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Gas-liquid and liquid-solid mass transfer were studied in capillaries under Taylor flow regime.
Then, gas holdup, mass transfer, mixing and heat transfer were studied as a function of the aeration rate.
Bubble breakage and coalescence phenomena and multicomponent gas liquid mass transfer were studied in a 194dm3 Rushton turbine agitated vessel.
The effects of silica coating and water droplet size as well as the volume fraction of dry water particles on reducing radiative heat transfer were studied parametrically.
Within this work the charge and discharge characteristics of the reactor concerning possible limitations due to heat and mass transfer were studied experimentally.
Axial and radial distributions of heat transfer were studied in a 15.1 m high, 100 mm diameter gas solids upflow fluidized bed (riser) with FCC particles.
Similar(50)
The influence of pulsation on the mass transfer is studied.
The effect of channel shape and geometrical parameter on the boiling heat transfer is studied.
Finally, the effect of the membrane deflection on the mass transfer was studied.
Magnetohydrodynamic and ferrohydrodynamic effects on convective heat transfer are studied in this chapter.
In this paper the mass transfer is studied simultaneously to the production process of asymmetric membranes.
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CEO of Professional Science Editing for Scientists @ prosciediting.com