“…The conventional values of drag and heat transfer coefficients must be corrected to account for various phenomena such as temperature gradients in the particle boundary layer (Pfender, 1999;Lee et al, 1985); noncontinuum effect (Knudsen effect) (Fauchais et al, 2008b;Lewis and Gauvin, 1973;Chen and Pfender, 1983a,b;Vardelle et al, 1997;Ganser, 1993;Chen and Ping, 1986a); vaporization effect (Vardelle et al, 1996); turbulence effect (Lee et al, 1985); particle shape effect, especially important for cold spray (Fukanuma et al, 2006) where particles do not melt; particle charging, which is no more negligible in VPS (Chen and Ping, 1986b); and thermophoresis effect, particularly for particles below 1 mm (Fauchais et al, 2008b). Chemical reactions between particles and ambient gas have also been considered with reactions due to diffusion (Vardelle et al, 1996) or convection (Neiser et al, 1998) and also reactions related to self-propagating high-temperature synthesis (Borisova and Borisov, 2008). Chemical reactions between particles and ambient gas have also been considered with reactions due to diffusion (Vardelle et al, 1996) or convection (Neiser et al, 1998) and also reactions related to self-propagating high-temperature synthesis (Borisova and Borisov, 2008).…”