The resistivity ratio due to gas bubbles underneath horizontal anodes in el
ectrolytic cells was measured and compared with that in an air-water model
of identical geometry. It was found that at equal current density or equiva
lent gas generation rate, the difference in the bubble resistivity ratio be
tween these two situations can be up to 20%. Consequently, the results obta
ined from an air-water model cannot be directly applied to an electrolytic
cell. Results also showed that within the range of experimental conditions
covered, the bubble resistivity ratios obtained for a given anode-cathode d
istance in both cells are linearly related to the bubble coverage ratio, ba
sed on bubbles greater than a certain size as limited by the measurement me
thod.