Results are presented and the effects of heat and mass transfer are analyzed.
Effect of Reynolds number, gas flow structure and Prandtl mixing length on the mass transfer were analyzed.
Based on carbon dioxide properties and its solubility in water, carbon dioxide deliming principle and mass transfer were analyzed, respectively.
Miscibility is to be reached within the cell through a phase composition changes subsequent to a multiple contact and mass transfer between analyzing cell fluids, i.e., crude oil, brine, and injected gas.
Mass transfer rates were analyzed with roughness mass transfer function and roughness Reynolds number.
Three-dimensional heat and mass transfer characteristics were analyzed using the Standard k ε turbulence model.
The effects of nanoparticle Brownian motion and thermophoresis on the heat and mass transfer characteristics are analyzed.
Further, the heat and mass transfer performances were analyzed and some guidance to improve the unit design was provided.
Performance indices including the moisture removal rate, dehumidification/regeneration efficiency, and volumetric mass transfer coefficient were analyzed in conjunction with the inlet parameters.
The effects of operating time and solid wall thickness on the air side convective heat and mass transfer coefficients are analyzed.
