Simulations for the CMPO and CMPO-BMA base models on platinum were carried out in a PFR, which was approximated as a series of CSTRs in Cantera, with C/O input gas ratios from 0.6 to 2.6 to replicate the experimental work. The models showed a noticeable di↵erence compared against the experimental data, but general descriptor trends agreed. As the goal of this work was to explore the influence of BMA rates, we determined the RMG model has good enough agreement with experimental results and would be used as a base reaction barriers are a function of the reaction enthalpy. Unlike the Brønsted-Evans-Polanyi (BEP) expression, this BMA form only requires one parameter (so it can be derived from a single reaction rate expression), and gives reasonable values when extrapolated to very high and low reaction enthalpies. We have shown that using BMA instead of simple Arrhenius expressions (with a fixed forward reaction barrier) during model analysis can lead to di↵erent results -both in the binding energies of the optimal catalyst, and in the relative importance of specific adsorbate enthalpies. Incorporating the BMA rate description into Cantera enables a new workflow, demonstrated herein, allowing rapid screening of catalysts using linear scaling relationships (LSRs) and BMA kinetics within the simulation software, with a single model input file. This can provide a starting point for a model of interest for further improvements.