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Specific experiments are proposed to investigate the effect of surfactants on liquid side mass transfer coefficients.
In general, the major rate limiting steps occur on the liquid side.
Commonly, the rate limiting step is the diffusive mass transport within the liquid side.
The same result has been observed with the volumetric liquid side mass transfer coefficient kLa.
The results indicate that liquid side resistance is negligible in comparison with membrane and gas side resistances.
Concerning the liquid side mass transfer, it is found that the liquid side mass transfer is well predicted by the Higbie (1935) theory provided that adequate velocity and length scales are considered for exposure time determination.
Similar(25)
Lower plate angles resulted in lower liquid-side mass transfer coefficients.
As a second step, different methods of calculating liquid-side mass transfer fluxes are compared.
The liquid-side mass transfer coefficient and the average bubble diameter dB were also estimated.
The mass transfer is supposed to be limited by the liquid-side resistance.
However, an opposite behavior was observed in the liquid-side mass transfer coefficient values.
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