“…To solve this problem, the following initial data were used [29,37]: c Ti = 528 J/(kgK), c s = c m = 462 J/(kgK), ρ Ti = 4500 kg/m 3 , ρ s = ρ m = 7900 kg/m 3 , Q = 5.8 × 10 5 , E = 141,510 J/mol, k 0 = 2.8 × 10 4 s −1 , M g = 28 × 10 −3 kg/mol, µ = 0.23, b = −0.17, ω/∑(v i c i ρ i ) = 70 K/min, V = 6 × 10 −2 m 3 , S = 0.72 m 2 . It was assumed that for the running mill the coefficient χ = 10 J/(s K m 2 ), and for the stop of the mill under forced cooling conditions χ = 1000 J/(s K m 2 ).…”