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The interfacial area decreases with increased value of Ka.
Calderbank's correlation for predicting interfacial area has been independently verified.
These results allow us to determine the specific interfacial area.
Currently, the interfacial area is predicted using flow regime-dependent semi-empirical correlations; however the interfacial area concentration is best computed through the use of the one-dimensional interfacial area transport equation (IATE).
Currently, the interfacial area is predicted using flow regime dependent empirical correlations; however the interfacial area concentration is best computed through the use of the one-dimensional interfacial area transport equation (IATE).
Variability of both the mass transfer coefficient that explicitly accounts for the interfacial area and the mass transfer coefficient that lumps the interfacial area was examined.
The silica exterior interfacial area is vanishingly small and the PS124 exterior interfacial area is much larger than that of the silica PS124 interface.
From this point of view, a simple equation for the interfacial area concentration has been derived from the interfacial area transport equation.
The high interfacial area produced in such reactors gives them an advantage over the conventional contactors.
With non-coalescing media the average interfacial area ranged from 40 to 560m−1.
Porous morphologies with increased interfacial area enhance light capture capacity and accelerate catalysis reaction.
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