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- W1510243950 abstract "A theoretical study of simultaneous heat and mass transfer in binary distillation has shown that heat and mass transfer coefficients can be appropriately evaluated if liquid phase temperatures and compositions are measured as functions of height in a column. In this study, the experiments were carried out in a wetted-wall column using a methanol-water binary system at one atmosphere. Special probes were designed to determine the state of the liquid phase. Temperatures were measured with microthermocouples and liquid samples were analyzed with a high precision refractometer. The liquid phase was found to be saturated which indicated, in accordance with the conclusions from a theoretical study, that all the resistance to mass transfer was in the vapor phase. Local transfer coefficients were calculated using the composition data as a function of column height. The results were correlated by an equation showing close agreement with the Chilton-Colburn equation. kyamV = 0.039Scy−23Rey−0.20 cm−1. It is concluded that mass transfer in the vapor phase is the controlling resistance in distillation and that there is no additional evaporation within the liquid phase caused by heat transferred from the vapor phase as proposed by some previous investigators." @default.
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- W1510243950 date "1977-01-01" @default.
- W1510243950 modified "2023-09-23" @default.
- W1510243950 title "Simultaneous heat and mass transfer in binary distillation—II" @default.
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- W1510243950 doi "https://doi.org/10.1016/0009-2509(77)80124-3" @default.
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