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If resistances to mass transfer, identified by the method as insignificant, are omitted from the simulations, the agreement between numerical predictions and experiment is not impaired.
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The modeling of the mass transfer is identified as the most important source of uncertainty of the simulation and discussed in detail.
Three parameters characterizing the mass transfer are identified and investigated with respect to pressure: the gas liquid interfacial area a, the volumetric liquid side mass transfer coefficient kLa and the volumetric gas side mass transfer coefficient kGa.
The kinetics of the IL in liquid and encapsulated form are compared with those for sodium carbonate solution and the cases where the capsule shell material limits mass transfer are identified.
Conditions favouring the significant effect of a discontinuous gas phase on mass transfer were identified as groundwater velocities less than ~ 0.01 m/day, and a gas phase that covers greater than ~ 10% of the pool surface area and is located within ~ 0.01 m of the pool surface.
The mass transfer mechanisms were identified.
Notably, gas mass transfer issues were identified, which allowed us to rationalize previous observations.
Droplet side volumetric mass transfer coefficients were identified from concentration field computations and the evolution of these coefficients as a function of the flow parameters and the channel size is discussed.
The compatibilization effect of PPE-epoxy copolymer formation was found to play a dominant role in determining the final size of the dispersed phase, while temperature control of reaction and mass transfer kinetics were identified as a possible means of further affecting the cured morphology.
The re-extraction of penicillin G from the solution of its ion-pair complex with the secondary amine Amberlite LA-2 was mathematically simulated, and the mass transfer coefficients were identified by means of the experimental investigations published in Likidis and Schügerl (1988, Chem. Engng Sci.43, 27 32) for a bench-scale Karr column, a pulsated perforated plate column and a Kühni column.
This study proposes a methodology to determine the external mass transfer coefficient and identify the influence of the mixing intensity on the conversion process in-situ in MBBR systems.
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CEO of Professional Science Editing for Scientists @ prosciediting.com