[1] J. Rizk,M. Nemer, D. Clodic, A real column design exergy optimization of a cryogenicair separation unit, Energy 37 (1) (2012) 417-429.[2] L. Spieel, W. Meier, Distillation columns with structured packings in the nextdecade, Trans. IChemE. 81 (2003) 39-47 (Part A).[3] C.F. Petre, F. Larachi, I. Iliuta, B.P.A. Grandjean, Pressure drop through structuredpackings: breakdown into the contributing mechanisms by CFD modeling, Chem.Eng. Sci. 58 (2003) 163-177.[4] S. Bian, M.A. Henson, P. Belanger, L. Megan, Nonlinear state estimation and modelpredictive control of nitrogen purification columns, Ind. Eng. Chem. Res. 44 (1)(2005) 153-167.[5] J.Miller,W.L. Luyben, P. Belanger, S. Blouin, L.Megan, Improving agility of cryogenicair separation plants, Ind. Eng. Chem. Res. 47 (2) (2008) 394-404.[6] H.H. Song, Simulation of practical column, Distillation Simulation, Tianjin UniversityPress, Tianjin, 2005, pp. 156-171, (in Chinese).[7] R. Krishnamurthy, R. Taylor, A non-equilibrium stage model of multicomponentseparation processes, Part III: the influence of unequal component-efficiencies inprocess design problems, AIChE J. 31 (12) (1985) 1973-1985.[8] R. Krishnamurthy, R. Taylor, A non-equilibrium stage model of multicomponentseparation processes. Part I: model description and method of solution, AIChE J. 31(3) (1985) 449-456.[9] L. Chen, J.U. Repke, G. Wozny, S.Q.Wang, Extension of the mass transfer calculationfor three-phase distillation in a packed column: non-equilibrium model based parameterestimation, Ind. Eng. Chem. Res. 48 (15) (2009) 7289-7300.[10] J.D. Seader, E.J. Henley, Theoretical model for an equilibrium stage, Separation ProcessPrinciples, John Wiley & Sons, Inc., Hoboken, 2006, pp. 365-400.[11] H.H. Song,W.J. Zhang, Direct simulations of the column used in air separation, Cryo.Technol. 5 (1996) 19-24 (in Chinese).[12] S.H. Tang, Z.H. Wu, A hybrid simulation model for multicomponent distillation instructured packing column, Chem. Eng. (China) 35 (4) (2007) 1-4 (in Chinese).[13] F. Shen, J.H. Zhu, Preliminary study on the non-equilibrium model for the reactivedistillation process, Comput. Appl. Chem. 3 (1994) 167-173 (in Chinese).[14] E.W. Lemmon, M.L. Huber, M.O. McLinden, NIST Standard Reference Database 23:Reference Fluid Thermodynamic and Transport Properties—REFPROP, NationalInstitute of Standards and Technology, Standard Reference Data Program,Gaithersburg, 2010.[15] Z. Olujic, Development of a complete simulation model for predicting the hydraulicand separation performance of distillation columns equipped with structured packings,Chem. Biochem. Eng. Q. 11 (1) (1997) 31-46.[16] S. Ratheesh, A. Kannan, Holdup and pressure drop studies in structured packingswith catalysts, Chem. Eng. J. 104 (1-3) (2004) 45-54.[17] J.A. Rocha, J.L. Bravo, J.R. Fair, Distillation columns containing structured packings: acomprehensivemodel for their performance. 2. Mass-transfermodel, Ind. Eng. Chem.Res. 35 (5) (1996) 1660-1667.[18] B. Hanley, C.C. Chen, New mass-transfer correlations for packed towers, AIChE J. 58(1) (2012) 132-152.[19] R. Taylor, R. Krishna, Simultaneousmass and energy transfer,MulticomponentMassTransfer, Wiley, New York, USA, 1993, pp. 266-303 |