“…The mathematical models are mass and heat balance equations incorporated with kinetic expressions of physical and chemical phenomena, which includes evaporation and condensation of pellet moisture, oxidation of magnetite, combustion of coke breeze, calcination of lime or dolomite, pellet shrinkage, etc. Rotary kilns are ubiquitous fixtures of the metallurgical and chemical process industries, the mathematical models of rotary kiln generally involve solid motion (Boateng and Barr, 1996;Puyvelde, 2006), heat transfer (Barr et al, 1989;Senegacnik et al, 2007;Shi et al, 2008;Tomaz and Filho, 1999), kinetics of chemical reactions such as pyrolysis, calcination, solid clinkering (Mujumdar et al, 2007;Ortiz et al, 2005;Patisson et al, 2000a) and fuel combustion. Similarly, overall model of rotary kiln is established via mass and heat balance equations, as reported in Marias (2003), Mujumdar and Ranade (2006), and Patisson et al (2000b).…”