\(\mathbf{\nu}\) |
Kinematic viscosity |
\(\mathbf{\rho}\) |
Density of the electrolyte |
\(\Phi\) |
Geometry parameter for laminar entry length |
\(\mathbf{A}\) |
Electrode area |
\(\mathbf{A}_{\mathbf{\text{ch}}}\) |
Cross-sectional area of the
channel |
\(\mathbf{A}_{\mathbf{\text{in}}}\) |
Cross-sectional area of the
inlet |
\(\mathbf{B}\) |
Electrode width (breadth) |
\(\mathbf{C}_{\mathbf{(}\mathbf{\text{III}}\mathbf{)}}\) |
Concentration
of hexachloroiridate(III) |
\(\mathbf{C}_{\left(\mathbf{\text{IV}}\right)}\) |
Concentration of
hexachloroiridate(IV) |
\(\mathbf{C}_{\mathbf{\text{bulk}}}\) |
Bulk concentration of the
reacting species |
\(\mathbf{D}\) |
Diffusion Coefficient |
\(\mathbf{d}_{\mathbf{H}}\) |
Hydraulic Diameter
2BS/(B+S) |
\(\mathbf{F}\) |
Faraday’s number, i.e. 76485 C/mol |
\(\mathbf{f}\) |
Friction factor |
\(\mathbf{i}_{\mathbf{A,lim}}\) |
Limiting current
density |
\(\mathbf{J}_{\mathbf{M}}\) |
J-factor for mass transfer
(Chilton-Colburn) |
\(\mathbf{k}_{\mathbf{\text{LS}}}\) |
Liquid-Solid Mass transfer
coefficient |
\(\mathbf{L}\) |
Electrode length |
\(\mathbf{L}_{\mathbf{\text{entry}}}\) |
Hydrodynamic Entry
Length |
Le |
Length number
L/dH
|
\(\mathbf{n}\) |
Number of electrons exchanged |
Re |
Reynolds number
\(v_{0}d_{H}/\nu\)
|
\(\mathbf{S}\) |
Electrode spacing |
Sc |
Schmidth number \(\nu/D\)
|
Sh |
Sherwood number
\(k_{\text{LS}}d_{H}/D\)
|
\(\mathbf{T}\) |
Temperature |
\(\mathbf{v}_{\mathbf{0}}\) |
Flow velocity over the
electrode |