On the basis of the serial output and analysis of integral equations of diffusion boundary layer for the gas phase system of gas (steam) - liquid justifies-the structure of the equation returns the masses, which is based on the allocation of a process to a specific standard conditions (equimolar process) and differs from known phenomenological equations of the presence of additional members, taking into account the effect on the mass transfer of the resulting mass flow through the surface of the phase. Justice of the equation is confirmed by the analysis of the known experiment-experimental data.
Многокомпонентная диффузия, массоотдача и массопередача, гетерофазная система, математическое описание, Multicomponent diffusion, returns the masses and the transfer of the masses, heterophase system, the mathematical description of
1. V.V.Kafarov, Osnovy massoperedachi. M.: Vysshaya shkola, 1972, S.494.
2. V.M.Ramm Absorbciya gazov. M.:Himiya, 1971, S.767.
3. Kachalova T.N., Kachalova L.I. Modernizaciya uzla gidrirovaniya etan-etilenovoy frakcii // Vestnik Kazan. tehnol un-ta, - 2012, №10, S.230.
4. Toor H.L. Diffusion in three-component gas mixtures // AIChE Journal. 1957. V. 3. № 2. R. 198.
5. Telyakov E.Sh., Nizamov I.I., Tarenko B.I., Bikmurzin A.R. Eksperimental'no-raschetnoe issledovanie mnogokomponentnoy diffuzii v gazovyh smesyah // Butlerovskie soobscheniya. - 2011. - T.27. - № 15. - S.71-79.
6. Lapteva T.V., Ziyatdinov N.N., Pervuhin D.D. Effektivnost' raboty metodov resheniya zadachi proektirovaniya rabotosposobnyh HTS // Vestnik Kazan. tehnol un-ta, - 2012, №11, S.268-271.
7. V.P.Isachenko, V.A.Osipova, A.S.Sukomel. Teploperedacha, Moskva, Energoizdat, 1981, S.416.
8. K. F. Pavlov, P. G. Romankov, A.A. Noskov Primery i zadachi po kursu proces-sov i apparatov himicheskoy tehnologii. Izd. 10-e, per. i dop. L., Himiya,1987. - S.576.
9. I.A. Aleksandrov Massoperedacha pri rektifikacii i absorbcii mnogokomponentnyh smesey. L.: Himiya, 1975, s.320.
10. Konstantinov E.N., Nikolaev A.M. Massoperedacha pri rektifikacii mnogokomponentnyh smesey // Izvestiya VUZov, Neft' i gaz. 1964. № 1. S. 53.
11. Osipova L.E., Telyakov E.Sh., Nikolaev N.A. Modelirovanie neekvimolyarnyh processov masso- i teploperenosa v sistemah gaz (par) - zhidkost' // Teoret. osnovy him. tehnologii. 1997. T. 31, № 3, S. 274.
12. Lothov V.A., Malyusov V.A., Zhavoronkov N.M. Opredelenie fazovyh soprotivleniy v processe plenochnoy rektifikacii po profilyu koncentraciy. Laminarnyy potok para. Teoret. osnovy him. tehnol., 1967, t.1, №3, s.319-322.
13. Konstantinov E.N., Kuznechikov V.A. Matematicheskaya model' turbulentnogo massoobmena v mnogokomponentnoy smesi. Teoret. osnovy him. tehnol., 1975, t.9, №2, s.163-169.
14. Von Krevelen D.W., Hoftijzer P.J. Studies of gas absorption: mass transfer in a film reactors (wetted wall columns). Rec. Trav. Chem., 1949, v.68, №4, p. 221-242/
15. Boyarchuk P.G. Issledovanie kinetiki massoobmena v rektifikacionnyh apparatah plenochnogo tipa. Diss…. kand. tehnicheskih nauk, M.: MIHM, 1963, S.164.
16. Telyakov E.Sh., Nikolaev A.M. Sposob opredeleniya chastnyh vysot edinic perenosa v processe rektifikacii. Teoret. osnovy him. tehnol., 1969, t.3, №6, s.826-830.
