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Journal of Applied Electrochemistry

, Volume 22, Issue 4, pp 315–324 | Cite as

Formation of hypochlorite, chlorate and oxygen during NaCl electrolysis from alkaline solutions at an RuO2/TiO2 anode

  • L. R. Czarnetzki
  • L. J. J. Janssen
Paper

Abstract

On-site electrolysis of a weak alkaline solution of NaCl has been applied to an increasing extent for disinfection. To optimize the electrolytic cell and the electrolysis conditions, the current efficiency for hypochlorite, chlorate and oxygen formation at a commercial RuO2/TiO2 anode were determined under various conditions. It was found that for solution with low NaCl concentrations, (lower than 200 mol m−3), and at 298 K, solution flow velocity of 0.075 ms−1 and high current density, (higher than 2 kA m−2), hypochlorite formation is determined by mass transfer of chloride. The formation of chlorate in weakly alkaline media at a chlorine and oxygen-evolving anode is ascribed to two reactions, namely, the direct oxidation of chloride to chlorate and the conversion of hypochlorite. This is suggested to split the well-known electrochemical Foerster reaction into a chemical reaction for the conversion of hypochlorite in chlorate and the electrochemical oxidation reaction of water. It is proposed that in an acidic reaction layer at the anode the mechanism of chlorate formation may be given by the following:

Keywords

Oxygen Physical Chemistry Chlorate Hypochlorite Alkaline Solution 
These keywords were added by machine and not by the authors. This process is experimental and the keywords may be updated as the learning algorithm improves.

Notation

Ac

electrode surface area (m2)

ci

concentration of speciesi (mol m−3)

ci, 0

ci attc=0 (mol m−3)

Di

diffusion constant of speciesi (m2 s−1)

E

electrode potential versus saturated calomel electrode (V)

F

Faraday constant (C mol−1)

i

current (A)

j

current density (A m−2)

jd

diffusion-limiting current density (A m−2)

hi

slope ofni/c3 curve (m3 s−1)

kd, i

diffusion mass-transfer coefficient of speciesi (m s−1)

kd, f, i

kd, i at forced convection of solution and in the absence of bubble (m s−1) evolution

Ni

quantity of speciesi formed during the electrolysis (mol)

ni

rate of formation for speciesi (mol s−1)

n4, S

n4 determined by diffusion limitation of hypochlorite (mol s−1)

t

time (s)

te

time of electrolysis (s)

T

absolute temperature (K)

v0

average flow velocity of solution in the anodic compartment of the cell at the level of the leading edge of the electrode (m s−1)

Φi

current efficiency for speciesi

Φi, o

Φ i atte=0

Subscripts

av

average

d

diffusion

e

electrolysis, electrode

f

forced convection

ox

oxygen

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Copyright information

© Chapman & Hall 1992

Authors and Affiliations

  • L. R. Czarnetzki
    • 1
  • L. J. J. Janssen
    • 1
  1. 1.Faculty of Chemical EngineeringEindhoven University of TechnologyEindhovenThe Netherlands

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