Abstract
Various mathematical models for the electrosynthesis of chlorate are analysed taking into account that the current efficiency is mainly affected by the distribution of the two competing reactions forming chlorate, i.e. the anodic oxidation and the autoxidation of hypochlorite. It is shown that the current efficiency is determined by four dimensionless groups one of which is commonly negligible. Results are compared with a known current efficiency equation. Two new current efficiency equations, representing the limiting operating conditions of chlorate systems, are proposed for industrial application.
Similar content being viewed by others
Abbreviations
- a :
-
activity (−)
- A :
-
electrode surface are (m2)
- c :
-
concentration of hypochlorite (mol m−3)
- C, C′ :
-
numerical constants, Equations 19 and 45
- F :
-
Faraday constant (F=96 487 A s mol−1)
- H :
-
electrode height (m)
- I :
-
total current (A)
- I 1,I 2 :
-
partial currents of chloride oxidation (A)
- I a :
-
partial current of hypochlorite oxidation (A)
- I v :
-
loss currents (A)
- K * :
-
equilibrium constant of Reaction 6 (−)
- K a :
-
anodic oxidation number (−)
- k d :
-
mass transfer coefficient (m s−1)
- k r :
-
reaction rate constant of chemical hypochlorite oxidation (m6 mol−2 s−1)
- K rC :
-
autoxidation number of cell (−)
- K rR :
-
autoxidation number of chemical reactor (−)
- \(N^\blacksquare \) :
-
flux of total hypochlorite (mol s−1)
- Re :
-
Reynolds number (−)
- S :
-
cross-sectional area of fluid flow (m2)
- Sc :
-
Schmidt number (−)
- Sh :
-
Sherwood number (−)
- St :
-
Stanton number, Equation 32 (−)
- t :
-
time (s)
- V :
-
volume (m3)
- \(V_L ^\blacksquare \) :
-
liquid flow rate (m3 s−1)
- x:
-
coordinate in flow direction (m)
- ε:
-
current efficiency (−)
- a:
-
anodic oxidation of hypochlorite
- C:
-
cell
- i:
-
entrance cell
- o:
-
exit cell
- r:
-
autoxidation of hypochlorite
- R:
-
chemical reactor
References
F. Foerster, E. Müller and F. Jorre,Z. Elektrochem. 6 (1899) 11–23.
B. V. Tilak, K. Viswanathan and C. C. Rader,J. Electrochem. Soc. 128 (1981) 1228.
N. Ibl and H. Vogt,in ‘Comprehensive Treatise of Electrochemistry’ (edited by J. O'M. Bockris, B. E. Conway, E. Yeager and R. E. White) Vol. 2, Plenum, New York (1981) pp. 169–201.
I. E. Flis and M. K. Bynyaeva,Zh. Prikl. Khim. 30 (1957) 339;J. Appl. Chem. USSR 30 (1957) 359–65.
M. M. Jaksić, B. Z. Nikolić, I. M. Csonka and A. B. Djordjević,J. Electrochem. Soc. 116 (1969) 684–7.
M. M. Jaksić, A. R. Despić and B. Z. Nikolić,Elektrokhim. 8 (1971) 1573–84;Sov. Electrochem. 8 (1973) 1533–42.
V. de Valera,Trans. Faraday Soc. 49 (1953) 1338–51.
L. Hammar and G. Wranglén,Electrochim. Acta 9 (1964) 1–16.
N. Ibl and D. Landolt,Chemie-Ing.-Tech. 329 (1967) 706–12.
N. Ibl and D. Landolt,J. Electrochem. Soc. 115 (1968) 713–20.
D. Landolt and N. Ibl,Electrochim. Acta 15 (1970) 1165–83.
M. M. Jaksić,J. Electrochem. Soc. 121 (1974) 71–9.
M. M. Jaksić,Electrochim. Acta 21 (1976) 1127–36.
A. R. Despić, M. M. Jaksić and B. Z. Nikolić,J. Appl. Electrochem. 2 (1972) 337–43.
T. R. Beck,J. Electrochem. Soc. 116 (1969) 1038–41.
T. R. Beck and R. Brännland,119 (1972) 320–25.
K. G. Denbigh and J. C. R. Turner, ‘A Chemical Reactor Theory’ 3rd edn, Cambridge University Press, Cambridge (1984).
H. Vogt and P. Wintzer,in ‘Ullmann's Encyclopedia of Industrial Chemistry’, Vol. A6, VCH Verlagsges., Weinheim (1986) pp. 501–14.
J. E. Colman,A. I. Ch. E. J. Symp. Ser. 77 (1981) No. 204, 244–69.
F. Hine, M. Yasuda and R. Nakamura,J. Electrochem. Soc. 122 (1975) 1185–90.
H. Vogt,Electrochim. Acta 26 (1981) 1311–17;27 (1982) 1157.
E. Müller and P. Koppe,Z. Elektrochem. 17 (1911) 421–30.
Author information
Authors and Affiliations
Rights and permissions
About this article
Cite this article
Vogt, H. Chlorate electrosynthesis current efficiency equations based on dimensionless groups. J Appl Electrochem 22, 1185–1191 (1992). https://doi.org/10.1007/BF01297422
Received:
Revised:
Accepted:
Issue Date:
DOI: https://doi.org/10.1007/BF01297422