Author:
Semenov I. A.,Ul’yanov B. A.,Dubrovskii D. A.,Kulov N. N.
Subject
General Chemical Engineering,General Chemistry
Reference22 articles.
1. Egoshi, N., Kawakami, H., and Asano, K., Heat and mass transfer model approach to prediction of separation performance of cryogenic air separation plant by packed columns with structured packing, J. Chem. Eng. Jpn., 2001, vol. 34, pp. 22–29.
2. Shchelkunov, B.I. and Ul’yanov, B.A., Gidravlika i massoobmen v tarel’chatykh rektifikatsionnykh apparatakh (Hydraulics and Mass Transfer in Tray Distillation Apparatuses), Irkutsk: Irkutsk. Gos. Tekh. Univ., 1997.
3. Elizarov V.I., Elizarov D.V., Merzlyakov S.A., D’akonov S.G. Calculating the number of actual separation stages in mass transfer columns, Theor. Found. Chem. Eng., 2012, vol. 46, pp. 567–575.
4. Laptev, A.G. and Danilov, V.A., Two-dimensional model of transfer processes on a bubble plate in multi-component rectification, J. Eng. Phys. Thermophys., 2003, vol. 76, pp. 819–825.
5. Ulyanov, B.A., Semenov, I.A., and Kulov, N.N., Efficiency of mass transfer trays with allowance made for nonequimolar counterdiffusion, Theor. Found. Chem. Eng., 2011, vol. 45, pp. 575–580.
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