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Generalized MEP-based formulations are derived to simulate hysteresis strain stress curves.
The model was based on analytical equations previously derived to simulate well-mixed fluidized bed dryers, combined with axial dispersion theory.
The combined model of thermionic emission and carrier drift-diffusion is derived to simulate the electrical transport through BST thin film capacitors.
A mathematical model was derived to simulate the process of hydrate dissociation and gas invasion into wellbore within a few hours when hydrate zones being penetrated during drilling.
Analytical solutions under proper assumptions are derived to simulate the transient- and steady-state rates of the overall hydrogen permeation, and close agreement is obtained between experiment and analysis.
The volume-of-fluid model is based on a multiple-marker method with a smoothed surface tension calculation, and a thin-film model is derived to simulate film drainage using a Reynolds equation approach.
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The design and optimization implications are demonstrated by using the derived solution to simulate the performance of an immobilized-urease fluidized-bed bioreactor with a recycle loop.
Then, according to the LDC, a calibration was conducted to determine the computational concentration profile at the station A and then the concentration profile was simulated and derived to each sampling station.
Then, a temperature expansion model is derived in order to simulate this behaviour with the finite element tool ABAQUS.
A stability criterion in terms of transfer functions was derived and used to simulate the behaviour of generic systems.
Furthermore, a statistical shear load transfer law based on the shear lag analysis was derived and implemented to simulate the interactions between adjacent fibers and provide a more accurate tensile stress distribution along the overlap distance.
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