A mathematical model of the dynamics of industrial distillation columns. Made numerous calculations on the computer. The influence of various disturbing factors on the transients in the columns. Specific recommendations on the use of the results in the synthesis of energy-efficient distillation process control systems under transient conditions.
математическая модель. динамика, система управления, ректификационная колонна, mathematical model. dynamics, control systems, distillation column
1. R.R. Gubaev, M.K. Gimaleev, A.K. Safi-ullina, Vestnik Kaz. tehnol. un-ta, 12, 111-114 (2012).
2. N.N. Ziyatdinov, N.Yu. Bogula, T.V. Lapteva, G.M. Ostrovskiy, Vestnik Kaz. tehnol. un-ta, 5, 118-123 (2011).
3. R.Rid, Dzh. Prausnic, T. Shervud, Svoystva gazov i zhidkostey, Himiya , Leningrad,1982. 592 s.
4. M.K. Gimaleev, E.Sh. Telyakov, Teor. osnovy him. tehnol., 20,4, 435-440 (1986).