Partially-premixed flames (PPF) can contain multiple reaction zones, e.g.,
one or two with a premixed-like structure and one being a nonpremixed react
ion zone. An intrinsic feature of partially premixed flames pertains to the
synergistic interactions between these two types of reaction zones that ar
e characterized by heat and mass transfer between them. Since these interac
tions are strongly dependent on the distribution of the radical and stable
species' concentrations, an accurate representation of the flame chemistry
involving these species is critical for simulating their behavior. The role
of C-1-chemistry in determining the structure of partially premixed methan
e-air flames is investigated herein by employing two relatively derailed ch
emical mechanisms. The first involves only C-1-containing species and consi
sts of 52 reactions involving 17 species, while the second mechanism repres
ents both C-1- and C-2-chemistry and consists of 81 reactions that involve
24 species. A planar two-dimensional partially premixed flame established o
n a rectangular slot burner is simulated. The simulation is based on the nu
merical solution of the time-dependent conservation equations for mass cont
inuity, momentum, species, and energy. The computations are validated by co
mparison with the experimentally-obtained chemiluminescent emission from ex
cited-C-2* free radical species, as well as with velocity measurements usin
g particle image velocimetry. A numerical study is then conducted to examin
e the applicability of C-1 and C-2 mechanisms for predicting the structure
of partially premixed flames for different levels of partial premixing and
reactant velocity. Results indicate that both the mechanisms reproduce the
global structure of PPF over a wide range of reactant velocity and stoichio
metry. Since the C-1 mechanism is known to be inadequate for fuel-rich prem
ixed flames, its relatively good performance can be attributed to the inter
actions between the two reaction zones that characterize the PPF structure.
There are, however, important quantitative differences between the predict
ions of the two mechanisms. The C-2 mechanism is overall superior compared
to the C-1 mechanism in that its predictions are in closer agreement with o
ur experimental results. The rich premixed reaction zone height obtained wi
th the C-2 mechanism is more sensitive to variations in the equivalence rat
io as compared with predictions that are obtained using the C-1-mechanism.
In addition, for high levels of partial premixing, the methane consumption
in the inner reaction zone is significantly increased when the C-2-mechanis
m is employed. compared to when the C-1-mechanism is used. Consequently, th
e amount of methane that leaks from the rich premixed to nonpremixed reacti
on zone is significantly lower when the C-2-mechanism is used. The interact
ions between the inner and outer reaction zones are stronger when the C-2-m
echanism is employed. Finally, the maximum temperature predicted by the C-2
-mechanism is slightly lower as compared to that obtained using the C-1-che
mistry alone. These differences are attributed to the presence of the C-2-c
hain in the 81-step mechanism, which strongly affects the inner premixed re
action zone.