Abstract
AbstractExperiments have been performed to determine mass transfer coefficients for the dissolution of sodium chloride particles carried as a “settling” suspension in a horizontal pipeline. The coefficients obtained for two sizes of particles, along with other coefficients available from the literature for different systems, have been correlated with an average deviation of only 7% by making use of Durand's equation for predicting pressure gradients for the flow of “settling” suspensions and the analogy between momentum and mass transfer.
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