In this two-part paper, we describe the construction,
validation,
and application of a multiscale model of entrained flow gasification.
The accuracy of the model is demonstrated by (1) rigorously constructing
and validating the key constituent submodels against relevant canonical
test cases from the literature and (2) validating the integrated model
against experimental data from laboratory scale and commercial scale
gasifiers. In part I, the flow solver and particle turbulent dispersion
models are validated against experimental data from nonswirling flow
and swirling flow test cases in an axisymmetric sudden expansion geometry
and a two-phase flow test case in a cylindrical bluff body geometry.
Results show that while the large eddy simulation (LES) performs best
among all tested models in predicting both swirling and nonswirling
flows, the shear stress transport (SST) k–ω
model is the best choice among the commonly used Reynolds-averaged
Navier–Stokes (RANS) models. The particle turbulent dispersion
model is accurate enough in predicting particle trajectories in complex
turbulent flows when the underlying turbulent flow is well predicted.
Moreover, a commonly used modeling constant in the particle dispersion
model is optimized on the basis of comparisons with particle-phase
experimental data for the two-phase flow bluff body case.