A bubble curtain model applied in chlorate electrolysis
A bubble curtain model applied in chlorate electrolysis
A bubble curtain model applied in chlorate electrolysis
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mR equivalent<br />
mR hydraulic<br />
Nomenclature<br />
Symbol<br />
unity<br />
A m 2 surface<br />
D m 2 /s diffusivity<br />
E J energy<br />
F C/mole Faraday constant: 96.485 C/mole<br />
F subscript N force<br />
I A current<br />
L m distance from electrode gap entrance<br />
M g/mole molar mass<br />
P Pa pressure<br />
R J/(mole. K) universal gas constant: 8,31 J/(mol K)<br />
R Ω resistance<br />
S mole/(m 3 , Pa) solubility<br />
T K temperature<br />
U V voltage<br />
V m 3 volume<br />
c mole/m 3 concentration<br />
d m diameter<br />
f - partial free area<br />
g m/s 2 gravitational acceleration: 9,81 m/s 2<br />
i A/m 2 current density<br />
m g mass<br />
r m radius<br />
s m distance electrode gap<br />
t s time<br />
v m/s velocity<br />
w m width of the electrode<br />
x m coord<strong>in</strong>ate over the width of the electrode gap<br />
y m coord<strong>in</strong>ate over the height <strong>in</strong> the electrode gap<br />
z - # exchanged electrons<br />
d e<br />
R<br />
d h<br />
R<br />
diameter<br />
diameter<br />
C d - drag coefficient<br />
iv