The time evolution of (bio)chemical processes, specifically
those
involving distributed species as in polymer synthesis and recycling,
can be obtained using Gillespie-based kinetic Monte Carlo simulations,
provided that a sufficiently high (Monte Carlo) control volume is
utilized with respect to the simulation targets (e.g., focus on only
conversion/yield or a combination of the former and average molar
masses, or even the combination with complete distributions with accurate
tail prediction). For more detailed kinetics and more demanding simulations
targets, currently, simulation results are mostly visually checked
to decide which control volume to practically use, taking into account
user time constraints. The present work puts forward a convergence
strategy that avoids relying on subjective visual analysis to set
the minimum control value that guarantees the minimization of the
stochastic noise for several simulation target combinations to acceptable
values. The strategy is illustrated for two (for simplicity, intrinsic)
non-dispersed phase bulk chain-growth polymerization processes, one
with high average chain lengths and a broad chain length distribution
(CLD), that is, free-radical polymerization (FRP), and one with low
average chain lengths and a narrow CLD, that is, nitroxide-mediated
polymerization (NMP). It is showcased that the monomer conversion
profile converges the fastest, with even the occurrence of noise-free
simulation results in the absence of numerical convergence. A sufficiently
accurate representation of the tail of the (number) CLD in FRP demands
a sufficiently high control volume so that relative errors below 0.5%
result for the z-based average chain length or molar
mass (M
z). This need to inspect M
z convergence further holds under NMP, in general,
reversible deactivation radical polymerization (RDRP) conditions,
in which it is uncommon to report such higher order averages. An automated
convergence check beyond threshold values is recommended to minimize
the impact of possible fluctuations in certain simulation targets,
specifically peak representations, for example, the initial spike
in the dispersity plot in RDRP. The convergence results are supported
by the number of radicals in the control volume with values much higher
than 2 to accurately represent termination kinetics for specifically
CLD prediction, already under intrinsic conditions.