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This document summarizes convective mass transfer between phases, specifically the removal of solute A from a gas stream using a countercurrent absorber. It provides example calculations for a system where the mole fraction of A in the gas is 0.035 and in the liquid is 0.01, at 300K and 2 atm pressure with 60% resistance in the gas phase. It calculates the interfacial compositions, overall mass transfer coefficient for the gas phase, and overall mass transfer coefficient for the liquid phase at this operati
- Author
- Xclipsion
- Language
- EN