CN110451628A - A kind of restorative procedure of trichloro ethylene polluted underground water - Google Patents

A kind of restorative procedure of trichloro ethylene polluted underground water Download PDF

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Publication number
CN110451628A
CN110451628A CN201910696338.8A CN201910696338A CN110451628A CN 110451628 A CN110451628 A CN 110451628A CN 201910696338 A CN201910696338 A CN 201910696338A CN 110451628 A CN110451628 A CN 110451628A
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trichloro ethylene
underground water
medicament
aqueous solution
polluted underground
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王晓东
刘玉仙
张克刚
丁冠涛
闫涛
彭圣洁
张晓慧
赵振超
张刚
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University of Jinan
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/72Treatment of water, waste water, or sewage by oxidation
    • C02F1/722Oxidation by peroxides
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/72Treatment of water, waste water, or sewage by oxidation
    • C02F1/725Treatment of water, waste water, or sewage by oxidation by catalytic oxidation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/30Organic compounds
    • C02F2101/36Organic compounds containing halogen
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/06Contaminated groundwater or leachate

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  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

A kind of restorative procedure of trichloro ethylene polluted underground water, belongs to organic contamination groundwater remediation field, comprising the following steps: (1) measures the content of trichloro ethylene in trichloro ethylene polluted underground water and calculate polluted underground water total amount;(2) it is prepared into and repairs medicament A aqueous solution;(3) it is prepared into and repairs medicament B aqueous solution;(4) medicament A aqueous solution will be repaired and repair medicament B aqueous solution and be respectively equally divided into 3 ~ 10 parts;(5) injection well and pumped well are opened up in trichloro ethylene polluted underground water pollution source area, reacts 12 ~ 36h;Meanwhile the re-injection of trichloro ethylene polluted underground water is extracted out from pumped well and enters the injection well;(6) step (5) after the reaction was completed, by pumped well or monitoring well acquisition underground water and to trichloro ethylene Concentration Testing, and records data.(7) when trichloro ethylene concentration, which is higher than, repairs target, then repeatedly step (4)-(6);When pollutant concentration is lower than target is repaired, repair is completed.

Description

A kind of restorative procedure of trichloro ethylene polluted underground water
Technical field
The invention belongs to organic contamination groundwater remediation fields, relate generally to a kind of reparation of trichloro ethylene polluted underground water Method.
Background technique
Trichloro ethylene be commonly used for metal degreasing agent,Fungicide, refrigerant and clothesDry cleaning agent, year usage amount it is huge and Increase year by year.Since trichloro ethylene is using the inappropriate processing of rear waste liquid and the leakage of some holding vessels, when trichloro ethylene pollutes There is generation, seriously polluted soil and groundwater, becomes and be distributed one of widest pollutant in current environment.Trichloro ethylene is A kind of noxious material, volatile and there are " three cause effect ", i.e., carcinogenic, teratogenesis, mutagenesis.In recent years a large number of studies show that they It can cause the illnesss such as paralysis of trigeminal nerve, be listed in a kind of questionable person's class carcinogenic substance at present.So three in underground water and soil The removal of vinyl chloride is particularly important.
Trichloro ethylene has the characteristics that viscosity is low, mobility is strong, once into soil and underground will be caused in environment The pollution of water increases and repairs difficulty.At present the restorative procedure of trichloro ethylene polluted underground water mainly have chemistry redox technology, Electrochemical techniques, bioremediation technology, hydrodynamic seepage pressure technology and ground pump-and-treat technology etc..Wherein it is used for in-situ chemical The oxidant of oxidation mainly includes persulfate, potassium permanganate, Fenton reagent (Fe2++H2O2), ozone etc..Fenton technology is because of it Most of organic matters can be aoxidized, and efficiency is higher and be concerned, but hydrogen peroxide easily decompose under conditions of neutral ph by disproportionation Failure and high-strength hydrogen peroxide oxidation of organic compounds while, can generate the gentle body of big calorimetric, this may cause underground collapse, Omnicide is even exploded.
Persulfate can generate SO by activation methods such as heat, alkali, transition metal4And OH, to have in water of degrading Machine pollutant.However the temperature in underground water is generally 15 DEG C or so, persulfate is not reacted with pollutant at this temperature, if The temperature of underground water is improved with modes such as heating, rehabilitation cost will be very high.Underground water in neutral pH environment is by adding Enter Fe2+/Fe3+Or add the same treatment effect of activation method of alkali bad or underground environment is caused to seriously affect, destroy ecological ring Border.
Calper calcium peroxide is gradually applied to the repairing and treating of polluted underground water because of its controllable-rate for decomposing generation hydrogen peroxide, Oxygen can also be generated simultaneously, facilitate the oxidative degradation of aerobic microbiological, as a kind of Green Oxidant, application increasingly by To attention.Patent No.: 201410561933.8, invention and created name is that " a kind of persulfate-calper calcium peroxide dual oxidants are gone Except the method for multiring aromatic hydrocarbon substance methyl naphthalene " Chinese patent disclose multiring aromatic hydrocarbon substance methyl in a kind of removal water body The method of naphthalene, has main steps that into the water body containing methyl naphthalene, and persulfate and calper calcium peroxide is added, stirs evenly, and ties up System pH is held to react 4-5 days under the conditions of neutral slant acidity, it can oxidation removal polluter.The method that the innovation and creation provide Oxidability is stronger, but practical groundwater environment complexity (such as HCO3 -、CO3 2-、Cl-Plasma interference, Some Organic Pollutants are same When be present in underground environment) or groundwater pollutant concentration it is higher (such as pollution source area, concentration over-standard hundreds times), therefore often need Want the calper calcium peroxide and persulfate additional amount of higher concentration.And underground water is because its buffer capacity is poor compared with soil, calper calcium peroxide The quick raising for easily causing underground environment pH value largely is added, underground water is caused to alkalize, destroys underground environment, while can also make Become extremely faint (calper calcium peroxide mainly generates oxygen under alkaline environment) at the significant wastage or even oxidability of medicament, Practical polluted underground water repairing effect is bad.In addition, technical grade calper calcium peroxide (content 60%) powder contain calcium hydroxide at Point, be dissolved in water will generate more calcium hydroxides (calcium hydroxide and calper calcium peroxide contained in itself be dissolved in water generation hydrogen-oxygen Change calcium), after technical grade calper calcium peroxide used is dissolved in water in live practical application, pH rises faster, influences more caused by environment Greatly.
CaO2After contacting with water, there are following two isolations:
CaO2+H2O→Ca(OH)2↓+1/2O2↑ (1)
CaO2+2H2O→Ca(OH)2↓+H2O2(2)
Above-mentioned patent additionally provides dual oxidants and plays a role optimal pH condition as neutral slant acidity, and acid used in regulating system is Nitric acid.Nitric acid is strong acid, has corrosivity, easily makes quick-fried, highly acid and unstability, and misoperation easily causes harm, such as inhales Acute poisoning, serious person's shock, asphyxia etc. can be caused by entering nitric acid smog.And after calper calcium peroxide is added, as calper calcium peroxide is continuous Dissolution, calcium hydroxide persistently generate, and maintain the underground environment of neutral slant acidity that will be continuously added nitric acid, technique is cumbersome and best PH condition is not easy to control, bad in practical polluted underground water repairing effect, or even as the restriction step of in-situ chemical reparation.
Summary of the invention
In view of the deficiencies of the prior art, the present invention provides can efficiently in-situ immobilization high concentration trichloro ethylene impurely under The method of water.
A kind of in-situ remediation method of trichloro ethylene polluted underground water, comprising the following steps:
(1) it measures the content of trichloro ethylene in trichloro ethylene polluted underground water and calculates polluted underground water total amount, determine underground water The initial concentration and polluted underground water total amount of middle trichloro ethylene, if trichloro ethylene content is a, polluted underground water total amount in underground water For b;
(2) persulfate and calper calcium peroxide are added to the water, are stirred evenly, be prepared into and repair medicament A aqueous solution, make described repair The content of persulfate is 4a ~ 40a in multiple medicament A aqueous solution, and the content of calper calcium peroxide is 10a ~ 40a, the reparation medicament A of configuration Aqueous solution total amount is 9/10b;
(3) surfactant and iron tourmaline powder are added to the water, are stirred evenly, be prepared into and repair medicament B aqueous solution, make institute The content for repairing surfactant in medicament B aqueous solution stated is 0.05a ~ 5a, and the content of iron tourmaline is 1a ~ 15a, configuration Reparation medicament B aqueous solution total amount is 1/10b;
(4) medicament A aqueous solution will be repaired and repair medicament B aqueous solution and be respectively equally divided into 3 ~ 10 parts, medicament A aqueous solution is repaired and repair Multiple medicament B aqueous solution number is identical;
(5) injection well and pumped well are opened up in trichloro ethylene polluted underground water pollution source area;Start high-pressure pump, injection pressure is preferred Portion is first repaired medicament B aqueous solution and injects the injection well by 0.05 ~ 0.10Mpa, after the completion of injection, then portion is repaired medicine Agent A aqueous solution is injected into water injection well, and injection pressure is 0.05 ~ 0.10Mpa, injection speed 5-8L/min, then react 12 ~ 36h;While injection repairs medicament B aqueous solution, repairs medicament A aqueous solution and reaction, trichloro ethylene is extracted out from pumped well Polluted underground water re-injection enters the injection well, and re-injection speed is 5-8L/min, and pumped well and injection well is made to form polluted underground water Circulation makes trichloro ethylene polluted underground water come into full contact with and react with reparation medicament A and reparation medicament B.Repair medicament B mainly as Repair the activator of medicament A.In order to make the pumped well and injection well form good polluted underground water circulation, the pumped well 1 ~ 3 meter, preferably 1.5 meters are divided between injection well;
(6) step (5) after the reaction was completed, acquires underground water by pumped well or monitoring well and to trichloro ethylene Concentration Testing, and Record data;
(7) when trichloro ethylene concentration, which is higher than, repairs target, then repeatedly step (4)-(6);Pollutant concentration is lower than reparation target When, repair is completed.Repairing target preferably uses in " groundwater quality standard " (GB/T 14848-2017) " III class " to mark Quasi- (70 μ g/L).
Calper calcium peroxide described in step (2), preferably nanometer calper calcium peroxide, the calper calcium peroxide solid powder added and ground The mass ratio of trichloro ethylene is 10~40:1, preferably 20~30:1 in lower contaminant water.
Persulfate described in step (2), including sodium peroxydisulfate or potassium peroxydisulfate or both mixture, preferably persulfuric acid The mass ratio of trichloro ethylene is 4~40:1 in sodium, persulfate and underground pollution water.
The mass ratio of trichloro ethylene is 1~15:1 in iron tourmaline described in step (2) and underground pollution water.
Surfactant described in step (2) can be cyclodextrin, three chloroethenes in the cyclodextrin and underground pollution water The mass ratio of alkene is 0.05~5:1.
It is 1:0.25 ~ 10, preferably 1:2.5 that the mass ratio of calper calcium peroxide and persulfate in medicament A is repaired in step (2).
It is 1:1 ~ 750, preferably 1:500 that the mass ratio of surfactant and iron tourmaline in medicament B is repaired in step (3).
1 ~ 3 meter, preferably 1.5 meters are divided into step (5) between pumped well and injection well.
Compared with prior art, the invention has the following advantages that
1. the iron tourmaline being added in the present invention can influence the redox electricity of aqueous solution since there are permanent electrodes for itself Position, and the pH value of aqueous solution is adjusted, it is allowed to tend to neutral, does not cause underground water because largely adding calper calcium peroxide or persulfate Environmental abnormality (pH is higher or relatively low) destroys ecological environment.And iron tourmaline dissolution generates Fe2+, utilize Fe2+Catalysis and Own face is catalyzed persulfate, calper calcium peroxide, more preferable relative to other oxidants and dual oxidants repairing effect, repairs effect Rate and medicament utilization rate are higher.
2. reparation is flexible and efficient, practical: for the equal energy of trichloro ethylene of low concentration in polluted underground water or high concentration Effectively degradation, in above-mentioned calper calcium peroxide and persulfate ratio, can be directed to various concentration or different types of trichloro ethylene Pollution adds the reparation medicament A aqueous solution of different proportion and repairs medicament B aqueous solution, reaches optimal repairing effect, not because of mistake The exception for causing groundwater environment is added in calcium oxide or a large amount of of persulfate.
3. repair process flow is simple, repairing effect efficient stable and will not generate secondary pollution, repaired conducive to later period biology It is multiple.Repair polluted underground water when, by will repair medicament A aqueous solution and reparation medicament B aqueous solution separately inject, can to avoid When configuring medicament aqueous solution, reaction is generated, medicament is caused to waste.
4. repairing short time limit, rehabilitation cost is low: calper calcium peroxide, persulfate are chemical agent, and repairing efficiency is short, repairs Effect is good, and when carrying out in-situ immobilization, save soil excavate, polluted underground water extraction and design sewage-treating reactor Time and expense, it is often more important that can excavate and extract out bring secondary pollution during polluted underground water to avoid soil.
Specific embodiment
Embodiment 1:
The in-situ remediation method of trichloro ethylene polluted underground water, comprising the following steps:
(1) it measures the concentration of trichloro ethylene in underground water and calculates polluted underground water total amount, obtain trichloro ethylene in underground water Concentration is 85mg/L, and polluted underground water total amount is 50m3
(2) 42.5kg sodium peroxydisulfate and 42.5kg calper calcium peroxide are weighed, 45m is added3Water is made and repairs medicament A aqueous solution;
(3) it weighs 4.25kg iron tourmaline powder and 5m is added in 0.425kg cyclodextrin3Water is made and repairs medicament B aqueous solution.
(4) medicament A aqueous solution will be repaired and repair medicament B aqueous solution and be respectively equally divided into 5 parts;
(5) injection well and pumped well are opened up in trichloro ethylene polluted underground water pollution source area;Start high-pressure pump, injection pressure is 0.5Mpa, injection speed 5L/min, first by 1m3It repairs medicament B aqueous solution and injects the injection well, after the completion of injection, then will 9m3It repairs medicament A aqueous solution and is injected into water injection well, then react 36h;Medicament B aqueous solution, reparation medicament A water are repaired in injection While solution and reaction, polluted underground water is evacuated to from pumped well by injection well with the speed of 5L/min, circulation is formed, makes trichlorine Ethylene polluted underground water comes into full contact with and reacts with reparation medicament A and reparation medicament B.Medicament B is repaired mainly as reparation medicament A's Activator.1.5 meters are divided between the pumped well and injection well.
(6) after the completion of first time circular response, underground water is acquired by pumped well or monitoring well and to trichloro ethylene concentration Detection, and data are recorded, it detects and the data recorded is 45mg/L, water quality is below standard.
(7) step (4)-(6) are repeated, after the completion of second of circular response, simultaneously from pumped well or monitoring well acquisition underground water To trichloro ethylene Concentration Testing, and data are recorded, detects and the data recorded are 25 mg/L, water quality is still below standard.
(8) step (4)-(6) are repeated, after the completion of third time circular response, simultaneously from pumped well or monitoring well acquisition underground water To trichloro ethylene Concentration Testing, and data are recorded, detects and the data recorded are 15 mg/L, water quality is still below standard.
(9) step (4)-(6) are repeated, after the completion of the 4th circular response, simultaneously from pumped well or monitoring well acquisition underground water To trichloro ethylene Concentration Testing, and data are recorded, detects and the data recorded are 5 mg/L, water quality is still below standard.
(10) step (4)-(6) are repeated, after the completion of the 5th circular response, simultaneously from pumped well or monitoring well acquisition underground water To trichloro ethylene Concentration Testing, and data are recorded, detects and the data recorded are 70 μ g/L, water quality reaching standard, repair is complete At.

Claims (11)

1. a kind of in-situ remediation method of trichloro ethylene polluted underground water, which comprises the following steps:
(1) it measures the content of trichloro ethylene in trichloro ethylene polluted underground water and calculates polluted underground water total amount, determine underground water The initial concentration and polluted underground water total amount of middle trichloro ethylene, if trichloro ethylene content is a, polluted underground water total amount in underground water For b;
(2) persulfate and calper calcium peroxide are added to the water, are stirred evenly, be prepared into and repair medicament A aqueous solution, make described repair The content of persulfate is 4a ~ 40a in multiple medicament A aqueous solution, and the content of calper calcium peroxide is 10a ~ 40a, the reparation medicament A of configuration Aqueous solution total amount is 9/10b;
(3) surfactant and iron tourmaline powder are added to the water, are stirred evenly, be prepared into and repair medicament B aqueous solution, make institute The content for repairing surfactant in medicament B aqueous solution stated is 0.05a ~ 5a, and the content of iron tourmaline is 1a ~ 15a, configuration Reparation medicament B aqueous solution total amount is 1/10b;
(4) medicament A aqueous solution will be repaired and repair medicament B aqueous solution and be respectively equally divided into 3 ~ 10 parts, medicament A aqueous solution is repaired and repair Multiple medicament B aqueous solution number is identical;
(5) injection well and pumped well are opened up in trichloro ethylene polluted underground water pollution source area, between the pumped well and injection well It is divided into 1 ~ 3 meter;Start high-pressure pump, portion is first repaired into medicament B aqueous solution and injects the injection well, after the completion of injection, then by one Part repairing medicament A aqueous solution is injected into water injection well, and injection pressure is 0.05 ~ 0.10Mpa, injection speed 5-8L/min, then React 12 ~ 36h;While injection repairs medicament B aqueous solution, repairs medicament A aqueous solution and reaction, three are extracted out from pumped well Vinyl chloride polluted underground water re-injection enters the injection well, and re-injection speed is 5-8L/min;
(6) step (5) after the reaction was completed, acquires underground water by pumped well or monitoring well and to trichloro ethylene Concentration Testing, and Record data;
(7) when trichloro ethylene concentration, which is higher than, repairs target, then repeatedly step (4)-(6);Pollutant concentration is lower than reparation target When, repair is completed.Repairing target preferably uses in " groundwater quality standard " (GB/T 14848-2017) " III class " to mark Quasi- (70 μ g/L).
2. the in-situ remediation method of trichloro ethylene polluted underground water according to claim 1, which is characterized in that the step (2) calper calcium peroxide described in is a nanometer calper calcium peroxide, trichlorine in the calper calcium peroxide solid powder added and underground pollution water The mass ratio of ethylene is 10~40:1.
3. the in-situ remediation method of trichloro ethylene polluted underground water according to claim 2, which is characterized in that added The mass ratio of trichloro ethylene is 20~30:1 in calper calcium peroxide solid powder and underground pollution water.
4. the in-situ remediation method of trichloro ethylene polluted underground water according to claim 1, which is characterized in that the step (2) persulfate described in, can be sodium peroxydisulfate or potassium peroxydisulfate or both mixture, and the persulfate and underground are dirty The mass ratio for contaminating trichloro ethylene in water is 4~40:1.
5. the in-situ remediation method of trichloro ethylene polluted underground water according to claim 1, which is characterized in that the step (2) mass ratio of trichloro ethylene is 1~15:1 in the iron tourmaline and underground pollution water described in.
6. the in-situ remediation method of trichloro ethylene polluted underground water according to claim 1, which is characterized in that the step (2) surfactant described in is cyclodextrin, and the mass ratio of trichloro ethylene is 0.05 in the cyclodextrin and underground pollution water ~5:1.
7. the in-situ remediation method of trichloro ethylene polluted underground water according to claim 1, which is characterized in that the step (2) it is 1:0.25 ~ 10 that the mass ratio of calper calcium peroxide and persulfate in medicament A is repaired in.
8. the in-situ remediation method of trichloro ethylene polluted underground water according to claim 7, which is characterized in that the step (2) it is 1:2.5 that the mass ratio of calper calcium peroxide and persulfate in medicament A is repaired in.
9. the in-situ remediation method of trichloro ethylene polluted underground water according to claim 1, which is characterized in that the step (3) it is 1:1 ~ 750 that the mass ratio of surfactant and iron tourmaline in medicament B is repaired in.
10. the in-situ remediation method of trichloro ethylene polluted underground water according to claim 9, which is characterized in that the step Suddenly it is 1:500 that the mass ratio of surfactant and iron tourmaline in medicament B is repaired in (3).
11. the in-situ remediation method of trichloro ethylene polluted underground water described in any one of -10 according to claim 1, special Sign is that step is divided into 1.5 meters in (5) between pumped well and injection well.
CN201910696338.8A 2019-07-30 2019-07-30 A kind of restorative procedure of trichloro ethylene polluted underground water Pending CN110451628A (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111704226A (en) * 2020-06-03 2020-09-25 中国电建集团中南勘测设计研究院有限公司 Petroleum organic polluted underground water remediation process, remediation system and application
CN111704180A (en) * 2020-06-18 2020-09-25 湖南恒凯环保科技投资有限公司 In-situ injection device and process for strengthening groundwater pollution remediation
CN111760899A (en) * 2020-06-22 2020-10-13 南京农业大学 Feeding improvement method for repairing toxic organic contaminated soil through oxidant compounding oxidation

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101428906A (en) * 2008-12-12 2009-05-13 天津大学 System and method for restoring triclene polluted groundwater
CN104071886A (en) * 2014-07-01 2014-10-01 中节能大地环境修复有限公司 Preparation method and application of self-activated persulfate oxidized medicament
CN104445570A (en) * 2014-10-22 2015-03-25 同济大学 Method for removing polycyclic aromatic hydrocarbon methylnaphthalene substance by adopting double oxidants including persulfate and calcium peroxide
CN104475440A (en) * 2014-12-04 2015-04-01 唐山柯林环保科技有限公司 In-situ remediation method of chromium pollution site and special water treatment equipment
WO2016090074A1 (en) * 2014-12-05 2016-06-09 Washington State University Destruction of dense nonaqueous phase liquids (dnapls) using a time-release formulation
CN108046404A (en) * 2017-12-20 2018-05-18 浙江省环境保护科学设计研究院 A kind of in situ chemical oxidation restorative procedure of organic pollution underground water
CN108160693A (en) * 2017-12-26 2018-06-15 北京宜为凯姆环境技术有限公司 For the persulfate combined heat activation method of environment remediation
CN108640250A (en) * 2018-04-19 2018-10-12 济南大学 A kind of method that calper calcium peroxide-sodium peroxydisulfate dual oxidants remove 2,4- Dichlorophenols in water removal

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101428906A (en) * 2008-12-12 2009-05-13 天津大学 System and method for restoring triclene polluted groundwater
CN104071886A (en) * 2014-07-01 2014-10-01 中节能大地环境修复有限公司 Preparation method and application of self-activated persulfate oxidized medicament
CN104445570A (en) * 2014-10-22 2015-03-25 同济大学 Method for removing polycyclic aromatic hydrocarbon methylnaphthalene substance by adopting double oxidants including persulfate and calcium peroxide
CN104475440A (en) * 2014-12-04 2015-04-01 唐山柯林环保科技有限公司 In-situ remediation method of chromium pollution site and special water treatment equipment
WO2016090074A1 (en) * 2014-12-05 2016-06-09 Washington State University Destruction of dense nonaqueous phase liquids (dnapls) using a time-release formulation
CN108046404A (en) * 2017-12-20 2018-05-18 浙江省环境保护科学设计研究院 A kind of in situ chemical oxidation restorative procedure of organic pollution underground water
CN108160693A (en) * 2017-12-26 2018-06-15 北京宜为凯姆环境技术有限公司 For the persulfate combined heat activation method of environment remediation
CN108640250A (en) * 2018-04-19 2018-10-12 济南大学 A kind of method that calper calcium peroxide-sodium peroxydisulfate dual oxidants remove 2,4- Dichlorophenols in water removal

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
王航: "《电气石催化过硫酸盐降解染料废水》", 《中国优秀硕士学位论文全文数据库 工程科技Ⅰ辑》 *
第五届功能性纺织品及纳米技术应用研讨会论文集组委会: "《第五届功能性纺织品及纳米技术应用研讨会论文集》", 31 December 2005 *
邹洪涛等: "《环境化学》", 31 December 2011, 暨南大学出版社 *

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111704226A (en) * 2020-06-03 2020-09-25 中国电建集团中南勘测设计研究院有限公司 Petroleum organic polluted underground water remediation process, remediation system and application
CN111704226B (en) * 2020-06-03 2022-10-25 中国电建集团中南勘测设计研究院有限公司 Petroleum organic polluted underground water remediation process, remediation system and application
CN111704180A (en) * 2020-06-18 2020-09-25 湖南恒凯环保科技投资有限公司 In-situ injection device and process for strengthening groundwater pollution remediation
CN111704180B (en) * 2020-06-18 2021-06-22 湖南恒凯环保科技投资有限公司 In-situ injection device and process for strengthening groundwater pollution remediation
CN111760899A (en) * 2020-06-22 2020-10-13 南京农业大学 Feeding improvement method for repairing toxic organic contaminated soil through oxidant compounding oxidation
CN111760899B (en) * 2020-06-22 2021-08-24 南京农业大学 Feeding improvement method for repairing toxic organic contaminated soil through oxidant compounding oxidation

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