A three-dimensional CP-DNS of a reacting dust cloud consisting of monodispersed iron particles in a turbulent mixing layer is conducted [1].
Left: Three-dimensional computational domain with gas velocity contour and iron particles coloured by their oxidation progress (black: non-oxidised, white: fully-oxidised). Right: Time evolution of gas temperature + particles coloured by their oxidation progress (top), oxygen mass fraction (middle) and flow vorticity (bottom) in the x-y plane at Lz/2.
The upper stream of the mixing layer is initialised with cold iron particles with a uniform diameter of 10 micron suspended in air, while the lower stream consists of hot air flowing in the opposite direction. As time progresses, turbulent mixing entrains particles from the upper to the lower stream. These particles interact with the lower stream, heat up and begin their oxidation process. When the particles reach a critical temperature, they start to ignite and burn, as can be observed from the local decrease of oxygen and increase of gas temperature.
The number of computational cells for the CP-DNS is ~85 million, ~5 million particles are used and the computational cost corresponds to ~165,225 CPUh. This study shows that the major differences between non-volatile iron flames and volatile-containing solid fuel flames (e.g. coal/biomass) are non-vanishing particles at late simulation times and a stronger limiting effect of the local oxygen concentration on the overall conversion process in iron dust flames [1].