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Accordingly, mathematical model and numerical method are offered.
Figure 1 shows a good match of gas flow rate and cumulative gas production between the semi-analytical model and numerical model and analytical model.
The physical model and numerical method for estimating different kinds of losses in CICCs are proposed.
The simulation results verify the effectiveness and feasibility of proposed mathematical model and numerical algorithm.
Numerical examples are presented to demonstrate the applicability of the proposed optimization model and numerical techniques.
Mathematical model and numerical methods employed are validated by comparing predicted results against prior experimental measurements.
Analytical results are compared with an existing analytical model and numerical simulation.
The mathematical model and numerical treatments for the CEACS H∞ control architecture are presented.
The mathematical model and numerical results are presented in non-dimensional form.
This generates as many simultaneous equations as there are degrees of freedom in the finite element model, and numerical techniques for solving such systems of equations are programmed for computer solution.
The results from the spray profile model and numerical simulation were compared to experimental data and good agreements were demonstrated.
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