CN103846275A - Stable solidification treatment and sanitary landfill disposal method for polluted soil - Google Patents
Stable solidification treatment and sanitary landfill disposal method for polluted soil Download PDFInfo
- Publication number
- CN103846275A CN103846275A CN201410118532.5A CN201410118532A CN103846275A CN 103846275 A CN103846275 A CN 103846275A CN 201410118532 A CN201410118532 A CN 201410118532A CN 103846275 A CN103846275 A CN 103846275A
- Authority
- CN
- China
- Prior art keywords
- soil
- contaminated soil
- liquid medicine
- treatment
- sanitary
- 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
Links
Images
Abstract
The invention relates to a stable solidification treatment and sanitary landfill disposal method for polluted soil. According to the stable solidification treatment and sanitary landfill disposal method, a corresponding medicament solution is prepared by adopting a solid medicament or a liquid medicament through a stable solidification treatment system of the polluted soil according to pollution properties of different types of heavy-metal polluted soil; the soil which is severely polluted by heavy metals including Pb, Zn, Cu and the like is rapidly treated; the medicament solution and the heavy metals in the polluted soil are subjected to a series of physical and chemical processes by agitating, so that free-state heavy metals which can move easily in the polluted soil are changed into an insoluble state or an indissolvable state. The treated soil reaches sanitary landfill entrance standards and is conveyed into a sanitary landfill to be filled; the soil is filled by layers, is compacted layer by layer and is subjected to daily covering treatment, so as to realize sanitary treatment disposal of the polluted soil. The stable solidification treatment and sanitary landfill disposal method for the polluted soil is wide in applicable range, rapid in reaction speed, short in repairing period, good in flexibility, safe and stable to operate and is economically feasible.
Description
Technical field
The present invention relates to a kind of contaminated soil stable curing and process and sanitary landfills method of disposal, belong to environmental protection technical field.
Background technology
Along with quickening and the day by day raising of people to environmental requirement of China's industrialization, urbanization process, a large amount of contaminated sites has been left in resettlement, stopping production or the bankruptcy of part industrial and mining enterprises, a large amount of uses of agricultural chemicals, pesticide and chemical fertilizer, the continuous increase of Industrial " three Waste ", soil pollution problem is on the rise, health is caused to great threat.Soil pollution relates to multiple industries such as chemical industry, mining, metallurgy, plating, oil refining, and major pollutants comprise heavy metal, volatile organic matter, semi-volatile organic matter, polycyclic aromatic hydrocarbon, Polychlorinated biphenyls, petroleum hydrocarbon, agricultural chemicals etc.But it is very weak that basis is administered in China soil pollution, very lack be ripely suitable for, economically feasible, safe and reliable contaminated soil processing disposal technology and equipment.At present, domestic existing contaminated soil recovery technique mainly comprises that phytoremediation, animal reparation, microorganism reparation, electronic reparation, gas expose to the sun repairs etc., but there are the following problems:
One, the general reaction speed of existing contaminated soil recovery technique is slow, and repairing efficiency is long.Phytoremediation, animal are repaired, microorganism is repaired, gas exposes to the sun, and the technology repairing efficiencies such as reparation are very long, the even time of more than ten years of some needs several years.
Two, existing contaminated soil is processed disposal technology generally has particular requirement to medicament form, and what have can only adopt solid-state pharmacy, and what have can only adopt liquid pharmaceutical, and what have can only adopt gaseous state medicament.
Three, lack economically viable processing disposal technology for heavy-metal contaminated soil.
Summary of the invention
For the problem of above-mentioned existence, the object of the present invention is to provide a kind of contaminated soil stable curing to process and sanitary landfills method of disposal.
To achieve these goals, the technical solution adopted in the present invention is:
Stable curing treatment system by contaminated soil is disposed heavy metal pollution soil treatment, and the soil after processing is disposed is delivered to sanitary filling field nearby and carried out landfill disposal, and concrete steps comprise:
Step 1: according to the polluting property of different heavy-metal contaminated soils, configure corresponding liquid medicine at dispensing system;
Step 2: the liquid medicine configuring is sent into medicament storage tank, store and cushioning effect;
Step 3: the contaminated soil of need processing is inserted to reaction system, by stirring, contaminated soil is evenly arranged in reaction system;
Step 4: the liquid medicine in medicament storage tank is delivered to liquid medicine sprinkling system by supercharging, contaminated soil in reaction system is evenly sprayed, heavy metal chemical reaction in liquid medicine and contaminated soil, per hour contaminated soil in reaction system is stirred 1 time, the stable curing time is 3 ~ 14 days, make the free state heavy metal that is easy to migration in contaminated soil originally become insoluble state or indissoluble state, be solidificated in soil after treatment;
Step 5: soil moisture content after treatment is below 30%, adopting HJ/T 299-2007 method to detect analyzes, if the content of Pb, Zn, Cu ion is respectively lower than 0.25mg/L, 100mg/L, 40mg/L in soil extract, meet sanitary filling field admission standard, the soil that meets sanitary filling field admission standard is transported to sanitary filling field nearby by motor vehicles and machines in batches, adopts independent Zoning landfill, carry out layering landfill, successively compacting, a day covering is processed; Analyze after testing, if in the content of Pb, Zn, Cu ion, any one index is greater than above-mentioned standard in soil, need this batch of contaminated soil again to insert in reaction tank 7, repeating step 1 is to step 4, until meet above-mentioned standard, then be transported to sanitary filling field nearby by motor vehicles and machines in batches, adopt independent Zoning landfill, carry out layering landfill, successively compacting, a day covering is processed.
Owing to having adopted above technical scheme, the present invention is according to the polluting property of different heavy-metal contaminated soils, configure corresponding liquid medicine, evenly be sprayed on the contaminated soil in reaction system, by uniform stirring, the heavy metal generation series of physical in liquid medicine and contaminated soil, chemical process, make the free state heavy metal that is easy to migration in contaminated soil originally become insoluble state or indissoluble state, be solidificated in soil after treatment, make its harm be reduced to the acceptable level of human body and environment.Soil after treatment reaches relevant criterion after testing, is transported to sanitary landfills nearby by motor vehicles and machines in batches, adopts independent Zoning landfill, carries out layering landfill, successively compacting, and a day covering is processed.The stable curing treatment system of contaminated soil of the present invention can be arranged in contaminated site, processes and disposes for the on-the-spot dystopy of contaminated site, reduces cubic metre of earth and stone transhipment amount; Also can be arranged on a special place outside contaminated site, form contaminated soil and process disposal base, for the treatment of the contaminated soil of multiple contaminated sites.
Contaminated soil stable curing of the present invention is processed and sanitary landfills method of disposal, can be according to different contaminated soil features, under different temperatures, adopt different shape, different types of processing to dispose medicament variable concentrations medicament contaminated soil is carried out to fast processing disposal, mainly be applicable to the heavy metals such as Pb, Zn, Cu, reaction speed is fast, and the processing disposal cycle is short, and flexibility is good, security of operation is stable, economically feasible.Soil after treatment reaches relevant criterion after testing, carries out sanitary landfills, realizes the sanitized of contaminated soil and disposes, and has good environmental benefit and social benefit.
Brief description of the drawings
Fig. 1 is the stable curing treatment system schematic diagram of contaminated soil of the present invention.
Fig. 2 is the layout schematic diagram of reaction tank and gantry agitator.
In figure: solid drug bucket 1, agitating device 2, dispensing canister 3, solid dosing mouth 31, liquid dosing mouth 32, solvent adds entrance 33, liquid medicine outlet 34, medicament storage tank 4, medicament storage tank entrance 41, medicament storage tank outlet 42, centrifugal pump 5, flusher 6, flusher entrance 61, circulation medicament entrance 62, reaction tank 7, filter course 71, accumulator tank 8, accumulator tank outlet 81, circulating pump 9, backacter 10, gantry agitator 11, agitator 111.
Detailed description of the invention
Below in conjunction with accompanying drawing, the present invention is described in further detail.
Contaminated soil stable curing provided by the invention is processed and sanitary landfills method of disposal, specifically adopts the method comprising the following steps:
Step 1: according to the polluting property of different heavy-metal contaminated soils, determine and adopt corresponding solid-state pharmacy or liquid pharmaceutical.The CMS series medicament that solid-state pharmacy can adopt Wuhan Urban Environment Protection Engineering Techn Co., Ltd. to produce, the N-type heavy metal fixative that liquid pharmaceutical can adopt Japanese rattan Industry Co., Ltd to produce.By solid-state pharmacy by solid drug bucket 1 within solid dosing mouth 31 adds dispensing canister 3, by liquid pharmaceutical by pipeline within liquid dosing mouth 32 adds dispensing canister 3, solvent is added to entrance 33 by pipeline through solvent and add in dispensing canister 3, stir by agitating device 2, form uniform liquid medicine; Solvent generally adopts water; The mass ratio of solid-state pharmacy and contaminated soil is 0.5% ~ 10%, and the mass ratio of liquid pharmaceutical and contaminated soil is 0.2% ~ 5%;
Step 2: by the liquid medicine configuring by the liquid medicine outlet 34 on dispensing canister 3 the medicament storage tank entrance 41 on medicament storage tank 4 deliver in medicament storage tank 4, store and cushion;
Step 3: the contaminated soil of need processing is inserted to reaction system, reaction system is made up of flusher 6 and reaction tank 7, the contaminated soil of need processing is inserted in reaction tank 7, by backacter 10 or gantry agitator 11, contaminated soil is evenly arranged on the filter course 71 in reaction tank 7;
Step 4: the liquid medicine in medicament storage tank 4 is delivered to the flusher entrance 62 on flusher 6 by the medicament storage tank outlet 42 on medicament storage tank 4 after centrifugal pump 5 superchargings, by the shower nozzle of flusher 6, the contaminated soil in reaction tank 7 is evenly sprayed.Flusher 6 is removable and stretching structure, can above reaction tank 7, move easily, and contaminated soil everywhere in reaction tank 7 is carried out to uniform liquid medicine sprinkling.In liquid medicine sprinkling process or after spraying, by backacter 10 or gantry agitator 11 to the contaminated soil in reaction tank 7 stir, blending or stirring, impel liquid medicine fully to contact with contaminated soil, improve the chemical reaction rate of liquid medicine and Heavy Metals in Contaminated Soils, Reaction time shorten.The agitator 111 that is arranged on gantry agitator 11 belows can adopt pawl formula agitator or rotary-type agitator.Agitator 111 can move left and right along the crossbeam of travelling gantry agitator 11, also can move up and down simultaneously, realize the stirring to the interior any position of reaction tank 7 contaminated soil, per hour contaminated soil in reaction system is stirred 1 time, promote that curing reaction carries out, improve reaction efficiency, Reaction time shorten.Liquid medicine in reaction tank 7 oozes down the filter course 71 to reaction tank 7 gradually, flow to accumulator tank 8 through filtering layer 71, the bottom of reaction tank 7 is provided with accumulator tank outlet 81, liquid medicine in accumulator tank 8 by accumulator tank outlet 81 through circulating pump 9 pumps to the flusher recirculated water entrance 61 on flusher 6, spray by the shower nozzle of flusher 6 again, medicament recycles, and can improve medicament service efficiency, reduces medicament use amount.Heavy metal generation chemical reaction in liquid medicine and the contaminated soil spraying, makes the free state heavy metal that is easy to migration in contaminated soil originally become insoluble state or indissoluble state, is solidificated in soil after treatment.The stable curing time is 3 ~ 14 days.
Step 5: soil moisture content after treatment is below 30%, adopting HJ/T 299-2007 method to detect analyzes, if the content of Pb, Zn, Cu ion is respectively lower than 0.25mg/L, 100mg/L, 40mg/L in soil extract, meet sanitary filling field admission standard, the soil that meets sanitary filling field admission standard is transported to sanitary filling field nearby by motor vehicles and machines in batches, adopts independent Zoning landfill, carry out layering landfill, successively compacting, a day covering is processed; Analyze after testing, if in the content of Pb, Zn, Cu ion, any one index is greater than above-mentioned standard in soil, need this batch of contaminated soil again to insert in reaction tank 7, repeating step 1 is to step 4, until meet above-mentioned standard, then be transported to sanitary filling field nearby by motor vehicles and machines in batches, adopt independent Zoning landfill, carry out layering landfill, successively compacting, a day covering is processed.Realize the sanitized of contaminated soil and dispose, reduce its harm to human body and environment.
Taking factory of Hubei Province contaminated soil as example, in soil, Cu content is 4289mg/kg, treating method according to the following steps:
Step 1: the characteristic that is Cu according to the pollutant of contaminated soil, the CMS-21 type solid-state pharmacy that treatment agent adopts Wuhan Urban Environment Protection Engineering Techn Co., Ltd. to produce, according to the mass ratio 5:100 of solid-state pharmacy and contaminated soil, add medicament, according to solid-state pharmacy and water 1:10 configuration liquid medicine.
Step 2: the liquid medicine configuring is sent into medicament storage tank 4, cushion and store.
Step 3: the Cu contaminated soil of need processing is inserted in reaction tank 7, by gantry agitator 11, contaminated soil is evenly arranged on the filter course 71 in reaction tank 7.
Step 4: the liquid medicine in medicament storage tank 4 is delivered to liquid medicine flusher 6 after by centrifugal pump 5 superchargings, contaminated soil in reaction tank 7 is evenly sprayed, heavy metal chemical reaction in liquid medicine and contaminated soil, the agitator 111 that is arranged on gantry agitator 11 belows moves left and right along the crossbeam of travelling gantry agitator 11, move up and down simultaneously, realize the stirring to the interior any position of reaction tank 7 contaminated soil, per hour contaminated soil in reaction tank 7 is stirred 1 time, promote that curing reaction carries out, improve reaction efficiency, Reaction time shorten.The stable curing time is 7 days, makes the free state Cu ion that is easy to migration in contaminated soil originally become indissoluble state, is solidificated in soil after treatment.
Step 5: soil moisture content after treatment is 23%, adopt HJ/T 299-2007 method to detect, testing result: leachate Cu ion concentration is 0.07mg/L, lower than 40mg/L, meet sanitary filling field admission standard, the soil that meets sanitary filling field admission standard is transported to sanitary filling field nearby by motor vehicles and machines in batches, adopt independent Zoning landfill, carry out layering landfill, successively compacting, a day covering is processed; Realize the sanitized of contaminated soil and dispose, reduce its harm to human body and environment.
Taking factory of Hubei Province contaminated soil as example, in soil, Zn content is 2593mg/kg, treating method according to the following steps:
Step 1: the characteristic that is Zn according to the pollutant of contaminated soil, the CMS-21 type solid-state pharmacy that treatment agent adopts Wuhan Urban Environment Protection Engineering Techn Co., Ltd. to produce, according to the mass ratio 2:100 of solid-state pharmacy and contaminated soil, add medicament, according to solid-state pharmacy and water 1:10 configuration liquid medicine.
Step 2: the liquid medicine configuring is sent into medicament storage tank 4, cushion and store.
Step 3: the Zn contaminated soil of need processing is inserted in reaction tank 7, by gantry agitator 11, contaminated soil is evenly arranged on the filter course 71 in reaction tank 7.
Step 4: the liquid medicine in medicament storage tank 4 is delivered to liquid medicine flusher 6 after by centrifugal pump 5 superchargings, contaminated soil in reaction tank 7 is evenly sprayed, heavy metal chemical reaction in liquid medicine and contaminated soil, the agitator 111 that is arranged on gantry agitator 11 belows moves left and right along the crossbeam of travelling gantry agitator 11, move up and down simultaneously, realize the stirring to the interior any position of reaction tank 7 contaminated soil, per hour contaminated soil in reaction tank 7 is stirred 1 time, promote that curing reaction carries out, improve reaction efficiency, Reaction time shorten.The stable curing time is 7 days, makes the free state Zn ion that is easy to migration in contaminated soil originally become indissoluble state, is solidificated in soil after treatment.
Step 5: soil moisture content after treatment is 15%, adopt HJ/T 299-2007 method to detect, testing result: leachate Zn ion concentration is 4.75mg/L, lower than 100mg/L, meet sanitary filling field admission standard, the soil that meets sanitary filling field admission standard is transported to sanitary filling field nearby by motor vehicles and machines in batches, adopt independent Zoning landfill, carry out layering landfill, successively compacting, a day covering is processed; Realize the sanitized of contaminated soil and dispose, reduce its harm to human body and environment.
Embodiment 3
Taking certain flying dust contaminated soil as example, in soil, Pb content is 3390mg/kg, treating method according to the following steps:
Step 1: the characteristic that is Pb according to the pollutant of contaminated soil, the N-12 type heavy metal fixative that adopts Japanese rattan Industry Co., Ltd to produce, this medicament is liquid pharmaceutical, according to the mass ratio 2:100 of liquid pharmaceutical and contaminated soil, add medicament, according to liquid pharmaceutical and water 2:10 configuration liquid medicine.
Step 2: the liquid medicine configuring is sent into medicament storage tank 4, cushion and store.
Step 3: the Pb contaminated soil of need processing is inserted in reaction tank 7, by gantry agitator 11, contaminated soil is evenly arranged on the filter course 71 in reaction tank 7.
Step 4: the liquid medicine in medicament storage tank 4 is delivered to liquid medicine flusher 6 after by centrifugal pump 5 superchargings, contaminated soil in reaction tank 7 is evenly sprayed, heavy metal chemical reaction in liquid medicine and contaminated soil, the agitator 111 that is arranged on gantry agitator 11 belows moves left and right along the crossbeam of travelling gantry agitator 11, move up and down simultaneously, realize the stirring to the interior any position of reaction tank 7 contaminated soil, per hour contaminated soil in reaction tank 3 is stirred 1 time, promote that curing reaction carries out, improve reaction efficiency, Reaction time shorten.The stable curing time is 3 days, makes the free state Pb ion that is easy to migration in contaminated soil originally become indissoluble state, is solidificated in soil after treatment.
Step 5: soil moisture content after treatment is 8%, adopt HJ/T 299-2007 method to detect, testing result: leachate Pb ion concentration is 0.07mg/L, lower than 0.25mg/L, meet sanitary filling field admission standard, the soil that meets sanitary filling field admission standard is transported to sanitary filling field nearby by motor vehicles and machines in batches, adopt independent Zoning landfill, carry out layering landfill, successively compacting, a day covering is processed; Realize the sanitized of contaminated soil and dispose, reduce its harm to human body and environment.
Embodiment 4
Taking certain flying dust contaminated soil as example, in soil, Pb content is 3390mg/kg, treating method according to the following steps:
Step 1: the characteristic that is Pb according to the pollutant of contaminated soil, the N-12 type heavy metal fixative that adopts Japanese rattan Industry Co., Ltd to produce, this medicament is liquid pharmaceutical, according to the mass ratio 3:100 of liquid pharmaceutical and contaminated soil, add medicament, according to liquid pharmaceutical and water 2:10 configuration liquid medicine.
Step 2: the liquid medicine configuring is sent into medicament storage tank 4, cushion and store.
Step 3: the Pb contaminated soil of need processing is inserted in reaction tank 7, by gantry agitator 11, contaminated soil is evenly arranged on the filter course 71 in reaction tank 7.
Step 4: the liquid medicine in medicament storage tank 4 is delivered to liquid medicine flusher 6 after by centrifugal pump 5 superchargings, contaminated soil in reaction tank 7 is evenly sprayed, heavy metal chemical reaction in liquid medicine and contaminated soil, the agitator 111 that is arranged on gantry agitator 11 belows moves left and right along the crossbeam of travelling gantry agitator 11, move up and down simultaneously, realize the stirring to the interior any position of reaction tank 7 contaminated soil, per hour contaminated soil in reaction tank 3 is stirred 1 time, promote that curing reaction carries out, improve reaction efficiency, Reaction time shorten.The stable curing time is 3 days, makes the free state Pb ion that is easy to migration in contaminated soil originally become indissoluble state, is solidificated in soil after treatment;
Step 5: soil moisture content after treatment is 8.3%, adopt HJ/T 299-2007 method to detect, testing result: leachate Pb ion concentration is less than 0.05mg/L, lower than 0.25mg/L, meet sanitary filling field admission standard, the soil that meets sanitary filling field admission standard is transported to sanitary filling field nearby by motor vehicles and machines in batches, adopt independent Zoning landfill, carry out layering landfill, successively compacting, a day covering is processed; Realize the sanitized of contaminated soil and dispose, reduce its harm to human body and environment.
Claims (1)
1. contaminated soil stable curing is processed and sanitary landfills method of disposal, it is characterized in that: the stable curing treatment system by contaminated soil is disposed heavy metal pollution soil treatment, soil after processing is disposed is delivered to sanitary filling field nearby and is carried out landfill disposal, and concrete steps comprise:
Step 1: according to the polluting property of different heavy-metal contaminated soils, configure corresponding liquid medicine at dispensing system;
Step 2: the liquid medicine configuring is sent into medicament storage tank, store and cushioning effect;
Step 3: the contaminated soil of need processing is inserted to reaction system, by stirring, contaminated soil is evenly arranged in reaction system;
Step 4: the liquid medicine in medicament storage tank is delivered to liquid medicine sprinkling system by supercharging, contaminated soil in reaction system is evenly sprayed, heavy metal chemical reaction in liquid medicine and contaminated soil, per hour contaminated soil in reaction system is stirred 1 time, the stable curing time is 3 ~ 14 days, make the free state heavy metal that is easy to migration in contaminated soil originally become insoluble state or indissoluble state, be solidificated in soil after treatment;
Step 5: soil moisture content after treatment is below 30%, adopting HJ/T 299-2007 method to detect analyzes, if the content of Pb, Zn, Cu ion is respectively lower than 0.25mg/L, 100mg/L, 40mg/L in soil extract, meet sanitary filling field admission standard, the soil that meets sanitary filling field admission standard is transported to sanitary filling field nearby by motor vehicles and machines in batches, adopts independent Zoning landfill, carry out layering landfill, successively compacting, a day covering is processed; Analyze after testing, if in the content of Pb, Zn, Cu ion, any one index is greater than above-mentioned standard in soil, need this batch of contaminated soil again to insert in reaction tank 7, repeating step 1 is to step 4, until meet above-mentioned standard, then be transported to sanitary filling field nearby by motor vehicles and machines in batches, adopt independent Zoning landfill, carry out layering landfill, successively compacting, a day covering is processed.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201410118532.5A CN103846275A (en) | 2014-03-27 | 2014-03-27 | Stable solidification treatment and sanitary landfill disposal method for polluted soil |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201410118532.5A CN103846275A (en) | 2014-03-27 | 2014-03-27 | Stable solidification treatment and sanitary landfill disposal method for polluted soil |
Publications (1)
Publication Number | Publication Date |
---|---|
CN103846275A true CN103846275A (en) | 2014-06-11 |
Family
ID=50854661
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201410118532.5A Pending CN103846275A (en) | 2014-03-27 | 2014-03-27 | Stable solidification treatment and sanitary landfill disposal method for polluted soil |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN103846275A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104614504A (en) * | 2015-01-29 | 2015-05-13 | 上海化工研究院 | Contaminated soil solidification treatment testing method |
CN105436199A (en) * | 2015-12-11 | 2016-03-30 | 凯天环保科技股份有限公司 | Soil remediation device |
CN106269834A (en) * | 2016-10-26 | 2017-01-04 | 南通科技职业学院 | Heavy-metal contaminated soil prosthetic device and restorative procedure thereof |
CN110116129A (en) * | 2019-04-24 | 2019-08-13 | 广西博世科环保科技股份有限公司 | The resistance control of heavy metal pollution of soil former address and vegetation consolidate combined remediation method again |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2005305297A (en) * | 2004-04-21 | 2005-11-04 | Takenaka Komuten Co Ltd | Insolubilization and solidification system for heavy metal polluted soil |
CN102303041A (en) * | 2011-05-16 | 2012-01-04 | 刘阳生 | Composite heavy metal polluted soil in-situ fixing method |
CN102527711A (en) * | 2012-03-02 | 2012-07-04 | 武汉都市环保工程技术股份有限公司 | Movable type contaminated soil remediation system adopting recirculating fluidized bed |
CN102641888A (en) * | 2012-04-19 | 2012-08-22 | 天津生态城环保有限公司 | In-situ remediation method of heavy metal polluted site |
CN202461105U (en) * | 2012-03-02 | 2012-10-03 | 武汉都市环保工程技术股份有限公司 | Movable contaminated soil remediation system with circulating fluid bed |
CN103143555A (en) * | 2013-01-31 | 2013-06-12 | 清华大学 | Reducibility solidification stabilization method of processing soil polluted by toxic organics |
CN103396806A (en) * | 2013-08-02 | 2013-11-20 | 重庆远传环保科技有限公司 | Agent and method used for remedying heavy metal polluted soil |
-
2014
- 2014-03-27 CN CN201410118532.5A patent/CN103846275A/en active Pending
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2005305297A (en) * | 2004-04-21 | 2005-11-04 | Takenaka Komuten Co Ltd | Insolubilization and solidification system for heavy metal polluted soil |
CN102303041A (en) * | 2011-05-16 | 2012-01-04 | 刘阳生 | Composite heavy metal polluted soil in-situ fixing method |
CN102527711A (en) * | 2012-03-02 | 2012-07-04 | 武汉都市环保工程技术股份有限公司 | Movable type contaminated soil remediation system adopting recirculating fluidized bed |
CN202461105U (en) * | 2012-03-02 | 2012-10-03 | 武汉都市环保工程技术股份有限公司 | Movable contaminated soil remediation system with circulating fluid bed |
CN102641888A (en) * | 2012-04-19 | 2012-08-22 | 天津生态城环保有限公司 | In-situ remediation method of heavy metal polluted site |
CN103143555A (en) * | 2013-01-31 | 2013-06-12 | 清华大学 | Reducibility solidification stabilization method of processing soil polluted by toxic organics |
CN103396806A (en) * | 2013-08-02 | 2013-11-20 | 重庆远传环保科技有限公司 | Agent and method used for remedying heavy metal polluted soil |
Non-Patent Citations (2)
Title |
---|
沈华主编: "《固体废物资源化利用与处理处置》", 31 July 2011, 科学出版社 * |
蒋小红: "异位稳定化技术处理重金属复合污染土壤的工程应用研究", 《环境工程》 * |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104614504A (en) * | 2015-01-29 | 2015-05-13 | 上海化工研究院 | Contaminated soil solidification treatment testing method |
CN104614504B (en) * | 2015-01-29 | 2016-06-15 | 上海化工研究院 | A kind of contaminated soil cured test method |
CN105436199A (en) * | 2015-12-11 | 2016-03-30 | 凯天环保科技股份有限公司 | Soil remediation device |
CN106269834A (en) * | 2016-10-26 | 2017-01-04 | 南通科技职业学院 | Heavy-metal contaminated soil prosthetic device and restorative procedure thereof |
CN106269834B (en) * | 2016-10-26 | 2019-03-26 | 南通科技职业学院 | Heavy-metal contaminated soil prosthetic device and its restorative procedure |
CN110116129A (en) * | 2019-04-24 | 2019-08-13 | 广西博世科环保科技股份有限公司 | The resistance control of heavy metal pollution of soil former address and vegetation consolidate combined remediation method again |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN105032916B (en) | The in-situ injection extracting moisturizing circulation disposal system and combined remediation method of a kind of organic material contaminated soil and underground water | |
CN102059247B (en) | Vehicle-mounted repairing equipment and method for polluted site soil and underground water body | |
CN103920703B (en) | The advanced oxidation reducing in-situ governing system of a kind of repairing polluted soil and method | |
CN102091716A (en) | Polluted composite soil repairing method | |
CN103894409A (en) | Stable curing repair system for polluted soil | |
CN106623389A (en) | Remediation method for cyanide contaminated soil | |
CN204892552U (en) | A restoration equipment for polluting deep stirring of soil normal position and injection | |
CN205732267U (en) | The in-situ remediation system of portable contaminated soil | |
CN103846275A (en) | Stable solidification treatment and sanitary landfill disposal method for polluted soil | |
CN104140153B (en) | A kind of device using nanotechnology to repair rock stratum environmental pollution and application | |
CN104971939B (en) | A kind of repair system and restorative procedure of chloro nitrotoleune contaminated land | |
CN103722007B (en) | A kind of contaminated soil in-situ combination restorative procedure | |
CN104353664A (en) | Method for constructing in-situ high-pressure jet-grouting stirring pile for polluted field remediation | |
CN203853374U (en) | In-situ polluted soil leaching system | |
CN103736722A (en) | In-situ polluted soil leaching system and method | |
CN107159698B (en) | Method for in-situ remediation of heavy metal contaminated soil by three-dimensional well leaching combined stabilization | |
CN112845569B (en) | Persulfate method soil persistent organic pollutant in-situ remediation method | |
EP1361002A2 (en) | Method and apparatus for purifying a layer of contaminated soil | |
CN203526195U (en) | Complete equipment for restoring polluted soil | |
CN104826864A (en) | Polluted soil ex-site chemical remediation system | |
CN103861868A (en) | Remediation and in-situ backfill method of polluted soil through stable solidification technology | |
CN103894408A (en) | Contaminated soil stabilizing and solidifying treatment and secure backfilling disposal method | |
CN103894410B (en) | The process of contaminated soil stable curing and the application method in roadbed filling | |
EP3287204A1 (en) | Modular system for remediation treatment of contaminated subterranean substrate and related method | |
CN103613199A (en) | Restoring device for ammonia nitrogen polluted underground water |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20140611 |
|
RJ01 | Rejection of invention patent application after publication |