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The end-member mixing model was employed for hydrograph separation.
An isotopic mixing model was employed to estimate the contributions of particulate sources.
A constant-pressure mixing model was adopted to simulate the ejector.
To study polymerization, the mixing model was combined with a kinetic model of the polymerization reaction.
Turbulent ignition temperatures were similar to laminar ones when the mixing model was modified to account for preferential diffusion.
A mixing model was designed that was capable of predicting RTD (residence time distribution) curves for different cases in non-isothermal conditions.
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The mixing model is easy to perform.
Such a mixing model is illustrated in Figure 1. Figure 1 Multi-microphone signal model.
This type of mixing model is called a convolutive model [176].
On the basis of the experimental results, a phenomenological mixing model is derived.
The mixing model is the log-max approximation and the compound states are inferred using factorial Viterbi algorithm.
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