posted on 2025-05-06, 01:05authored bySimon Shindler, Rong Yang
While
initiated chemical vapor deposition (iCVD) has been used
in a wide range of fundamental and applied studies in the past two
decades, little is known about the reactive vapor phase, leading to
inconsistent treatment of the initiation process in the existing literature.
Di-tert-butyl peroxide (TBPO) is commonly used as
an initiator in iCVD by leveraging radical intermediates produced
during thermal decomposition. Despite its widespread use, no models
exist for TBPO decomposition in iCVD. To bridge this knowledge gap,
we integrated the Pirani pressure gauge into the iCVD setup to measure
the real-time vapor-phase composition in the reactor. After establishing
the relationship between the Pirani gauge pressure and composition
from batch data, we use it to quantify the fractional conversion of
pure TBPO in the reactor in the continuous mode. We find that under
iCVD conditions, TBPO fully decomposes to acetone and ethane following
a first-order Arrhenius kinetics. This means that (i) the partial
pressures of radicals are small (below the detection limit of the
Pirani gauge) and (ii) there is a stoichiometric increase in the number
of gas molecules in the reactor, which has not been accounted for
in existing models. This causes the overestimation of monomer pressure,
which is a key parameter in the current understanding of iCVD. We
analyze the decomposition of TBPO in the presence of cyclohexyl methacrylate
(CHMA) monomer suggesting that the monomer does not react appreciably
in the vapor phase. To show how this model of the vapor phase is related
to the deposition kinetics, we compare our data to the classical linear
polymerization theory, which describes free radical polymerization
of CHMA in solution and finds an acceptable fit. Notably, in Arrhenius
plots of the deposition rate, there is a well-documented but unexplained
decrease in the apparent activation energy at high filament temperature
(>300 °C), which is predicted by our models.