fine filter washing mechanism (40), and in the process that bottom mud flows down along the cleaning inclined plate (42), use the cleaning nozzle ( 471) The jetted high-speed water flow washes the bottom mud; S4、步骤S3经过冲洗后的底泥从清洗排出壳(46)中排出,然后利用烘干设备对底泥进行除水处理,将底泥的含水率控制在70%~85%;S4. The bottom mud after washing in step S3 is discharged from the cleaning and discharging shell (46), and then the bottom mud is dewatered by using a drying device, and the water content of the bottom mud is controlled at 70% to 85%; S5、将步骤S4处理后的底泥输送到底泥孔隙化制备机构(50)的固化制备桶(51)中,利用曝气输出壳(52)向底泥中曝入大量的微型气泡并对整个固化制备桶(51)进行加热升温,温度控制在150℃~300℃,对固化制备桶(51)中的底泥进行干燥固化,得到多孔隙底泥;S5. Transport the bottom mud processed in step S4 to the solidification preparation barrel (51) of the bottom mud porosity preparation mechanism (50), and use the aeration output shell (52) to expose a large amount of micro air bubbles to the bottom mud and to the whole The solidification preparation barrel (51) is heated to raise the temperature, and the temperature is controlled at 150°C to 300°C, and the bottom sludge in the solidification preparation barrel (51) is dried and solidified to obtain porous bottom sludge; S6、将步骤S5制备的多孔隙底泥破碎成0.1~1mm的颗粒,并加入相对于多孔隙底泥体积10%~20%比例的沙粒混合均匀,沙粒的粒径为0.5~2mm,将混合有沙粒的底泥盛放在生物富集处理机构(30)的种植容纳壳体(31)中,在底泥中种植植物对底泥中的重金属进行富集;S6, breaking the porous bottom mud prepared in step S5 into particles of 0.1 to 1 mm, and adding sand particles in a ratio of 10% to 20% relative to the volume of the porous bottom mud and mixing evenly, the particle size of the sand particles is 0.5 to 2 mm, The bottom mud mixed with sand is placed in the planting housing (31) of the biological enrichment treatment mechanism (30), and plants are planted in the bottom mud to enrich the heavy metals in the bottom mud; 将富含水汽的空气从湿度调节接口(321)中注入,富含水汽的空气透过种植容纳壳体(31)中的土壤,对土壤进行补充水分,将普通空气通过加压通风接口(322)注入,空气流经种植容纳壳体(31)中的土壤起到透气作用;Inject air rich in water vapor from the humidity adjustment interface (321), the air rich in water vapor passes through the soil in the planting housing (31) to replenish moisture to the soil, and the ordinary air passes through the pressurized ventilation interface (322 ) injection, the air flows through the soil in the planting housing (31) to play the role of ventilation; 当种植容纳壳体(31)中的土壤透气性过差时,平衡排气接口(323)上的泄压阀能够及时将注入的空气泄压排出;When the air permeability of the soil in the planting housing (31) is too poor, the pressure relief valve on the balance exhaust port (323) can discharge the injected air in time; S7、将植物富集处理后的底泥在室外温度大于25℃的条件下暴晒10~15天,在暴晒过程中每隔2~3小时进行翻搅一次,然后利用滤网将底泥中混合的沙粒进行过滤分离。S7. Expose the bottom mud after the plant enrichment treatment to the sun for 10-15 days under the condition that the outdoor temperature is higher than 25°C, stir once every 2-3 hours during the sun exposure process, and then use a filter to mix the bottom mud The sand particles are filtered and separated. 10.根据权利要求9所述的一种重金属污染底泥的修复方法,其特征在于:所述步骤S5向底泥中曝入大量的微型气泡的过程中,开始时保持固化制备桶(51)中的气压为1.2~1.8个标准大气压,在150℃~300℃的条件下对固化制备桶(51)中的底泥进行干燥固化,待固化制备桶(51)中底泥的含水率降至45%~60%时,调节固化制备桶(51)中的气压在10~30s内均匀降低至于外界气压平衡。10. The repairing method of a kind of heavy metal polluted bottom mud according to claim 9, it is characterized in that: in the process that described step S5 is exposed to a large amount of micro-bubbles in bottom mud, keep solidification preparation bucket (51) at the beginning The air pressure in the tank is 1.2 to 1.8 standard atmospheric pressure, and the bottom sludge in the solidification preparation barrel (51) is dried and solidified under the condition of 150°C to 300°C, and the moisture content of the bottom sludge in the solidification preparation barrel (51) is reduced to When the temperature is 45% to 60%, the air pressure in the curing preparation barrel (51) is adjusted to decrease evenly within 10 to 30 seconds until the external air pressure is balanced.
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