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A one-dimensional simulation model based on mass and energy balances and a drift flux model is developed which predicts well the pressure and temperature transients and the mass flow rate.
The microreactor (25×17×1.3mm3) is constructed from glass and silicon substrates to form a serpentine catalyst-coated microchannel of 333 mm in length and cross-section of 0.6×0.4mm2, designed based on mass and heat balance analyses using a one-dimensional model.
Therefore, we propose the afterburner temperature control based on mass and thermal balances.
These models are developed based on mass and energy balance equations.
This mathematical model is developed based on mass and energy equation.
A hydrodynamic model was developed based on mass and pressure balances.
The steady-state evaporation process was modeled by means of a phenomenological model based on mass and energy balances.
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A 10 μl sample of a 4-fold dilution was analyzed by LC-MS for GDP and GTP based on mass, fragmentation and retention time.
The TAL cell model represents 13 major solutes and the associated transporters and channels; model equations are based on mass conservation and electroneutrality constraints.
Basic design calculations have been carried out based on fluidization engineering methods and a practical process configuration has been evaluated based on mass- and energy balances.
But the FSM was based on mass meetings and consensus.
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