Bd. Phenix et al., INCORPORATION OF PARAMETRIC UNCERTAINTY INTO COMPLEX KINETIC MECHANISMS - APPLICATION TO HYDROGEN OXIDATION IN SUPERCRITICAL WATER, Combustion and flame, 112(1-2), 1998, pp. 132-146
In this study, uncertainty analysis is applied to a supercritical wate
r hydrogen oxidation mechanism to determine the effect of uncertaintie
s in reaction rate constants and species thermochemistry on predicted
species concentrations. Forward rate constants and species thermochemi
stry are assumed to be the sole contributors to uncertainty in the rea
ction model with all other model parameters and inputs treated as dete
rministic quantities. The analysis is conducted by treating the model
parameters as random variables, assigning each a suitable probability
density function, and propagating the parametric uncertainties through
to the predicted species concentrations. Uncertainty propagation is p
erformed using traditional Monte Carlo (MC) simulation and a new, more
computationally efficient, probabilistic collocation method called th
e Deterministic Equivalent Modeling Method (DEMM). Both methods predic
t virtually identical probability distributions for the resulting spec
ies concentrations as a function of time, with DEMM requiring approxim
ately two orders of magnitude less computation time than the correspon
ding MC simulation. The results of both analyses show that there is co
nsiderable uncertainty in all predicted species concentrations. The pr
edicted H-2 and O-2 concentrations vary +/- 70% from their median valu
es. Similarly, the HO2 concentration ranges from +90 to -70% of its me
dian, while the H2O2 concentration varies by +180 to -80%. In addition
, the DEMM methodology identified two key model parameters, the standa
rd-state heat of formation of HO2 radical and the forward rate constan
t for H2O2 dissociation, as the largest contributors to the uncertaint
y in the predicted hydrogen and oxygen species concentrations. The ana
lyses further show that the change in model predictions due to the inc
lusion of real-gas effects, which are potentially important for SCWO p
rocess modeling, is small relative to the uncertainty introduced by th
e model parameters themselves. (C) 1998 by The Combustion Institute.