[go: up one dir, main page]

CN117862205A - Tower plate type leaching repair system suitable for low-permeability soil heavy metal pollution - Google Patents

Tower plate type leaching repair system suitable for low-permeability soil heavy metal pollution Download PDF

Info

Publication number
CN117862205A
CN117862205A CN202311715006.2A CN202311715006A CN117862205A CN 117862205 A CN117862205 A CN 117862205A CN 202311715006 A CN202311715006 A CN 202311715006A CN 117862205 A CN117862205 A CN 117862205A
Authority
CN
China
Prior art keywords
soil
unit
heavy metal
metal pollution
eluent
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN202311715006.2A
Other languages
Chinese (zh)
Inventor
向甲甲
谭学军
殷瑶
孙瑞
张祥
黄晟
孙勇
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shanghai Municipal Engineering Design Insitute Group Co Ltd
Original Assignee
Shanghai Municipal Engineering Design Insitute Group Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Shanghai Municipal Engineering Design Insitute Group Co Ltd filed Critical Shanghai Municipal Engineering Design Insitute Group Co Ltd
Priority to CN202311715006.2A priority Critical patent/CN117862205A/en
Publication of CN117862205A publication Critical patent/CN117862205A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B09DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09CRECLAMATION OF CONTAMINATED SOIL
    • B09C1/00Reclamation of contaminated soil
    • B09C1/02Extraction using liquids, e.g. washing, leaching, flotation

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Soil Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

The invention relates to the field of soil heavy metal remediation, in particular to a tray type leaching remediation system suitable for low-permeability soil heavy metal pollution. The system comprises a soil particle feeding unit, a sieve plate, a leaching solution spraying unit, a negative pressure suction filtration unit and a waste liquid treatment and circulation unit, wherein the soil particle feeding unit is used for feeding by adopting a soil particle powder spraying mode, so that the soil void ratio is increased, and the soil permeability is enhanced; the leaching solution is sprayed and soaked to effectively transfer heavy metals from soil to water phase; performing negative pressure suction filtration to complete solid-liquid separation; the waste liquid is treated and recycled, so that water is saved; the tray type design is flexible and efficient, and the occupied area is saved. The method can be used for leaching and repairing the heavy metal pollution of the sand soil and also can be used for leaching and repairing the low-permeability soil, so that the heavy metal pollution in the low-permeability soil is effectively repaired and removed.

Description

一种适用于低渗透性土壤重金属污染塔板式淋洗修复系统A tray-type leaching and remediation system suitable for heavy metal contamination of low-permeability soil

技术领域Technical Field

本发明涉及土壤重金属修复领域,具体地说是一种适用于低渗透性土壤重金属污染塔板式淋洗修复系统。The invention relates to the field of soil heavy metal remediation, in particular to a tray-type elution remediation system suitable for low-permeability soil heavy metal pollution.

背景技术Background technique

土壤重金属污染对环境和人体健康造成的威胁引起了国内外学者的关注,对其治理已成为日前研究的热点。The threat posed by heavy metal pollution in soil to the environment and human health has attracted the attention of scholars at home and abroad, and its governance has become a hot topic of research recently.

土壤重金属污染具有不可降解性和较强的迁移性,同时重金属土壤污染自然净化耗时长,易引起环境连锁反应,不但影响植物生长,也可能影响大气、水环境质量。土壤重金属污染还可能引起食物链污染,危害人体健康。土壤淋洗法是行之有效的土壤重金属修复方法,土壤淋洗不仅可快速将污染物从土壤中移除,短时间内完成高浓度污染土壤的治理,工艺简单、修复效率高,而且投资消耗和治理费用相对较低廉,尤其适用于小面积重度污染土壤的治理,现已成为污染土壤快速修复技术主要手段之一。传统的搅拌式土壤淋洗修复(装置)系统对低渗透性土壤(粉土/黏土)处理效果不佳、适用性不强,对淋洗产生的泥浆处理成本较高。Heavy metal pollution in soil is non-degradable and highly mobile. At the same time, the natural purification of heavy metal soil pollution takes a long time and is prone to cause environmental chain reactions, which not only affects plant growth, but may also affect the quality of the atmosphere and water environment. Heavy metal pollution in soil may also cause food chain pollution and endanger human health. Soil leaching is an effective method for soil heavy metal remediation. Soil leaching can not only quickly remove pollutants from the soil, but also complete the treatment of high-concentration contaminated soil in a short period of time. It has a simple process and high remediation efficiency, and the investment consumption and treatment costs are relatively low. It is especially suitable for the treatment of small areas of heavily contaminated soil. It has now become one of the main means of rapid remediation technology for contaminated soil. The traditional stirring soil leaching remediation (device) system has poor treatment effect on low permeability soil (silt/clay) and is not very applicable. The cost of treating the mud produced by leaching is high.

发明内容Summary of the invention

本发明针对传统的搅拌式土壤淋洗修复系统对低渗透性土壤(粉土/黏土)处理效果不佳、适用性不强,对淋洗产生的泥浆处理成本较高的问题,提出了一种适用于低渗透性土壤重金属污染塔板式淋洗修复系统,能够有效地修复去除低渗透性土壤中重金属污染。In view of the problems that traditional stirring soil leaching and remediation systems have poor treatment effects on low-permeability soils (silt/clay), are not very applicable, and have high costs for treating the mud produced by leaching, the present invention proposes a tower plate leaching and remediation system suitable for heavy metal pollution in low-permeability soils, which can effectively repair and remove heavy metal pollution in low-permeability soils.

为了解决上述技术问题,本发明通过下述技术方案得以解决:In order to solve the above technical problems, the present invention is solved by the following technical solutions:

一种适用于低渗透性土壤重金属污染塔板式淋洗修复系统,所述修复系统包括若干修复单元,每个修复单元包括土壤颗粒上料单元、筛板、淋洗液喷淋单元、负压抽滤单元和废液处理循环单元;A tray-type elution remediation system suitable for low-permeability soil heavy metal contamination, the remediation system comprising a plurality of remediation units, each of which comprises a soil particle feeding unit, a sieve plate, an eluent spraying unit, a negative pressure filtration unit and a waste liquid treatment circulation unit;

进一步的,所述土壤颗粒上料单元,包括气力输送机和土壤上料喷口,所述气力输送机能够输送粒径为2mm及以下的颗粒且流速可调,流速与土壤粒径成正比。所述土壤上料喷口可移动,能够均匀地将土壤颗粒喷洒到筛板上。Furthermore, the soil particle feeding unit comprises a pneumatic conveyor and a soil feeding nozzle, wherein the pneumatic conveyor can convey particles with a particle size of 2 mm or less and has an adjustable flow rate, which is proportional to the soil particle size. The soil feeding nozzle is movable and can evenly spray the soil particles onto the sieve plate.

进一步的,所述筛板,包括下层微孔陶瓷过滤板及上层尼龙滤网,所述陶瓷过滤板孔径不大于土壤粒径,优选地所述陶瓷过滤板孔径为0.05mm,所述尼龙滤网为1000目滤网。所述筛板上土壤上料厚度与土壤粒径成正比。Furthermore, the sieve plate comprises a lower microporous ceramic filter plate and an upper nylon filter screen, the pore size of the ceramic filter plate is not larger than the soil particle size, preferably the pore size of the ceramic filter plate is 0.05 mm, and the nylon filter screen is a 1000 mesh filter screen. The soil material thickness on the sieve plate is proportional to the soil particle size.

进一步的,所述淋洗液喷淋单元配备多个喷头,喷洒范围可均匀覆盖筛板,雾化程度高,水滴细小,对下方土壤打击强度小,喷速与土壤上料厚度成正比。淋洗液对土壤具有较好的润湿度。所述淋洗液浸没土壤,静置一段时间,静置时间与土壤粒径成反比。Furthermore, the eluent spray unit is equipped with multiple nozzles, the spraying range can evenly cover the sieve plate, the atomization degree is high, the water droplets are small, the impact strength on the soil below is small, and the spraying speed is proportional to the thickness of the soil. The eluent has a good wettability to the soil. The eluent immerses the soil and stands for a period of time, and the standing time is inversely proportional to the soil particle size.

进一步的,所述负压抽滤单元包括真空泵和抽气口,所述真空泵能够产生较高的真空度,多级真空泵串联使用,所述抽气口有挡板保护装置防止淋洗液进入,所述负压抽滤单元具有较好的密封性,抽滤时排液口处于密封状态。Furthermore, the negative pressure filtration unit includes a vacuum pump and an air suction port. The vacuum pump can produce a higher vacuum degree. Multi-stage vacuum pumps are used in series. The air suction port has a baffle protection device to prevent the eluent from entering. The negative pressure filtration unit has good sealing performance, and the discharge port is in a sealed state during filtration.

进一步的,所述废液处理循环单元包括淋洗废液处理池和淋洗液配制池。Furthermore, the waste liquid treatment circulation unit includes a leaching waste liquid treatment tank and a leaching liquid preparation tank.

进一步的,所述修复单元采取模块化设计,根据场地情况可以进行塔板式组合。Furthermore, the repair unit adopts a modular design and can be combined in a tower plate manner according to site conditions.

适用于低渗透性土壤重金属污染塔板式淋洗修复系统包括以下修复步骤:The plate elution remediation system for heavy metal pollution in low permeability soil includes the following remediation steps:

(1)根据重金属污染特征、土壤类型、场地状况布设所述土壤颗粒上料单元、筛板、淋洗液喷淋单元、负压抽滤单元和废液处理循环单元;(1) Arranging the soil particle feeding unit, sieve plate, eluent spraying unit, negative pressure filtration unit and waste liquid treatment circulation unit according to the heavy metal pollution characteristics, soil type and site conditions;

(2)将预先筛分的受污染土壤(粒径≤2mm)通过所述土壤颗粒上料单元均匀铺洒到上述筛板上;(2) evenly spreading the pre-screened contaminated soil (particle size ≤ 2 mm) onto the sieve plate through the soil particle feeding unit;

(3)通过所述淋洗液喷淋单元向所述筛板上污染土壤颗粒喷洒淋洗液,待淋洗液浸没土壤颗粒停止喷淋,静置一段时间,通过负压抽滤单元将淋洗液抽出到筛板下排液口,至抽干;(3) spraying the eluent onto the contaminated soil particles on the sieve plate through the eluent spraying unit, stopping the spraying when the eluent submerges the soil particles, letting it stand for a period of time, and extracting the eluent to the drain port under the sieve plate through the negative pressure filtration unit until it is drained;

(4)淋洗废液经所述废液处理循环单元处理循环利用;(4) the elution waste liquid is treated and recycled by the waste liquid treatment circulation unit;

(5)重复进行步骤(2)至(4)的处理,以循环往复地溶出处理重金属;(5) Repeating steps (2) to (4) to dissolve and treat heavy metals in a cyclic manner;

(6)一批土壤处理完成后经出料口取出,新一批上料处理。(6) After a batch of soil is processed, it is taken out through the discharge port and a new batch of soil is loaded for processing.

本发明与传统的土壤淋洗修复系统相比有如下优点:Compared with the traditional soil leaching and remediation system, the present invention has the following advantages:

(1)自动化程度高,气力输送机喷粉式上料均匀:通过采用气力输送机和可移动的土壤上料喷口,实现了粒径为2mm及以下的颗粒的自动输送,且流速可调。这使得土壤颗粒在筛板上均匀分布,产生空隙,从而增加土壤透水性。(1) High degree of automation, uniform powder feeding by pneumatic conveyor: By adopting pneumatic conveyor and movable soil feeding nozzle, automatic conveying of particles with a particle size of 2mm and below is achieved, and the flow rate is adjustable. This makes the soil particles evenly distributed on the sieve plate, creating gaps, thereby increasing soil permeability.

(2)喷淋方式润湿土壤颗粒,浸泡方式增加接触时间:淋洗液喷淋单元配备多个喷头,能够均匀覆盖筛板,高度雾化,水滴细小,从而均匀、充分润湿土壤颗粒。通过浸泡方式,淋洗液与土壤颗粒接触时间增加,有助于重金属转移到液相,提高了淋洗效果。(2) Spraying method wets soil particles, and immersion method increases contact time: The eluent spray unit is equipped with multiple nozzles, which can evenly cover the sieve plate, highly atomize, and produce small water droplets, thereby evenly and fully wetting the soil particles. Through the immersion method, the contact time between the eluent and the soil particles is increased, which helps the heavy metals transfer to the liquid phase and improves the elution effect.

(3)采用负压抽滤方式完成固液分离,减少泥浆处理费用:负压抽滤单元通过真空泵产生较高真空度,多级真空泵串联使用,实现了固液分离。相比传统搅拌式系统,该设计不易产生泥浆,大大减少了泥浆处理费用。(3) Use negative pressure filtration to complete solid-liquid separation and reduce mud treatment costs: The negative pressure filtration unit generates a high vacuum degree through a vacuum pump, and multiple vacuum pumps are used in series to achieve solid-liquid separation. Compared with the traditional stirring system, this design is less likely to produce mud, greatly reducing the cost of mud treatment.

(4)模块化设计,灵活组装,节省场地空间:修复单元采用模块化设计,可根据场地情况自由搭建塔板式系统,灵活组装。每个修复单元可以单独控制,操作便捷,并且该设计节省场地空间。(4) Modular design, flexible assembly, and space saving: The repair unit adopts a modular design, and the tower plate system can be freely built according to the site conditions and assembled flexibly. Each repair unit can be controlled individually, which is convenient to operate, and the design saves site space.

(5)淋洗废液循环利用,节约用水:废液处理循环单元包括淋洗废液处理池和淋洗液配制池,实现了淋洗废液的循环利用,节约用水,符合环保理念。(5) Recycling of leaching waste liquid to save water: The waste liquid treatment circulation unit includes a leaching waste liquid treatment pool and a leaching liquid preparation pool, which realizes the recycling of leaching waste liquid, saves water, and complies with the concept of environmental protection.

附图说明BRIEF DESCRIPTION OF THE DRAWINGS

图1为本发明某一具体实施例的整体系统示意图;FIG1 is a schematic diagram of an overall system of a specific embodiment of the present invention;

图2为本发明某一具体实施例的整体工艺流程图;FIG2 is an overall process flow chart of a specific embodiment of the present invention;

图中各编号:1.气力输送机;2.土壤上料喷口;3.筛板;4.淋洗液喷头;5.离心泵;6.淋洗废液处理池;7.真空泵;8.抽气口;9.排液口;10.出料口;11.阀门;12.污染土壤;13.淋洗液配制池。The numbers in the figure are: 1. Pneumatic conveyor; 2. Soil feeding nozzle; 3. Sieve plate; 4. Eluent nozzle; 5. Centrifugal pump; 6. Eluent waste treatment tank; 7. Vacuum pump; 8. Vacuum port; 9. Drain port; 10. Discharge port; 11. Valve; 12. Contaminated soil; 13. Eluent preparation tank.

具体实施方式Detailed ways

以下通过特定的具体实例说明本发明的实施方式,本领域技术人员可由本说明书所揭露的内容轻易地了解本发明的其他优点与功效。本发明还可以通过另外不同的具体实施方式加以实施或应用,本说明书中的各项细节也可以基于不同观点与应用,在没有背离本发明的精神下进行各种修饰或改变。需要说明的是,以下实施例中所提供的图示仅以示意方式说明本发明的基本构想,在不冲突的情况下,以下实施例及实施例中的特征可以相互组合。The following describes the embodiments of the present invention by specific examples, and those skilled in the art can easily understand other advantages and effects of the present invention from the contents disclosed in this specification. The present invention can also be implemented or applied through other different specific embodiments, and the details in this specification can also be modified or changed in various ways based on different viewpoints and applications without departing from the spirit of the present invention. It should be noted that the illustrations provided in the following embodiments only illustrate the basic concept of the present invention in a schematic manner, and the following embodiments and the features in the embodiments can be combined with each other without conflict.

参照附图1、图2与实施例,对本发明作进一步详细描述:With reference to Figures 1 and 2 and the embodiments, the present invention is further described in detail:

在一具体实施例中,土壤颗粒上料单元气力输送机1选用正压密相气力输送机,能够输送粒径为2mm及以下的颗粒且流速可调,流速与土壤粒径成正比。土壤上料喷口2喷头孔径为3mm,可以移动能够均匀地将土壤颗粒喷洒到筛板上。在一具体实施例中上料厚度为20cm。喷粉式上料主要为了产生土壤颗粒空隙,增大土壤透水性。In a specific embodiment, the pneumatic conveyor 1 of the soil particle feeding unit is a positive pressure dense phase pneumatic conveyor, which can convey particles with a particle size of 2 mm or less and has an adjustable flow rate, which is proportional to the soil particle size. The nozzle aperture of the soil feeding nozzle 2 is 3 mm, and it can be moved to evenly spray the soil particles onto the screen plate. In a specific embodiment, the feeding thickness is 20 cm. The powder spraying feeding is mainly to create gaps between soil particles and increase soil permeability.

筛板3主要起到过滤淋洗液的作用,在一具体实施例中筛板3选用5m×5m×0.06m孔径为0.05mm陶瓷过滤板,过滤板底部及四周有不锈钢加强筋支撑,过滤板上附有5m×5m筛孔为1000目的尼龙滤网,方便下料。The sieve plate 3 mainly plays the role of filtering the eluent. In a specific embodiment, the sieve plate 3 uses a 5m×5m×0.06m ceramic filter plate with a pore size of 0.05mm. The bottom and surrounding of the filter plate are supported by stainless steel reinforcing ribs. A 5m×5m nylon filter screen with a sieve hole of 1000 mesh is attached to the filter plate to facilitate material discharge.

在一具体实施例中淋洗液喷淋单元淋洗液喷头4选用漫射式不锈钢喷头,雾化程度高,水滴细小,对下发土壤打击强度小,淋洗液浸泡时间为20min。离心泵5选用10级离心泵,额定功率1000kw,额定扬程2953m。In a specific embodiment, the eluent spraying unit eluent nozzle 4 uses a diffuse stainless steel nozzle with high atomization degree, small water droplets, low impact strength on the soil below, and the eluent soaking time is 20 minutes. The centrifugal pump 5 uses a 10-stage centrifugal pump with a rated power of 1000kw and a rated head of 2953m.

在一具体实施例中负压抽滤单元真空泵7选用3级真空泵串联产生较高真空度。抽气口8上方选用20cmPVC弧形挡板进行保护防止淋洗液抽出。In a specific embodiment, the vacuum pump 7 of the negative pressure filtration unit uses a three-stage vacuum pump connected in series to produce a high vacuum degree. A 20 cm PVC arc baffle is used above the suction port 8 to protect it from the eluent being drawn out.

在一具体实施例中废液处理循环单元淋洗废液处理池6通过投加氢氧化钠回调废液pH值,生成氢氧化铅沉淀。随后通过絮凝、气浮,将氢氧化铅沉淀絮凝成团,通过刮渣机刮走。淋洗液配制池13加入柠檬酸及表面活性剂配制淋洗液,经配制池底部滤网过滤后通过离心泵吸入喷淋系统。In a specific embodiment, the waste liquid treatment circulation unit elution waste liquid treatment tank 6 adjusts the waste liquid pH value by adding sodium hydroxide to generate lead hydroxide precipitate. Then, the lead hydroxide precipitate is flocculated into a mass by flocculation and flotation, and scraped away by a scraper. The elution liquid preparation tank 13 adds citric acid and a surfactant to prepare the elution liquid, which is filtered through the filter screen at the bottom of the preparation tank and then sucked into the spray system through a centrifugal pump.

在一具体实施例中选取5层修复单元进行塔板式搭设。In a specific embodiment, 5 layers of repair units are selected for tower plate type erection.

本发明的一种适用于低渗透性土壤重金属污染塔板式淋洗修复系统包括以下步骤:A tray-type leaching and remediation system for heavy metal pollution in low-permeability soil of the present invention comprises the following steps:

(1)根据重金属污染特征、土壤类型、场地状况布设所述土壤颗粒上料单元、筛板3、淋洗液喷淋单元、负压抽滤单元和废液处理循环单元;(1) Arranging the soil particle feeding unit, the sieve plate 3, the eluent spraying unit, the negative pressure filtration unit and the waste liquid treatment circulation unit according to the heavy metal pollution characteristics, soil type and site conditions;

(2)将预先筛分的受污染土壤通过所述土壤颗粒上料单元均匀铺洒到上述筛板上;(2) evenly spreading the pre-screened contaminated soil onto the sieve plate through the soil particle feeding unit;

(3)通过所述淋洗液喷淋单元向所述筛板上污染土壤颗粒喷洒淋洗液,待淋洗液浸没土壤颗粒停止喷淋,静置一段时间,通过负压抽滤单元将淋洗液抽出到筛板下排液口,至抽干;(3) spraying the eluent onto the contaminated soil particles on the sieve plate through the eluent spraying unit, stopping the spraying when the eluent submerges the soil particles, letting it stand for a period of time, and extracting the eluent to the drain port under the sieve plate through the negative pressure filtration unit until it is drained;

(4)淋洗废液经所述废液处理循环单元处理循环利用;(4) the elution waste liquid is treated and recycled by the waste liquid treatment circulation unit;

(5)重复进行步骤(2)至(4)的处理,以循环往复地溶出处理重金属;(5) Repeating steps (2) to (4) to dissolve and treat heavy metals in a cyclic manner;

(6)一批土壤处理完成后经出料口取出,新一批上料处理。(6) After a batch of soil is processed, it is taken out through the discharge port and a new batch of soil is loaded for processing.

综上,本发明的适用于低渗透性土壤重金属污染塔板式淋洗修复系统,土壤颗粒气力输送自动化程度高,喷粉式上料上料均匀,容易产生土壤颗粒空隙,增大土壤透水性。通过喷淋方式添加淋洗液,能够均匀、充分润湿土壤颗粒;通过浸泡方式增加淋洗液与土壤接触时间,有助于重金属转移到液相。采用负压抽滤方式完成固液分离,不易产生泥浆,大大减少泥浆处理费用。筛板式淋洗可以少量多次淋洗,淋洗较为彻底。塔板式模块化设计,组装灵活,可以根据项目需求自由搭建,节省场地空间。每个修复单元可以单独控制,操作便捷。淋洗废液循环利用,节约用水。In summary, the tower plate elution remediation system suitable for heavy metal pollution in low permeability soil of the present invention has a high degree of automation in the pneumatic conveying of soil particles, and the powder spraying type feeding is uniform, which can easily produce soil particle gaps and increase soil permeability. The addition of elution liquid by spraying can evenly and fully wet the soil particles; increasing the contact time between the elution liquid and the soil by immersion helps to transfer heavy metals to the liquid phase. The solid-liquid separation is completed by negative pressure filtration, which is not easy to produce mud and greatly reduces the cost of mud treatment. The sieve plate elution can be eluted in small amounts and multiple times, and the elution is more thorough. The tower plate modular design is flexible in assembly and can be freely built according to project requirements, saving site space. Each remediation unit can be controlled individually and is easy to operate. The elution waste liquid is recycled to save water.

Claims (7)

1.一种适用于低渗透性土壤重金属污染塔板式淋洗修复系统,其特征在于:1. A tray-type elution and remediation system suitable for low-permeability soil heavy metal pollution, characterized by: 所述修复系统包括若干修复单元,每个修复单元包括土壤颗粒上料单元、筛板(3)、淋洗液喷淋单元、负压抽滤单元和废液处理循环单元;The remediation system comprises a plurality of remediation units, each of which comprises a soil particle feeding unit, a sieve plate (3), a washing liquid spraying unit, a negative pressure filtration unit and a waste liquid treatment circulation unit; 淋洗修复包括以下步骤:The following steps are involved in the leaching repair process: 根据重金属污染特征、土壤类型、场地状况布设所述土壤颗粒上料单元、筛板(3)、淋洗液喷淋单元、负压抽滤单元和废液处理循环单元;The soil particle feeding unit, the sieve plate (3), the eluent spraying unit, the negative pressure filtration unit and the waste liquid treatment circulation unit are arranged according to the heavy metal pollution characteristics, the soil type and the site conditions; 将预先筛分的受污染土壤通过所述土壤颗粒上料单元均匀铺洒到筛板(3)上;Evenly spreading the pre-screened contaminated soil onto the sieve plate (3) through the soil particle feeding unit; 通过所述淋洗液喷淋单元向所述筛板(3)上污染土壤颗粒喷洒淋洗液,待淋洗液浸没土壤颗粒停止喷淋,静置一段时间,通过负压抽滤单元将淋洗液抽出到筛板下排液口,至抽干;The eluent spraying unit sprays the contaminated soil particles on the sieve plate (3) with the eluent spraying unit, stops spraying when the eluent submerges the soil particles, leaves the eluent to stand for a period of time, and then extracts the eluent to the drain port under the sieve plate through the negative pressure filtration unit until it is drained; 淋洗废液经所述废液处理循环单元处理循环利用;The elution waste liquid is treated and recycled by the waste liquid treatment circulation unit; 重复进行上述步骤的处理,以循环往复地溶出处理重金属;Repeat the above steps to dissolve and treat heavy metals repeatedly; 一批土壤处理完成后经出料口取出,新一批上料处理。After one batch of soil is processed, it is taken out through the discharge port and a new batch is loaded for processing. 2.根据权利要求1所述的适用于低渗透性土壤重金属污染塔板式淋洗修复系统,其特征在于:所述土壤颗粒上料单元,包括气力输送机(1)和土壤上料喷口(2),所述气力输送机(1)能够输送粒径为2mm及以下的颗粒且流速可调;所述土壤上料喷口(2)可移动,能够均匀地将土壤颗粒喷洒到筛板上。2. According to claim 1, the tower plate elution remediation system suitable for heavy metal pollution in low permeability soil is characterized in that: the soil particle feeding unit includes a pneumatic conveyor (1) and a soil feeding nozzle (2), the pneumatic conveyor (1) can transport particles with a particle size of 2 mm or less and the flow rate is adjustable; the soil feeding nozzle (2) is movable and can evenly spray soil particles onto the screen plate. 3.根据权利要求1所述的适用于低渗透性土壤重金属污染塔板式淋洗修复系统,其特征在于:所述筛板(3),包括下层微孔陶瓷过滤板及上层尼龙滤网,所述下层微孔陶瓷过滤板孔径不大于土壤粒径,所述筛板上土壤上料厚度与土壤粒径成正比。3. According to claim 1, the tower plate elution remediation system suitable for low permeability soil heavy metal pollution is characterized in that: the sieve plate (3) includes a lower microporous ceramic filter plate and an upper nylon filter screen, the pore size of the lower microporous ceramic filter plate is not larger than the soil particle size, and the soil loading thickness on the sieve plate is proportional to the soil particle size. 4.根据权利要求1所述的适用于低渗透性土壤重金属污染塔板式淋洗修复系统,其特征在于:所述淋洗液喷淋单元配备多个淋洗液喷头(4),喷洒范围均匀覆盖筛板(3),喷速与土壤上料厚度成正比;所述淋洗液浸没土壤,静置一段时间,静置时间与土壤粒径成反比。4. According to claim 1, the tower plate elution remediation system suitable for low permeability soil heavy metal pollution is characterized in that: the eluent spray unit is equipped with multiple eluent nozzles (4), the spraying range evenly covers the sieve plate (3), and the spraying speed is proportional to the soil loading thickness; the eluent immerses the soil and stands for a period of time, and the standing time is inversely proportional to the soil particle size. 5.根据权利要求1所述的适用于低渗透性土壤重金属污染塔板式淋洗修复系统,其特征在于:所述负压抽滤单元包括真空泵(7)和抽气口(8),多级真空泵串联使用,所述抽气口(8)有挡板保护装置防止淋洗液进入;所述负压抽滤单元具有较好的密封性,抽滤时排液口(9)处于密封状态。5. According to claim 1, the tower plate elution remediation system suitable for low permeability soil heavy metal pollution is characterized in that: the negative pressure filtration unit includes a vacuum pump (7) and an air suction port (8), and multiple vacuum pumps are used in series. The air suction port (8) has a baffle protection device to prevent the elution liquid from entering; the negative pressure filtration unit has good sealing performance, and the discharge port (9) is in a sealed state during filtration. 6.根据权利要求1所述的适用于低渗透性土壤重金属污染塔板式淋洗修复系统,其特征在于:所述废液处理循环单元包括淋洗废液处理池(6)和淋洗液配制池(13)。6. The tray-type elution remediation system for heavy metal pollution in low-permeability soil according to claim 1 is characterized in that the waste liquid treatment circulation unit comprises an elution waste liquid treatment tank (6) and an elution liquid preparation tank (13). 7.根据权利要求1所述的适用于低渗透性土壤重金属污染塔板式淋洗修复系统,其特征在于:所述修复单元采取模块化设计,根据场地情况可以进行塔板式组合。7. The tray-type elution remediation system for heavy metal pollution in low-permeability soil according to claim 1 is characterized in that the remediation unit adopts a modular design and can be combined in tray-type according to site conditions.
CN202311715006.2A 2023-12-13 2023-12-13 Tower plate type leaching repair system suitable for low-permeability soil heavy metal pollution Pending CN117862205A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202311715006.2A CN117862205A (en) 2023-12-13 2023-12-13 Tower plate type leaching repair system suitable for low-permeability soil heavy metal pollution

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202311715006.2A CN117862205A (en) 2023-12-13 2023-12-13 Tower plate type leaching repair system suitable for low-permeability soil heavy metal pollution

Publications (1)

Publication Number Publication Date
CN117862205A true CN117862205A (en) 2024-04-12

Family

ID=90595901

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202311715006.2A Pending CN117862205A (en) 2023-12-13 2023-12-13 Tower plate type leaching repair system suitable for low-permeability soil heavy metal pollution

Country Status (1)

Country Link
CN (1) CN117862205A (en)

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002355663A (en) * 2001-05-29 2002-12-10 Ichinomiya Kimitake Soil cleaning system with high pressure jet and method for the same
US20030108462A1 (en) * 2001-12-06 2003-06-12 Oskoui Kazem Eradat Method of extracting contaminants from solid matter
JP2004057901A (en) * 2002-07-26 2004-02-26 Kokan Kogyo Kk Sorting recovery method for metal piece included in soil
JP2017217575A (en) * 2016-06-03 2017-12-14 株式会社フジタ Pretreatment device and pretreatment method of waste
JP2019177322A (en) * 2018-03-30 2019-10-17 株式会社フジタ Processing unit
JP2021007903A (en) * 2019-06-28 2021-01-28 株式会社フジタ Processing system, billing system, and control unit
CN114192559A (en) * 2021-10-29 2022-03-18 成都酉辰环境检测有限公司 Hexavalent chromium contaminated soil remediation device and method

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002355663A (en) * 2001-05-29 2002-12-10 Ichinomiya Kimitake Soil cleaning system with high pressure jet and method for the same
US20030108462A1 (en) * 2001-12-06 2003-06-12 Oskoui Kazem Eradat Method of extracting contaminants from solid matter
JP2004057901A (en) * 2002-07-26 2004-02-26 Kokan Kogyo Kk Sorting recovery method for metal piece included in soil
JP2017217575A (en) * 2016-06-03 2017-12-14 株式会社フジタ Pretreatment device and pretreatment method of waste
JP2019177322A (en) * 2018-03-30 2019-10-17 株式会社フジタ Processing unit
JP2021007903A (en) * 2019-06-28 2021-01-28 株式会社フジタ Processing system, billing system, and control unit
CN114192559A (en) * 2021-10-29 2022-03-18 成都酉辰环境检测有限公司 Hexavalent chromium contaminated soil remediation device and method

Similar Documents

Publication Publication Date Title
CN103722005B (en) A kind of chemical leaching system processing heavy metal-polluted soil, organic contamination
CN203170696U (en) Leaching and repairing equipment of polluted soil
CN114262096A (en) Urban sewage treatment device
CN1171814C (en) Sludge de-watering drying system
CN215712211U (en) Quick flocculation device for sewage treatment
CN215355324U (en) A low-carbon environment-friendly polluted soil leaching and remediation system
CN203803912U (en) Chemical leaching system for treatment of soil heavy metal and organic pollution
CN216614387U (en) Adopt town sludge decrement integrated system of high-efficient physics broken wall
CN117862205A (en) Tower plate type leaching repair system suitable for low-permeability soil heavy metal pollution
CN201626891U (en) Treatment device for waste acid in metal smelting acid making with gas
CN212712974U (en) Energy-concerving and environment-protective type mill sewage treatment plant
CN218502931U (en) Rapid oil sludge leaching device
CN110922027A (en) Sludge dewatering, deodorizing and drying device with solar panel heating
CN205990319U (en) A kind of sewage disposal system
CN204752453U (en) Energy -concerving and environment -protective type sewage treatment plant
CN206508651U (en) The equipment that a kind of high efficiency directly handles blue-green algae in water body
CN208038185U (en) A kind of bubble green pepper and pickle wastewater filtering device
CN208440482U (en) A kind of river surge silt purification device
CN113000586A (en) Be used for prosthetic drip washing device of soil
CN206305190U (en) A kind of organic material contaminated soil prosthetic device
CN215823912U (en) Ultrasonic wave reinforced polluted soil leaching equipment
CN206499941U (en) Aluminium cuts filter
CN212741026U (en) Sewage treatment plant that hydraulic engineering used
CN213416523U (en) Pollute prosthetic high efficiency processing apparatus of water
CN212924776U (en) Sewage treatment system of mud zero release

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination