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The model we develop for the reaction mechanism is based on the mass transfer limited (shrinking core) reaction scheme.
The scheme for mass transfer analysis is based on an immobilized emulsion globule drop model and the classical film theory, i.e. the overall mass transfer resistance includes that due to the external turbulent boundary layer, the interfacial surfactant layer and the diffusion layer within the emulsion globule.
In heterogeneous schemes, on the other hand, the mass transfer and the general hydrodynamic behaviour of the system can become crucial.
Heat and mass transfer models are necessary in the predictive calculation schemes used by the motorists.
A transient three-dimensional numerical scheme considering both inter-particle and intra-particle mass transfer resistances is developed to examine the performance of silica gel/water adsorption chiller.
The coupled heat and mass transfer equations were solved using a fully implicit accurate finite difference scheme to predict air temperature and humidity distribution throughout the dry and wet channels.
Two earlier classification schemes based on the underlying heat and mass transfer processes and the combination of reaction with various unit operations are reviewed.
Different spatial discretization schemes including the fifth-order WENO (weighted essentially nonoscillatory), second-order ENO (essentially nonoscillatory) and power-law schemes, are tested for the solution of mass transfer to or from single drops.
In the design of remediation schemes that use surfactants, it is necessary to estimate the mass transfer rate coefficients under multi-dimensional flow fields that exit at field sites.
Three phase reaction schemes pose numerous challenges to reactor design due to the slow diffusional mass transfer of reactants from the gas phase through a liquid to the active sites of the catalyst.
A three-dimensional transient double-population thermal lattice Boltzmann BGK scheme for the global evaporator of a CPL is proposed to describe the heat and mass transfer in the porous wick, the cover plate and the vapor groove.
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CEO of Professional Science Editing for Scientists @ prosciediting.com