Publication | Open Access
Diffusion Coefficients and Viscosities of CO<sub>2</sub> + H<sub>2</sub>O, CO<sub>2</sub> + CH<sub>3</sub>OH, NH<sub>3</sub> + H<sub>2</sub>O, and NH<sub>3</sub> + CH<sub>3</sub>OH Liquid Mixtures
240
Citations
10
References
1996
Year
Gas−liquid Absorption ExperimentsChemical EngineeringTaylor−aris Dispersion MethodFluid PropertiesEngineeringMolecular ThermodynamicsDiffusion ResistanceLiquid-liquid FlowFluid MechanicsDiffusion ProcessDiffusion CoefficientsDisperse FlowExperimental ThermodynamicsChemistryAmmonia Mole FractionGas-liquid FlowChemical Kinetics
To evaluate quantitatively the results of gas−liquid absorption experiments, accurate liquid-phase diffusion coefficients and viscosities are needed. In this paper experimental values of these quantities will be reported for the binary systems carbon dioxide + water, carbon dioxide + methanol, ammonia + water, and ammonia + methanol. The diffusion coefficients have been measured using the Taylor−Aris dispersion method, and the viscosities have been measured with a falling ball viscometer at temperatures from 293 to 333 K. The ammonia mole fraction ranged from 0 to 0.312. The results have been correlated using Arrhenius-type equations and have been compared with literature data, where available. Furthermore, the measured diffusion coefficients are compared with values predicted by the modified Stokes−Einstein equation and the Wilke−Chang equation.
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