Motaleby: Thank you very much for sharing, it is a very good reference. Could it be possible that you share the following papers please? Fluid Mechanics of Distillation Trays (I): Depth-Averaged Theory and One-Dimensional Flows Fred K. There is no law that demands that above a certain diameter you have to use 4-pass trays. 4-pass trays are difficult to design, so I suggest you first try 2-pass trays. Read also the good old Glitsch Ballast Tray Design Manual. Wohlhuterad, Osman A. Harriottc Separation Science and Technology Volume 30, Issue 7-9, 1995, pages 1219-1231 DOI:10.10 Fluid Mechanics of Distillation Trays (II): Prediction of Flow Fields on Some Practically Important Sieve Trays Osman A. Basarana & Fred K. Wohlhuterbc Separation Science and Technology Volume 30, Issue 7-9, 1995, pages 1233-1244 DOI:10.10 Than you very much. Last Updated on Thu, 01 Nov 2012| References: 1. Glitsch, Inc.,, Bulletin 4900, 6th ed., 1993. Available from, Wichita, Kans. Koch Engineering Co., Inc., Design Manual—Flexitray, Bulletin 960-1, Wichita, Kans., 1982. Nutter Engineering, Float Valve Design Manual, 1976. Available from Sulzer ChemTech, Tulsa, Okla. Lockett, Distillation Tray Fundamentals, Cambridge University Press, Cambridge, England, 1986. To convert lb/ft3 to kg/m3, multiply by 16.0. Kister, Distillation Design, copyright © 1992 by McGraw-Hill, Inc. Reprinted by permission. 14-33 Entrainment. Andy laverne chord substitutions torrents pdf. [Reprinted courtesy of Fractionation Research Inc. (FRI).] Fair (paper presented at the AIChE Annual Meeting, Chicago, 111., November 1996) correlated data for efficiency reduction due to the rise of entrainment near entrainment flood, getting ln v = A + BO + CO2 where O is the fractional approach to entrainment flood and A, B, and C are constants given by 0 0.
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