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Degradation of aniline by mediated electrochemical 
Oxidation (MEO) process 
Vladimir Bobrov, Sang Joon Chung, S. Balaji & Il Shik Moon* (Dept. of Chemical Engineering, Sunchon National University) 
Clean Technology Pilot Laboratory 
Sunchon National University
Introduction 
Offers attractive route for the destruction of organic pollutants 
Metallic ion in the oxidized form in an acid acts as a mediator 
Mediator ion will oxidize organic pollutants into CO2and H2O 
Metallic ion constantly undergoing oxidation and reduction 
Major byproducts are CO2and H2O 
Highlights of Mediated Electrochemical Oxidation (MEO) 
Aniline as Target Organic Pollutant 
Aniline is a major by-product in petro-chemical and coal-tar 
industries 
Aniline will polymerize into more toxic poly aniline if not removed 
Clean Technology Pilot Laboratory 
Sunchon National University
Mediated Electrochemical Oxidation(MEO) 
AnodeRegeneration of Ce4+ Ce3+→ Ce4++ e- 
Oxidation Reaction 
Ce4++ Organics → Ce3++ CO2+ InorganicsOxidationCe4+ 
Reduction 
Ce3+ 
Organics 
Inorganics, CO2 
e- 
Clean Technology Pilot Laboratory 
Sunchon National University
Object of this study 
•To Apply MEO Technology to Analyze the Destruction of High Concentrations of Aniline, under different solution temperatures 
•To evaluate the pattern of redox potential and CO2generation, during the destruction of aniline 
•To compare the theoretical and experimental values of Ce(IV) requirement for aniline destruction 
Clean Technology Pilot Laboratory 
Sunchon National University
Experimental 
Fig. 1. Schematic of MEO Process Clean Technology Pilot LaboratorySunchon National UniversityMEO SolutionTank 
Silyine Pump 
Reactor 
Pt Electrode 
Scrubber 
CO2Analyzer 
Multi-Meter 
N2Cylinder
Experimental 
Analysis 
Estimation of this study 
Ce3+/Ce4+redox potential in anolyte solution 
Estimating the amount of CO2in the off-gas 
Measurement of Ce3+/Ce4+redox potential 
-Pt-Ag/AgCl combined electrode 
-pH/ORP meter(Orion, model 720A) 
Measurement of degradation of Aniline 
-CO2analyzer(Environmental Instruments, Anagas CD 95) 
C6H7N+12H2O+28Ce(IV)6CO2+27H++NH4+28Ce(III) 
Clean Technology Pilot Laboratory 
Sunchon National University
Results & Discussion 
Fig. 2. Evolution of CO2 during the degradation of 600ppm aniline at 70℃ 
(Theoretical Total Volume of CO2 for Complete degradation of Aniline = 232 ml) 
0 
1000 
2000 
3000 
4000 
5000 
6000 
7000 
8000 
9000 
0 20 40 60 80 100 
Reaction Time(min) 
Concentration of CO2(ppm) 
0 
20 
40 
60 
80 
100 
120 
140 
Cumulative Volume of CO2(ml) 
Clean Technology Pilot Laboratory 
Sunchon National University
Results & Discussion 
0 
1000 
2000 
3000 
4000 
5000 
6000 
7000 
8000 
9000 
0 20 40 60 80 100 
Reaction TIme(min) 
Concentration of CO2(ppm) 
-50 
0 
50 
100 
150 
200 
250 
Cumulative Volume of CO2(ml) 
Fig. 3. Evolution of CO2 during the degradation of 600ppm aniline at 80℃ 
(Theoretical Total Volume of CO2 for Complete degradation of Aniline = 232 ml) 
Clean Technology Pilot Laboratory 
Sunchon National University
Results & Discussion 
Fig. 4. Evolution of CO2 during the degradation of 600ppm aniline at 90℃ 
0 
2000 
4000 
6000 
8000 
10000 
12000 
14000 
16000 
18000 
0 10 20 30 40 50 60 70 80 90 100 
Reaction Time(min0 
Concentration of CO2(ppm) 
0 
50 
100 
150 
200 
250 
Cumulative Volume of 
CO2(ml) 
CO2 Theory 100% destruction of aniline (600 ppm) 232 ml CO2 
EXPRIMENT 98% destruction of aniline (600 ppm) 227 ml CO2 
C6H7N + 12 H2O + 28 Ce(IV)  6 CO2 + 27 H+ + NH4 + 28 Ce(III) 
Clean Technology Pilot Laboratory 
Sunchon National University
Results & Discussion 
Fig. 5. Redox potential and Ce(IV) concentration under the degradation 
of 600ppm aniline at 90℃ 
1460 
1470 
1480 
1490 
1500 
1510 
1520 
0 50 100 150 200 
Time, min 
Redox Potential, 
mV 
0.7 
0.75 
0.8 
0.85 
0.9 
0.95 
1 
Ce(IV), M 
Redox,mV 
Ce(IV), M 
Ce(IV) Theory 100% destruction of aniline (600 ppm) 0.18 M Ce(IV) 
EXPERIMENT 98% destruction of aniline (600 ppm) 0.16 M Ce(IV) 
For Theoretical Value for multi-electron coefficient degradation of aniline: 
Molar concentration of Ce(IV) / Molar Concentration of Aniline n=28 
Clean Technology Pilot Laboratory 
Sunchon National University
Results & Discussion 
0 
10 
20 
30 
40 
50 
60 
70 
80 
90 
100 
0 30 60 90 120 150 180 210 
Reaction Time(min) 
Degradation of Aniline(%) 
70℃ 
80℃ 
90℃ 
Fig. 6. The degradation of 600ppm aniline at different temperatures 
Clean Technology Pilot Laboratory 
Sunchon National University
Results & Discussion 
0 
2000 
4000 
6000 
8000 
10000 
12000 
14000 
0 10 20 30 40 50 60 70 80 90 100 
Reaction Time(min) 
Concentration of CO2(ppm) 
0 
50 
100 
150 
200 
250 
Cumulative Volume of CO2(ml) 
Fig. 7. Evolution of CO2 during the degradation of 1080ppm aniline at 70℃ 
Clean Technology Pilot Laboratory 
Sunchon National University
Results & Discussion 
0 
5000 
10000 
15000 
20000 
25000 
0 10 20 30 40 50 60 70 80 90 100 
Reaction Time(min) 
Concentration of CO 2(ppm) 
0 
50 
100 
150 
200 
250 
300 
350 
400 
Cumulative Volume of CO 2(ml) 
Fig. 8. Evolution of CO2 during the degradation of 1200ppm aniline at 80℃ 
Clean Technology Pilot Laboratory 
Sunchon National University
Results & Discussion 
Fig. 9. Evolution of CO2 during the degradation of 1200ppm aniline at 90℃ 
0 
5000 
10000 
15000 
20000 
25000 
30000 
0 10 20 30 40 50 60 70 80 90 100 
Reaction Time(min) 
Concentration of CO2(ppm) 
0 
50 
100 
150 
200 
250 
300 
350 
400 
450 
500 
Cumulative Volume of 
CO2(ml) 
CO2 Theory 100% destruction of aniline (600 ppm) 464 ml CO2 
EXPRIMENT 93% destruction of aniline (600 ppm) 430 ml CO2 
C6H7N + 12 H2O + 28 Ce(IV)  6 CO2 + 27 H+ + NH4 + 28 Ce(III) 
Clean Technology Pilot Laboratory 
Sunchon National University
Results & Discussion 
Fig. 10 Redox potential and Ce(IV) concentration under the degradation of 1200 ppm aniline 
at 90℃ 
Ce(IV) Theory 100% destruction of aniline (600 ppm) 0.36 M Ce(IV) 
EXPERIMENT 98% destruction of aniline (600 ppm) 0.35 M Ce(IV) 
For Theoretical Value for multi-electron coefficient degradation of aniline: 
Molar concentration of Ce(IV) / Molar Concentration of Aniline n=28 
1440 
1450 
1460 
1470 
1480 
1490 
1500 
1510 
1520 
1530 
0 50 100 150 200 250 
Time, min 
Redox, mV 
0.6 
0.65 
0.7 
0.75 
0.8 
0.85 
0.9 
0.95 
1 
Ce(IV), M 
Redox,mv 
Ce(IV), M 
Clean Technology Pilot Laboratory 
Sunchon National University
Results & Discussion 
0 
10 
20 
30 
40 
50 
60 
70 
80 
90 
100 
0 50 100 150 200 250 
Reaction Time(min) 
Degradation of Aniline(%) 
70℃ 
80℃ 
90℃ 
Fig. 11. The degradation of 1200ppm aniline at different temperatures 
Clean Technology Pilot Laboratory 
Sunchon National University
Results & Discussion 
Fig. 12. The degradation of 2400 aniline at temperature 90℃ in flow reactor. 
(Flow Rate of MEO solution = 2 ml/min, flow Aniline solution = 10 ml/h, 
volume of reactor = 120 ml) 
2400 ppm Aniline 
0 
1000 
2000 
3000 
4000 
5000 
6000 
0 20 40 60 80 
min 
CO2, ppm 
CO2,ppm 
Temp, deg C 
Clean Technology Pilot Laboratory 
Sunchon National University
Results & Discussion 
Fig. 13. The degradation of 1200 aniline at temperature 90℃ in flow reactor. 
(Flow MEO solution = 2 ml/min, flow Aniline solution = 5 ml/h, 
volume of reactor = 120 ml ) 
Aniline 1200 ppm 90 deg C 
0 
500 
1000 
1500 
2000 
2500 
3000 
3500 
0 20 40 60 80 
min 
CO2, ppm 
CO2,ppm 
Temp, deg C 
Clean Technology Pilot Laboratory 
Sunchon National University
Results & Discussion 
Fig. 14. Redox Potential by means of three Pt mini-electrodes on 
distance 
13 cm, 24 cm and 35 cm from the basis of a reactor 
Aniline 2400 ppm 
1440 
1460 
1480 
1500 
1520 
1540 
1560 
0 20 40 60 80 
min 
Redox Potential, mv 
R/O 1, mv 
R/O 2, mv 
R/O 3, mv 
Clean Technology Pilot Laboratory 
Sunchon National University
Results & Discussion 
Fig. 15. Redox Potential by means of three Pt mini-electrodes on distance 
13 cm, 24 cm and 35 cm from the basis of a reactor 
Aniline 1200 ppm 90 deg c 
1450 
1460 
1470 
1480 
1490 
1500 
1510 
1520 
1530 
1540 
0 20 40 60 80 
min 
Redox Potential, mv 
R/O 1, mv 
R/O 2, mv 
R/O 3, mv 
Clean Technology Pilot Laboratory 
Sunchon National University
Conclusions 
It is measured of kinetics of destruction of aniline by using MEO technique with Ce(IV) (aniline 1200 ppm and 600 ppm and temperature 70, 80, 90℃). 
It is established that at temperature of 90℃destruction of aniline was found to be more than 90%. 
The results obtained from the redox potential and moles of Ce(IV), testify in favor of the mechanism of destruction aniline with multi-electron coefficient n=28. 
Clean Technology Pilot Laboratory 
Sunchon National University
Acknowledgements 
This work was funded by “Core Environmental Technology Development 
Project for Next Generation”(Eco-Technopia-21) of “Korea Institute of 
Environmental Science and Technology”. 
Clean Technology Pilot Laboratory 
Sunchon National University

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Bobrov presentation ce4+ 2005

  • 1. Degradation of aniline by mediated electrochemical Oxidation (MEO) process Vladimir Bobrov, Sang Joon Chung, S. Balaji & Il Shik Moon* (Dept. of Chemical Engineering, Sunchon National University) Clean Technology Pilot Laboratory Sunchon National University
  • 2. Introduction Offers attractive route for the destruction of organic pollutants Metallic ion in the oxidized form in an acid acts as a mediator Mediator ion will oxidize organic pollutants into CO2and H2O Metallic ion constantly undergoing oxidation and reduction Major byproducts are CO2and H2O Highlights of Mediated Electrochemical Oxidation (MEO) Aniline as Target Organic Pollutant Aniline is a major by-product in petro-chemical and coal-tar industries Aniline will polymerize into more toxic poly aniline if not removed Clean Technology Pilot Laboratory Sunchon National University
  • 3. Mediated Electrochemical Oxidation(MEO) AnodeRegeneration of Ce4+ Ce3+→ Ce4++ e- Oxidation Reaction Ce4++ Organics → Ce3++ CO2+ InorganicsOxidationCe4+ Reduction Ce3+ Organics Inorganics, CO2 e- Clean Technology Pilot Laboratory Sunchon National University
  • 4. Object of this study •To Apply MEO Technology to Analyze the Destruction of High Concentrations of Aniline, under different solution temperatures •To evaluate the pattern of redox potential and CO2generation, during the destruction of aniline •To compare the theoretical and experimental values of Ce(IV) requirement for aniline destruction Clean Technology Pilot Laboratory Sunchon National University
  • 5. Experimental Fig. 1. Schematic of MEO Process Clean Technology Pilot LaboratorySunchon National UniversityMEO SolutionTank Silyine Pump Reactor Pt Electrode Scrubber CO2Analyzer Multi-Meter N2Cylinder
  • 6. Experimental Analysis Estimation of this study Ce3+/Ce4+redox potential in anolyte solution Estimating the amount of CO2in the off-gas Measurement of Ce3+/Ce4+redox potential -Pt-Ag/AgCl combined electrode -pH/ORP meter(Orion, model 720A) Measurement of degradation of Aniline -CO2analyzer(Environmental Instruments, Anagas CD 95) C6H7N+12H2O+28Ce(IV)6CO2+27H++NH4+28Ce(III) Clean Technology Pilot Laboratory Sunchon National University
  • 7. Results & Discussion Fig. 2. Evolution of CO2 during the degradation of 600ppm aniline at 70℃ (Theoretical Total Volume of CO2 for Complete degradation of Aniline = 232 ml) 0 1000 2000 3000 4000 5000 6000 7000 8000 9000 0 20 40 60 80 100 Reaction Time(min) Concentration of CO2(ppm) 0 20 40 60 80 100 120 140 Cumulative Volume of CO2(ml) Clean Technology Pilot Laboratory Sunchon National University
  • 8. Results & Discussion 0 1000 2000 3000 4000 5000 6000 7000 8000 9000 0 20 40 60 80 100 Reaction TIme(min) Concentration of CO2(ppm) -50 0 50 100 150 200 250 Cumulative Volume of CO2(ml) Fig. 3. Evolution of CO2 during the degradation of 600ppm aniline at 80℃ (Theoretical Total Volume of CO2 for Complete degradation of Aniline = 232 ml) Clean Technology Pilot Laboratory Sunchon National University
  • 9. Results & Discussion Fig. 4. Evolution of CO2 during the degradation of 600ppm aniline at 90℃ 0 2000 4000 6000 8000 10000 12000 14000 16000 18000 0 10 20 30 40 50 60 70 80 90 100 Reaction Time(min0 Concentration of CO2(ppm) 0 50 100 150 200 250 Cumulative Volume of CO2(ml) CO2 Theory 100% destruction of aniline (600 ppm) 232 ml CO2 EXPRIMENT 98% destruction of aniline (600 ppm) 227 ml CO2 C6H7N + 12 H2O + 28 Ce(IV)  6 CO2 + 27 H+ + NH4 + 28 Ce(III) Clean Technology Pilot Laboratory Sunchon National University
  • 10. Results & Discussion Fig. 5. Redox potential and Ce(IV) concentration under the degradation of 600ppm aniline at 90℃ 1460 1470 1480 1490 1500 1510 1520 0 50 100 150 200 Time, min Redox Potential, mV 0.7 0.75 0.8 0.85 0.9 0.95 1 Ce(IV), M Redox,mV Ce(IV), M Ce(IV) Theory 100% destruction of aniline (600 ppm) 0.18 M Ce(IV) EXPERIMENT 98% destruction of aniline (600 ppm) 0.16 M Ce(IV) For Theoretical Value for multi-electron coefficient degradation of aniline: Molar concentration of Ce(IV) / Molar Concentration of Aniline n=28 Clean Technology Pilot Laboratory Sunchon National University
  • 11. Results & Discussion 0 10 20 30 40 50 60 70 80 90 100 0 30 60 90 120 150 180 210 Reaction Time(min) Degradation of Aniline(%) 70℃ 80℃ 90℃ Fig. 6. The degradation of 600ppm aniline at different temperatures Clean Technology Pilot Laboratory Sunchon National University
  • 12. Results & Discussion 0 2000 4000 6000 8000 10000 12000 14000 0 10 20 30 40 50 60 70 80 90 100 Reaction Time(min) Concentration of CO2(ppm) 0 50 100 150 200 250 Cumulative Volume of CO2(ml) Fig. 7. Evolution of CO2 during the degradation of 1080ppm aniline at 70℃ Clean Technology Pilot Laboratory Sunchon National University
  • 13. Results & Discussion 0 5000 10000 15000 20000 25000 0 10 20 30 40 50 60 70 80 90 100 Reaction Time(min) Concentration of CO 2(ppm) 0 50 100 150 200 250 300 350 400 Cumulative Volume of CO 2(ml) Fig. 8. Evolution of CO2 during the degradation of 1200ppm aniline at 80℃ Clean Technology Pilot Laboratory Sunchon National University
  • 14. Results & Discussion Fig. 9. Evolution of CO2 during the degradation of 1200ppm aniline at 90℃ 0 5000 10000 15000 20000 25000 30000 0 10 20 30 40 50 60 70 80 90 100 Reaction Time(min) Concentration of CO2(ppm) 0 50 100 150 200 250 300 350 400 450 500 Cumulative Volume of CO2(ml) CO2 Theory 100% destruction of aniline (600 ppm) 464 ml CO2 EXPRIMENT 93% destruction of aniline (600 ppm) 430 ml CO2 C6H7N + 12 H2O + 28 Ce(IV)  6 CO2 + 27 H+ + NH4 + 28 Ce(III) Clean Technology Pilot Laboratory Sunchon National University
  • 15. Results & Discussion Fig. 10 Redox potential and Ce(IV) concentration under the degradation of 1200 ppm aniline at 90℃ Ce(IV) Theory 100% destruction of aniline (600 ppm) 0.36 M Ce(IV) EXPERIMENT 98% destruction of aniline (600 ppm) 0.35 M Ce(IV) For Theoretical Value for multi-electron coefficient degradation of aniline: Molar concentration of Ce(IV) / Molar Concentration of Aniline n=28 1440 1450 1460 1470 1480 1490 1500 1510 1520 1530 0 50 100 150 200 250 Time, min Redox, mV 0.6 0.65 0.7 0.75 0.8 0.85 0.9 0.95 1 Ce(IV), M Redox,mv Ce(IV), M Clean Technology Pilot Laboratory Sunchon National University
  • 16. Results & Discussion 0 10 20 30 40 50 60 70 80 90 100 0 50 100 150 200 250 Reaction Time(min) Degradation of Aniline(%) 70℃ 80℃ 90℃ Fig. 11. The degradation of 1200ppm aniline at different temperatures Clean Technology Pilot Laboratory Sunchon National University
  • 17. Results & Discussion Fig. 12. The degradation of 2400 aniline at temperature 90℃ in flow reactor. (Flow Rate of MEO solution = 2 ml/min, flow Aniline solution = 10 ml/h, volume of reactor = 120 ml) 2400 ppm Aniline 0 1000 2000 3000 4000 5000 6000 0 20 40 60 80 min CO2, ppm CO2,ppm Temp, deg C Clean Technology Pilot Laboratory Sunchon National University
  • 18. Results & Discussion Fig. 13. The degradation of 1200 aniline at temperature 90℃ in flow reactor. (Flow MEO solution = 2 ml/min, flow Aniline solution = 5 ml/h, volume of reactor = 120 ml ) Aniline 1200 ppm 90 deg C 0 500 1000 1500 2000 2500 3000 3500 0 20 40 60 80 min CO2, ppm CO2,ppm Temp, deg C Clean Technology Pilot Laboratory Sunchon National University
  • 19. Results & Discussion Fig. 14. Redox Potential by means of three Pt mini-electrodes on distance 13 cm, 24 cm and 35 cm from the basis of a reactor Aniline 2400 ppm 1440 1460 1480 1500 1520 1540 1560 0 20 40 60 80 min Redox Potential, mv R/O 1, mv R/O 2, mv R/O 3, mv Clean Technology Pilot Laboratory Sunchon National University
  • 20. Results & Discussion Fig. 15. Redox Potential by means of three Pt mini-electrodes on distance 13 cm, 24 cm and 35 cm from the basis of a reactor Aniline 1200 ppm 90 deg c 1450 1460 1470 1480 1490 1500 1510 1520 1530 1540 0 20 40 60 80 min Redox Potential, mv R/O 1, mv R/O 2, mv R/O 3, mv Clean Technology Pilot Laboratory Sunchon National University
  • 21. Conclusions It is measured of kinetics of destruction of aniline by using MEO technique with Ce(IV) (aniline 1200 ppm and 600 ppm and temperature 70, 80, 90℃). It is established that at temperature of 90℃destruction of aniline was found to be more than 90%. The results obtained from the redox potential and moles of Ce(IV), testify in favor of the mechanism of destruction aniline with multi-electron coefficient n=28. Clean Technology Pilot Laboratory Sunchon National University
  • 22. Acknowledgements This work was funded by “Core Environmental Technology Development Project for Next Generation”(Eco-Technopia-21) of “Korea Institute of Environmental Science and Technology”. Clean Technology Pilot Laboratory Sunchon National University