“…(𝐿 0 (𝑖 0 (𝑡) + 𝑖 2 (𝑡) − 𝑖 1 (𝑡) − 𝑖 3 (𝑡)) + 𝑞 с.э (𝑡)𝐹 т.п 𝜀 + 𝑘𝐹𝑇 о.с (𝑡))𝑑𝑡 − 𝑘𝐹(𝑎 а 𝑇 2 + 𝑏 а )𝑑𝑡 = 0 (12) For functions i0(t), i1(t), i2(t), i3(t), qc.э(t), Tо.с(t) and T2(t) it is known that: 𝑖 0 (𝑡) = С 𝑐.в 𝑇 о.с (𝑡) + 0,001𝑥 н (𝑟 0 + С п 𝑇 о.с (𝑡)), (13) 𝑖 1 (𝑡) = С 𝑐.в 𝑇 1 (𝑡) + 0,001𝑥 н (𝑟 0 + С п 𝑇 1 (𝑡)), (14) 𝑖 2 (𝑡) = С 𝑐.в 𝑇 2 + 0,001𝑥 к (𝑟 0 + С п 𝑇 2 ), (15) 𝑖 3 (𝑡) = С 𝑐.в 𝑇 3 (𝑡) + 0,001𝑥 к (𝑟 0 + С п 𝑇 3 (𝑡)), (16) where: Сс.в -heat capacity of dry air, kJ/(kg К); xн, xк -correspondingly, initial and final moisture content of the drying agent, g/kg; r0 -specific heat of vaporization at temperature 0 0 С; Cп -heat capacity of vapor, kJ/(kg К); 𝑇 1 -temperature of the drying agent at the inlet to the dryer, К; 𝑇 3 -temperature of the spent drying agent at the outlet of the combined heat exchanger, К.…”