This paper describes
a novel reactor for acetylene synthesis by
high-temperature thermochemical conversion of paraffin hydrocarbons.
The reactor utilizes a conical annular swirling jet, which becomes
extremely thin as swirl intensifies. The small thickness provides
fast mass, momentum, and heat transfer to facilitate the rapid heating
and conversion of the reactants. We employ a unique wall shape for
the converging–diverging combustion zone, which maintains relatively
low reactor wall temperature and avoids the need for external cooling.
The wall shape and angle were derived from an approximate analytical
solution of the Navier–Stokes and energy equations, which leads
to the maximal jet flow rate and avoids wall separation under extreme
high swirling flow conditions. The analytical solution predicts a
high-speed swirling flow, which includes a thin annular conical diverging
jet where mass, momentum, and heat fluxes concentrate, and chemical
reactions can occur rapidly. Across the jet, the temperature sharply
drops from its large near-axis value to its small near-wall value.
We illustrate and study these features with the help of numerical
simulations of the Navier–Stokes, energy, and species equations
and proof-of-concept experiments. The experiments confirm the thin
annular conical shape of the flame, which is blue, transparent, and
well anchored near the throat. The present device produces a flow
pattern, which minimizes the reactor wall temperature, while producing
light olefins with high selectivity and conversion.