Efficiency-based nonequilibrium modeling of industrial-scale multicomponent distillation columns

References

• Krishna, R.; Kooijman, R.; Taylor, H.A. (2003) Modeling of distillation. Chemical Engineering Progress, 99: 28.
   Web of Science ®Google Scholar
• Khoury, F.M. (2005) Multistage Separation Processes; CRC Press: New York.
   Google Scholar
• Waggoner, R.C.; Loud, G.D. (1977) Algorithms for the solution of material balance equations for non-conventional multi-stage operations. Computers and Chemical Engineering, 1: 49–56.
   Web of Science ®Google Scholar
• Klemola, K.; Ilme, J. (1996) Distillation efficiencies of an industrial-scale i-butane/n-butane fractionator. Industrial & Engineering Chemistry Research, 35: 4579–4586.
   Web of Science ®Google Scholar
• Klemola, K.; Aittamaa, J.; Nystrom, L.; Ilme, J. (2001) Calculating distillation efficiencies of multicomponent i-Butane/n-Butane column. Chemical Engineering Communications, 184: 1–21.
   Web of Science ®Google Scholar
• Biddulph, M.W. (1977) Deducing multicomponent distillation efficiencies from industrial data. Chemical Engineering, 14 (7): 7–15.
   Google Scholar
• Aittamaa, J. (1981) Estimating multicomponent plate efficiencies in distillation. Kemia-Kemi, 8: 295.
   Google Scholar
• Ilme, J. (1997) Estimating plate efficiencies in simulation of industrial scale distillation columns, Ph.D. Thesis, Lappeenranta University of Technology, Finland.
   Google Scholar
• Klemola, K. (1998) Efficiencies in distillation and reactive distillation. Acta Polytechnica Scandinavica, Chemical Technology Series, Finnish Academy of Technology, 257.
   Google Scholar
• Jakobsson, K.; Aittamaa, J. (2001) Comparison of plate efficiency estimation models to experimental results of pilot scale: a case study. Separation Technology (pp. 98–103). AIChE Annual Meeting.
   Google Scholar
• Ilme, J.; Keskinen, K.; Markanen, V.; Aittamaa, J. (2002) Simulation of industrial multicomponent MTBE distillation column using an equilibrium stage model with efficiency calculation. Distillation & Absorption. Institution of Chemical Engineers, Symposium Series.
   Google Scholar
• Jakobsson, K.; Aittamaa, J.; Keskinen, K.I.; Ilme, J. (2002) Plate efficiencies of industrial scale dehexanizer. Baden-Baden, Distillation & Absorption Conference, Germany.
   Google Scholar
• Henley, E.J.; Roper, D.K.; Seader, J.D. (2011) Separation Process Principles, Chemical and Biochemical Operations. John Wiley: New York.
   Google Scholar
• Murphree, E. (1925) Rectifying column calculations with particular reference to n-component mixtures. Industrial & Engineering Chemistry, 17: 747–750.
   Google Scholar
• Rahimi, M.R.; Karimi, H. (2011) Modeling distillation mass transfer efficiency. International Journal of Chemical and Environmental Engineering, 2 (3): 1–3.
   Google Scholar
• Jakobsson, K. (2005) Modeling and Simulation of Process Configurations Combining Distillation and Reaction, Chemical engineering report series. Espoo: Kemian laitetekniikan raporttisarja, No. 47.
   Google Scholar
• Taylor, R.; Krishna, R. (1993) Multicomponent Mass Transfer, 1st edn; John Wiley: New York.
   Google Scholar
• Durbin, L.; Holland, C.; Welch, N. (1964) Mixing on valve trays and in downcomers of a distillation column. AIChE, 10, 373.
   Web of Science ®Google Scholar
• O’Connel, M.; Gautreaux, H. (1955) Effect of length of liquid path on plate efficiency. Chemical Engineering Progress, 51: 232–237.
   Google Scholar
• Haselden, M.J.; Ashley, G.G. (1970) The calculation of plate efficiency under conditions of finite mixing in both phases in multiplate columns, and the potential advantage of parallel flow. Chemical Engineering Science, 25: 1665.
   Web of Science ®Google Scholar
• Kister, H. (1992) Distillation Design; McGraw-Hill: New York.
   Google Scholar
• AIChE. (1958) Bubble Tray Design Manual: Prediction of Fractionation Efficiency; AIChE: New York.
   Google Scholar
• Fair, H.; Chan, J.R. (1984a) Prediction of point efficiencies on sieve trays: 1. Binary systems. Industrial & Engineering Chemistry Process Design and Development, 23: 814–819.
   Web of Science ®Google Scholar
• Fair, H.; Chan, J.R. (1984b) Prediction of point efficiencies on sieve trays: 2. Multicomponent systems. Industrial & Engineering Chemistry Process Design and Development, 23: 820–827.
   Web of Science ®Google Scholar
• Bennett, D.L.; Agrawal, R.; Cook, P.J. (1983) New pressure drop correlation for sieve tray distillation columns. AIChE, 29 (3): 434–442.
   Web of Science ®Google Scholar
• Fujiwara, K.; Nakata, T.; Okamoto, N. (1993) Method foe determining relaxation factor for modified Newton-Raphson method. IEEE Transaction on Magnetics, 29 (2): 1962–1965.
   Web of Science ®Google Scholar
• Naphtali, L.M.; Sandholm, D.P. (1971) Multicomponent separation calculations by linearization. AIChE, 17 (1): 148–153.
   Web of Science ®Google Scholar
• Danesh, A. (1998) PVT Behavior of Petroleum Reservoir Fluids. Heriot Watt University, Elsevier: New York.
   Google Scholar
• Reid, R.C. (1987) The Properties of Gases and Liquids, 4th edn; McGraw-Hill, Inc: New York.
   Google Scholar