Abstract
An approximate numerical method for the estimation of the velocity exponent in (small-scale) flow-through porous and gauze electrodes is presented. The method can also be employed to determine if a plug-flow or a parabolic-flow model offers a more reliable representation of the experimental behaviour of the electrode.
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Abbreviations
- a :
-
cross sectional area of the electrode
- B :
-
integration parameter (Equations 7 and 8)
- c :
-
exit active ion concentration,\(\bar c\) its mean measured value in the case of parabolic flow,c o its inlet value;c m its mean value;\(\overline {c_m }\) its mean calculated value in the case of parabolic flow;c * dimensionless concentration, equal toc/c o;\(\overline {c^* }\) mean dimensionless concentration, equal to ⊸/c o
- F :
-
Faraday's constant
- i L :
-
mean limiting current density (geometric-area base)
- j :
-
proportionality factor (Equation 1)
- k m :
-
mass transport coefficient,\(\overline {k_m }\) its mean value
- L :
-
length of the electrode
- n :
-
number of electrons involved in the electrode reaction
- N :
-
ionic flux
- r :
-
radial coordinate
- R E :
-
geometric radius
- R :
-
limiting degree of conversion
- s :
-
specific surface area of the electrode (surface per volume)
- u :
-
linear solution velocity; uo its maximum (centreline) value; ū its mean value (ū=uo/2)
- v :
-
volumetric flow rate;\(\bar v\) its mean value
- x :
-
transform variable forz
- z :
-
dimensionless radial distance
- α:
-
velocity exponent for mass transport (Equation 1)
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Sioda, R.E., Fahidy, T.Z. The performance of porous and gauze electrodes in electrolysis with parabolic velocity distribution. J Appl Electrochem 18, 853–856 (1988). https://doi.org/10.1007/BF01016041
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DOI: https://doi.org/10.1007/BF01016041