Thanks to Algorithm 1, it is possible for the first time (up to our knowledge) to study the distribution of patterns in a data set of upstream regions using an heterogeneous model.
The study followed the common, core protocol of the INTERPHONE study, but for estimating RF exposure level in different areas of the brain in light of its great variability, we adopted a new approach using a heterogeneous head model (Japanese numerical TARO model's head) (Nagaoka et al, 2004).
Using these clinical restitution data, we studied the dynamics of VF in the human heart using a heterogeneous computational model of human ventricles.
The performance of both adiabatic fixed-bed reactors (FBR and RFRR operating with particulate or monolith catalysts has been simulated using a heterogeneous one-dimensional model, experimentally validated for other reactions in previous works.
The simulation of a reverse-flow operation of a fixed-bed catalytic reactor, where the highly exothermal partial oxidation of o-xylene to phthalic anhydride is processed, is accomplished by using a heterogeneous one-dimensional model, which accounts for mass transport by diffusion and convection inside large-pore catalytic particles.
While additional phylogenetic analyses (not shown) were carried out in PhyloBayes (v2.3) using a heterogeneous-site model (GTRCAT), our dataset failed to converge after surpassing the recommended maximum of 10,000 MCMC cycles on each of 6 chains and running for over 60 days [ 106].
The combustion of binary mixtures of these compounds (up to 500 ppmV total hydrocarbon concentration) over a commercial Pt/Al2O3 catalyst in reverse flow reactors has been studied both experimentally, in a bench-scale unit, and by simulations, using a heterogeneous mono-dimensional dynamic model, good correspondence being observed between both approaches.
The rate data were interpreted by developing, and using, a heterogeneous, unsteady state mass transfer model based on Danckwerts' surface renewal theory and particle-to-interface adhesion.
The sensitivity behavior of fixed-bed catalytic reactors is examined using a heterogeneous one-dimensional plug-flow model, for the case of n-th order irreversible reactions.
The first three components are modeled using engineering physically-based models, while the activity patterns of individuals are modeled using a heterogeneous Markov chain.
