Last Updated on Wed, 03 Apr 2013 In Eq. (14-83), QL = m3 liquid downflow/(h m weir length) and Af = fractional hole area based on active ('bubbling') area; for instance, Af = Ah/Aa. The Kister and Haas method can also be applied to valve trays, but the additional approximations reduce its data prediction accuracy for valve trays to within ±20 percent.

Design Manual Tray.pdf Free Download Here. 2013 Anniversary Reprint This is a reprint of the 1993 Sixth Edition of the Glitsch BALLAST™ Tray Design Manual. It contains information considered to be 2011 - Cooper Industries. BICSI Customer Owned Outside Plant Design Manual. Cable tray can be used for Inter-building. Other Business Interest Company Name Company Registration Number Capacity No of Nominal Shares Value of Shares Remuneration 28 Business Owner 4 Name Surname Capacity SA Citizenship Yes No ID Number Gender Male Female Population Group Asian Percentage Ownership Black Coloured Telephone Number Facsimile Number Mobile Number Fax To Email% Indian.

For valve trays, adaptations of Eqs. (14-81) to (14-84) are required: 4 x (area of opening of one fully open valve) wetted perimeter of opening of one fully open valve = no. Valves x (area of opening of one fully open valve) active (bubbling) area A correlation for valve tray entrainment flooding that has gained respect and popularity throughout the industry is the Glitsch 'Equation 13' (Glitsch, Inc., Ballast Tray Design Manual, 6th ed., 1993; available from Koch-Glitsch, Wichita, Kans.). This equation has been applied successfully for valve trays from different manufacturers, as well as for sieve trays with large fractional hole areas (12 to 15 percent). With tray spacings of 600 mm and higher, its flood prediction accuracy for valve trays has generally been within ±10 percent in the author's experience.

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The Glitsch correlation is%flood 100 0 -1.

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. [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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