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Guide,
Dr. Vinish V. Nair
Associate Professor
Dept. Of Civil Engineering
VIJAI KRISHNAN V.
S7 CE
ROLL NO.: 58
Govt. RIT,Kottayam, KERALA
INTRODUCTION
 EKR is most efficient green technology to remove heavy metals
from soil by using low volt DC
 Heavy metals – group of metals or metalloids with atomic
density > 5 g/cm3
 Fe, Mn, Zn, Cu, Ni, Cd, Cr, Co, Hg, As etc…
 Non-biodegradable & persistent
 Affect quality of soil & water
 Stored by plants & crops
 Intake leads to health hazards - toxic, carcinogenic
 Use in US & Europe
How soil is contaminated?
 Rapid industrialization & urbanization
 Open dumping & landfills
 Mining, manufacture & use of synthetic products
 Waste-water & municipal sludge
 Change in life style
 Military & volcanic areas
 Pesticides & Fertilizers
Heavy metal
contamination at
Bagacay copper
mines, Philippines
Scenario in world & India
REF : European Environment Agency, 2015
Contaminants affecting soil matrix in Europe (2011)
Metal Surat
Pali,
Rajasthan Thane Chennai
Max limit in Soil
(mg/kg)
US-EPA Dutch
Standar
ds
Arsenic (As) - - - - 14 29
Selenium (Se) - - - - 1.6 0.7
Nickel (Ni) 79.0 - 183.6 78.8 32 35
Cobalt (Co) 51.3 - 68.7 - 20 9
Cadmium (Cd) - - - - 1.6 0.8
Chromium(Cr) 305.2 240.0 521.3 418.0 120 100
Copper (Cu) 137.5 298.0 104.6 372.0 100 36
Lead (Pb) - 293.0 - - 60 85
Mercury (Hg) - - - - 0.5 0.3
Zinc (Zn) 139.0 1,364.0 191.3 213.6 220 140
REF : Int. J. Electrochem. Sci. 2011, SPRINGER 2006, Researchgate 2005
Contamination in India
• Site Investigation
• Contaminants-type, depth,
concentration
Stages in Soil Remediation
Risk
assessment
Feasible
remediation
options
Verification
Design &
Implementation
Monitoring &
maintenance
• Solidification
• Soil washing
• Vitrification
• Isolation
•Bio-remediation
• Coagulation
• Flotation
• Electro-kinetic
remediation
• Type & Spacing of electrodes
• Electrolyte, Voltage gradient
•Period of operation
Lab test – removal
efficiency, economy
Why Electro-kinetic Remediation?
 Suitable for low permeability soils
 Faster remediation
 Efficient & applicable to wide range of heavy metals
 In-situ & ex-situ method
 Remove radio nucleotides, organic & inorganic contaminants
 Low cost
Electro-kinetic Remediation
 Consist of 4 parts
i). Electrode compartment - graphite, platinum
ii). Electrolytic solution reservoir
iii). Power supply unit – DC, Solar cell, Pulse current
iv). Soil cell
 Processes in EKR :-
i). Electro-osmosis
ii). Electro-migration
iii). Electrophoresis
 Electro-osmosis
 Movement of water molecules
 Flow towards cathode
 Electro-migration
 Transport of ions to opposite charged electrode
 Major transport of metal ions
 Electrophoresis
 Transport of charged colloidal particles
 Negligible in low permeable soil
Laboratory Setup – Chromium removal
 Sample is contaminated by Potassium Chromate solution
 Cr(VI) commonly exist in anionic form
 After 24hrs contaminated soil is compacted in HDPE container
 Electrodes – slotted graphite
 Electrolyte – potable water
 Voltage gradient – 1 Volt DC/cm
REF: Journal Of Environmental Engineering, ASCE 2004
 Electrolysis of water  At anode : 2H20 O2 + 4H+ + 4e-
At cathode : 4H2O + 4e-  2H2 + 4OH-
 H+ move from anode to cathode ( acidic front )
 OH- from cathode to anode ( basic front )
 Acidic front mobilize metal ions  Electro-migration occurs
 Cr(VI) migrate to anode ( + ) & precipitated
 Exhausted electrolyte stored in reservoir
 Concentration of Cr is determined by Atomic Absorption
Spectrometer
 Removal efficiency is low
 Enhancing agents are added & test is repeated
Enhancing Agent Removal Efficiency
EDTA 45 %
Acetic acid 57 %
Sulfuric acid 73 %
NaCl & EDTA 79 %
Citric acid 82 %
Enhancing Agents & Removal
Efficiency
Electrokinetic Remediation Field Setup
 Well is constructed
 Filling electrolyte
 Inserting Anode (+) &
Cathode ( - )
 Applying electric field
 Electro-osmosis &
Electrolysis of water
 Desorption of metal ion by acidic front
 Electro-migration & precipitation or dissolution of metal ion
 Pumping & storing of exhausted electrolyte
 Avg Spacing b/w anode & cathode – 14 ft
 Avg Spacing b/w anodes or Cathodes – 7 ft
 Vary depending on level of contamination & remediation time
How to improve removal efficiency?
 Use of enhancing agents :-
 EDTA, NTA, acetic acid, citric acid, NaOH, NaCl etc…
 Form complexes with metal ions  easy removal
 Ion selective membrane around electrodes Electrodialytic
remediation
 Use of pulse current
 Using combined EK technologies-EKR with Ultrasonics
 EKR remove metal
 Ultrasonic removes organic matter
 Removal efficiency for Pb increase up to 91%
 Making consistency of soil equal to liquid limit
Case Study
A. US Army Waterway Experiment Station, Louisiana
 Electrokinetics Inc.
 Electro-Klean Electrical Separation process
 Lead – avg removal efficiency -85%
B. Old TNX Basin, South Carolina
 Isotron Corporation
 Electrosorb process
 Mercury, Lead, Chrome
C. Sandia National Laboratories Chemical Waste Landfill
 Chromium
 Supported by US Dept of Energy
REF : US-EPA, 1995
Problems
 Insoluble organic matter & stable compound reduce removal
efficiency
 Polluting metal species is high  very slow remediation
 Buried metal objects  short circuiting, waste of current
 Careful design
 Success depends on :-
 Soil type
 Soil pH  high pH ( >10 ), lower removal efficiency
 Applied electric field
 Presence of carbonate
 Concentration of target metal ion
Installation of
electrode in site
Electrodes installed
at site
Conclusion
 Industrial effluent increase heavy metal contaminants
 Heavy metals cause several health hazards
 In-situ technique  minimum surface disturbance
 EKR - High removal efficiency upto 90%
 Suitable for any depth
 High level of sustainability, social acceptability & economic
performance
 Used commercially in Europe, USA
 Necessary to keep environment safe & healthy
References
1. US-EPA (1995), “Insitu remediation technology: Electrokinetics”
2. InterstateTechnology & Regulatory Council ( 2010 ), “Technology Overview-Electrokinetics”
3. Krishna R. Reddy & Supraja Chinthamreddy ( 2004 ), “Enhanced Electrokinetic Remediation
of Heavy Metals in Glacial Till Soil Using Different Electrolyte Solutions”, ASCE
4. Riffat Naseem Malik, Syed Zahoor Husain & Ishfaq Nazir ( 2015 ), “Heavy Metal
Contamination And Accumulation In Soil And Wild Plant Species From Industrial Area Of
Islamabad, Pakistan”, ResearchGate
5. P.K.Govil, J.E.Sorlie, N. N. Murthy, D. Sujatha, G.L.N.Reddy, Kim Rudolph-Lund,
A.K.Krishna & K.Rama Mohan (2007 ) “Soil contamination of heavy metals in the Katedan
Industrial Development Area, Hyderabad, India”, Springer
6. A.K.Krishna, P.K.Govil (2007), “Soil contamination due to heavy metals from an industrial
area of Surat, Gujarat”, Springer
7. A.K.Krishna, P.K.Govil (2004),“Heavy metal contamination of soil around Pali Industrial
Area,Rajasthan, India”,Springer
8. Burlakovs Juris, Stankevica Karina, Hassan Ikrema, Janovskis Reinis, Lacis Sandris,
“Removal Of Heavy Metals From Contaminated Soils By Elektrokinetic Remediation”
9. US Army Environmental Center ( 2000 ), “In-Situ Electrokinetic Remediation of Metal
Contaminated Soils Technology Status Report”
10. European Environment Agency (2007,2015), “Progress in management of contaminated sites”
11. Shweta .S. Angadi, Rashma Shetty , Manjunath N.T. (2015), “Coagulation Study to Remove
Heavy Metals from Leachate”, IJIRSET
12. J.Aruna, Dr.B.Naga Malleswara Rao (2015), “Remediation of Heavy Metal Contaminated Soils”,
IJIRSET
13. Rageena S.S., Rani V. (2015), “Effect of Various Pore Fluids on Free Swell and Shrinkage
Cracking of Clays”, IJIRSET
14. Jaishree, T.I.Khan,(2015), “Assessment of Heavy Metals’ Risk on Human Health via Dietary
Intake of Cereals and Vegetables from Effluent Irrigated Land Jaipur District, Rajasthan”,
IJIRSET
15. Sruthy O A and S Jayalekshmi (2014), “Electrokinetic Remediation Of Heavy Metal
Contaminated Soil”, IJSCER
16. Okeke P. N. (2013), “Enhanced Electrokinetic Remediation of Cadmium Contaminated Soil “,
An Int. Journal of Sci. and Tech.
 Potassium chromate, Nickel chloride,Cadmium chloride
 Ion selective membrane-prevent entry of ions generated at electrode to soil
 Pulse current
A unidirectional surge of current of very short duration. It quickly rises to a maximum, then
drops to zero in a similar fashion
 EDTA – ethylene di amine tetra acetic acid-Form soluble complexes with Cr
 NTA – nitrilo tri acetic acid
 DTPA- di ethylene tri amine penta acetic acid
 Chelating agents – form several bonds to a single metal ion
 DC volt 20-30 V
 Diseases : - gastro intestinal disorders, diarrhoea , tremor, paralysis, vomiting,depression,
pneumonia
 Nuerotoxic,mutagenic
 Coagulation – alum + polyelectrolyte ( FeCl3)
 Electrode – carbon,platinum,graphite – cylindrical – inert –no residue
Pb Cd Cu Cr
* EDTA,DTPA •NTA (65-95%)
•H2SO4 soln (76 %)
* Battery &
electronics
* DTPA ( 60 %) * Citric acid>acetic
acid
 Cd – Ni-Cd battery, alloys, paints, ink catridge
 Zn- galvanizing
 Vitrification
 Soil is heated at high temp ~ 2000 C.Organic pollutants are volatalized, heavy metals are
retained in soil.Melted soil forms a solid block
 Dist b/w anode or cathode 7ft, b/w anode & cathode 14 ft ( US army
environment center)
 EKR field projects are funded & carried out in USA (by USEPA, ITRC, US army
Envt. Centre, Electropetroleum Inc., Terran Corporation, General electric) ,
Europe(Geokinetics International Inc.), Japan, Korea.
 Cost <100 $/cub m to >400 $/cub m ( site specific )
 Effect of pore fluid :-
 Increase in conc of NaCl, NH4Cl, Acetic acid to clay decrease free swell but
NaOH increases free swell.Affects crack behavoir
 Electrosorb process – contaminants are adsorbed to electrode
 Pesticides & fertilizer - Cd & Pb
 Micronutrients - Fe, Mn, Zn, Cu, Ni
 Fines & closure notice – India
 Potassium & sodium bichromate industry, gujarat
 Dyeing units, Tirupur,TN
 Steel industry, Kalmeshwar, Maharashtra
 Heavy metal contamination in Kerala –
 Kerala Minerals & Metals Ltd, Kollam – Lead & mercury ( perimeter of 500 m ) –
NDTV & KIMS
 Eloor & edayar industrial develpmt area- HIL,Grasim Indstrys, Merchem Limited
and FACT ( Zn,Pb,Cd,Hg,Cr ) closed all units (2004-05)
 KINFRA Textile Industries, Kannur – Zn,As,Pb
 Kerala Clay & Ceramics Ltd,Kannur – closed due > Fe in water
Enhancing agents
 EDTA Enhancement
 At Cathode – EDTA
 Form soluble complexes with Cr
 Removal efficiency 45%
 Acetic Acid Enhancement
 At Cathode – acetic acid
 Increase solubility of metal ion
 Removal efficiency 57%
 Citric Acid Enhancement
 Cathode – citric acid
 Electro-migration to anode is
more
 Chromium citrate complexes are
formed
 Removal efficiency 82%
 NaCl & EDTA Enhancement
 Anode – NaCl & Cathode – EDTA
 NaCl sustain high current &
electro-osmosis
 Removal efficiency 79%
 Sulfuric Acid Enhancement
 Greater electro-migration &
solubility
 Removal efficiency 73%

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Electrokinetic Remediation of Heavy Metal contaminated soil

  • 1. Guide, Dr. Vinish V. Nair Associate Professor Dept. Of Civil Engineering VIJAI KRISHNAN V. S7 CE ROLL NO.: 58 Govt. RIT,Kottayam, KERALA
  • 2. INTRODUCTION  EKR is most efficient green technology to remove heavy metals from soil by using low volt DC  Heavy metals – group of metals or metalloids with atomic density > 5 g/cm3  Fe, Mn, Zn, Cu, Ni, Cd, Cr, Co, Hg, As etc…  Non-biodegradable & persistent  Affect quality of soil & water  Stored by plants & crops  Intake leads to health hazards - toxic, carcinogenic  Use in US & Europe
  • 3. How soil is contaminated?
  • 4.  Rapid industrialization & urbanization  Open dumping & landfills  Mining, manufacture & use of synthetic products  Waste-water & municipal sludge  Change in life style  Military & volcanic areas  Pesticides & Fertilizers Heavy metal contamination at Bagacay copper mines, Philippines
  • 5. Scenario in world & India REF : European Environment Agency, 2015 Contaminants affecting soil matrix in Europe (2011)
  • 6. Metal Surat Pali, Rajasthan Thane Chennai Max limit in Soil (mg/kg) US-EPA Dutch Standar ds Arsenic (As) - - - - 14 29 Selenium (Se) - - - - 1.6 0.7 Nickel (Ni) 79.0 - 183.6 78.8 32 35 Cobalt (Co) 51.3 - 68.7 - 20 9 Cadmium (Cd) - - - - 1.6 0.8 Chromium(Cr) 305.2 240.0 521.3 418.0 120 100 Copper (Cu) 137.5 298.0 104.6 372.0 100 36 Lead (Pb) - 293.0 - - 60 85 Mercury (Hg) - - - - 0.5 0.3 Zinc (Zn) 139.0 1,364.0 191.3 213.6 220 140 REF : Int. J. Electrochem. Sci. 2011, SPRINGER 2006, Researchgate 2005 Contamination in India
  • 7. • Site Investigation • Contaminants-type, depth, concentration Stages in Soil Remediation Risk assessment Feasible remediation options Verification Design & Implementation Monitoring & maintenance • Solidification • Soil washing • Vitrification • Isolation •Bio-remediation • Coagulation • Flotation • Electro-kinetic remediation • Type & Spacing of electrodes • Electrolyte, Voltage gradient •Period of operation Lab test – removal efficiency, economy
  • 8. Why Electro-kinetic Remediation?  Suitable for low permeability soils  Faster remediation  Efficient & applicable to wide range of heavy metals  In-situ & ex-situ method  Remove radio nucleotides, organic & inorganic contaminants  Low cost
  • 9. Electro-kinetic Remediation  Consist of 4 parts i). Electrode compartment - graphite, platinum ii). Electrolytic solution reservoir iii). Power supply unit – DC, Solar cell, Pulse current iv). Soil cell  Processes in EKR :- i). Electro-osmosis ii). Electro-migration iii). Electrophoresis
  • 10.  Electro-osmosis  Movement of water molecules  Flow towards cathode  Electro-migration  Transport of ions to opposite charged electrode  Major transport of metal ions  Electrophoresis  Transport of charged colloidal particles  Negligible in low permeable soil
  • 11. Laboratory Setup – Chromium removal  Sample is contaminated by Potassium Chromate solution  Cr(VI) commonly exist in anionic form  After 24hrs contaminated soil is compacted in HDPE container  Electrodes – slotted graphite  Electrolyte – potable water  Voltage gradient – 1 Volt DC/cm REF: Journal Of Environmental Engineering, ASCE 2004
  • 12.  Electrolysis of water  At anode : 2H20 O2 + 4H+ + 4e- At cathode : 4H2O + 4e-  2H2 + 4OH-  H+ move from anode to cathode ( acidic front )  OH- from cathode to anode ( basic front )  Acidic front mobilize metal ions  Electro-migration occurs  Cr(VI) migrate to anode ( + ) & precipitated  Exhausted electrolyte stored in reservoir  Concentration of Cr is determined by Atomic Absorption Spectrometer  Removal efficiency is low  Enhancing agents are added & test is repeated
  • 13. Enhancing Agent Removal Efficiency EDTA 45 % Acetic acid 57 % Sulfuric acid 73 % NaCl & EDTA 79 % Citric acid 82 % Enhancing Agents & Removal Efficiency
  • 14. Electrokinetic Remediation Field Setup  Well is constructed  Filling electrolyte  Inserting Anode (+) & Cathode ( - )  Applying electric field  Electro-osmosis & Electrolysis of water  Desorption of metal ion by acidic front  Electro-migration & precipitation or dissolution of metal ion  Pumping & storing of exhausted electrolyte
  • 15.  Avg Spacing b/w anode & cathode – 14 ft  Avg Spacing b/w anodes or Cathodes – 7 ft  Vary depending on level of contamination & remediation time
  • 16. How to improve removal efficiency?  Use of enhancing agents :-  EDTA, NTA, acetic acid, citric acid, NaOH, NaCl etc…  Form complexes with metal ions  easy removal  Ion selective membrane around electrodes Electrodialytic remediation  Use of pulse current  Using combined EK technologies-EKR with Ultrasonics  EKR remove metal  Ultrasonic removes organic matter  Removal efficiency for Pb increase up to 91%  Making consistency of soil equal to liquid limit
  • 17. Case Study A. US Army Waterway Experiment Station, Louisiana  Electrokinetics Inc.  Electro-Klean Electrical Separation process  Lead – avg removal efficiency -85% B. Old TNX Basin, South Carolina  Isotron Corporation  Electrosorb process  Mercury, Lead, Chrome C. Sandia National Laboratories Chemical Waste Landfill  Chromium  Supported by US Dept of Energy REF : US-EPA, 1995
  • 18. Problems  Insoluble organic matter & stable compound reduce removal efficiency  Polluting metal species is high  very slow remediation  Buried metal objects  short circuiting, waste of current  Careful design  Success depends on :-  Soil type  Soil pH  high pH ( >10 ), lower removal efficiency  Applied electric field  Presence of carbonate  Concentration of target metal ion
  • 19. Installation of electrode in site Electrodes installed at site
  • 20. Conclusion  Industrial effluent increase heavy metal contaminants  Heavy metals cause several health hazards  In-situ technique  minimum surface disturbance  EKR - High removal efficiency upto 90%  Suitable for any depth  High level of sustainability, social acceptability & economic performance  Used commercially in Europe, USA  Necessary to keep environment safe & healthy
  • 21. References 1. US-EPA (1995), “Insitu remediation technology: Electrokinetics” 2. InterstateTechnology & Regulatory Council ( 2010 ), “Technology Overview-Electrokinetics” 3. Krishna R. Reddy & Supraja Chinthamreddy ( 2004 ), “Enhanced Electrokinetic Remediation of Heavy Metals in Glacial Till Soil Using Different Electrolyte Solutions”, ASCE 4. Riffat Naseem Malik, Syed Zahoor Husain & Ishfaq Nazir ( 2015 ), “Heavy Metal Contamination And Accumulation In Soil And Wild Plant Species From Industrial Area Of Islamabad, Pakistan”, ResearchGate 5. P.K.Govil, J.E.Sorlie, N. N. Murthy, D. Sujatha, G.L.N.Reddy, Kim Rudolph-Lund, A.K.Krishna & K.Rama Mohan (2007 ) “Soil contamination of heavy metals in the Katedan Industrial Development Area, Hyderabad, India”, Springer 6. A.K.Krishna, P.K.Govil (2007), “Soil contamination due to heavy metals from an industrial area of Surat, Gujarat”, Springer 7. A.K.Krishna, P.K.Govil (2004),“Heavy metal contamination of soil around Pali Industrial Area,Rajasthan, India”,Springer 8. Burlakovs Juris, Stankevica Karina, Hassan Ikrema, Janovskis Reinis, Lacis Sandris, “Removal Of Heavy Metals From Contaminated Soils By Elektrokinetic Remediation” 9. US Army Environmental Center ( 2000 ), “In-Situ Electrokinetic Remediation of Metal Contaminated Soils Technology Status Report”
  • 22. 10. European Environment Agency (2007,2015), “Progress in management of contaminated sites” 11. Shweta .S. Angadi, Rashma Shetty , Manjunath N.T. (2015), “Coagulation Study to Remove Heavy Metals from Leachate”, IJIRSET 12. J.Aruna, Dr.B.Naga Malleswara Rao (2015), “Remediation of Heavy Metal Contaminated Soils”, IJIRSET 13. Rageena S.S., Rani V. (2015), “Effect of Various Pore Fluids on Free Swell and Shrinkage Cracking of Clays”, IJIRSET 14. Jaishree, T.I.Khan,(2015), “Assessment of Heavy Metals’ Risk on Human Health via Dietary Intake of Cereals and Vegetables from Effluent Irrigated Land Jaipur District, Rajasthan”, IJIRSET 15. Sruthy O A and S Jayalekshmi (2014), “Electrokinetic Remediation Of Heavy Metal Contaminated Soil”, IJSCER 16. Okeke P. N. (2013), “Enhanced Electrokinetic Remediation of Cadmium Contaminated Soil “, An Int. Journal of Sci. and Tech.
  • 23.
  • 24.  Potassium chromate, Nickel chloride,Cadmium chloride  Ion selective membrane-prevent entry of ions generated at electrode to soil  Pulse current A unidirectional surge of current of very short duration. It quickly rises to a maximum, then drops to zero in a similar fashion  EDTA – ethylene di amine tetra acetic acid-Form soluble complexes with Cr  NTA – nitrilo tri acetic acid  DTPA- di ethylene tri amine penta acetic acid  Chelating agents – form several bonds to a single metal ion  DC volt 20-30 V  Diseases : - gastro intestinal disorders, diarrhoea , tremor, paralysis, vomiting,depression, pneumonia  Nuerotoxic,mutagenic  Coagulation – alum + polyelectrolyte ( FeCl3)  Electrode – carbon,platinum,graphite – cylindrical – inert –no residue Pb Cd Cu Cr * EDTA,DTPA •NTA (65-95%) •H2SO4 soln (76 %) * Battery & electronics * DTPA ( 60 %) * Citric acid>acetic acid
  • 25.  Cd – Ni-Cd battery, alloys, paints, ink catridge  Zn- galvanizing  Vitrification  Soil is heated at high temp ~ 2000 C.Organic pollutants are volatalized, heavy metals are retained in soil.Melted soil forms a solid block  Dist b/w anode or cathode 7ft, b/w anode & cathode 14 ft ( US army environment center)  EKR field projects are funded & carried out in USA (by USEPA, ITRC, US army Envt. Centre, Electropetroleum Inc., Terran Corporation, General electric) , Europe(Geokinetics International Inc.), Japan, Korea.  Cost <100 $/cub m to >400 $/cub m ( site specific )  Effect of pore fluid :-  Increase in conc of NaCl, NH4Cl, Acetic acid to clay decrease free swell but NaOH increases free swell.Affects crack behavoir  Electrosorb process – contaminants are adsorbed to electrode  Pesticides & fertilizer - Cd & Pb  Micronutrients - Fe, Mn, Zn, Cu, Ni
  • 26.  Fines & closure notice – India  Potassium & sodium bichromate industry, gujarat  Dyeing units, Tirupur,TN  Steel industry, Kalmeshwar, Maharashtra  Heavy metal contamination in Kerala –  Kerala Minerals & Metals Ltd, Kollam – Lead & mercury ( perimeter of 500 m ) – NDTV & KIMS  Eloor & edayar industrial develpmt area- HIL,Grasim Indstrys, Merchem Limited and FACT ( Zn,Pb,Cd,Hg,Cr ) closed all units (2004-05)  KINFRA Textile Industries, Kannur – Zn,As,Pb  Kerala Clay & Ceramics Ltd,Kannur – closed due > Fe in water
  • 27. Enhancing agents  EDTA Enhancement  At Cathode – EDTA  Form soluble complexes with Cr  Removal efficiency 45%  Acetic Acid Enhancement  At Cathode – acetic acid  Increase solubility of metal ion  Removal efficiency 57%  Citric Acid Enhancement  Cathode – citric acid  Electro-migration to anode is more  Chromium citrate complexes are formed  Removal efficiency 82%  NaCl & EDTA Enhancement  Anode – NaCl & Cathode – EDTA  NaCl sustain high current & electro-osmosis  Removal efficiency 79%  Sulfuric Acid Enhancement  Greater electro-migration & solubility  Removal efficiency 73%