# 947 00110000672 for montz n rev 8400045900688

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Unformatted text preview: (1), for NOR PAC, with hL = 0.0162 m3/m3 and liquid Froude number = 6.63x10-5 P 0.947 - 0.0162 = 0.0113 lT 0.947 1.5 exp 1/ 2 13300 6.63 10 -5 ) = 0.0126 psi/ft 3/ 2 ( 86.8 Exercise 7.52 (continued) Analysis: (e) Rectifying section (continued) From Eq. (1), for Montz, with hL = 0.0241 m3/m3 and liquid Froude number =9.91x10-5 P 0.930 - 0.0241 = 0.0163 lT 0.930 1.5 exp 1/ 2 13300 9.91 10-5 ) = 0.0161 psi/ft 3/ 2 ( 300 Stripping section of the column: For NOR PAC , column diameter = DT = 3.4 ft 1 2 1 DP 2 1 0.012 From Eq. (6-111), = 1+ = 1+ = 1044 . KW 3 1 - DT 3 1 - 0.947 3.4 Therefore, KW = 1/1.044 = 0.957 For Montz, column diameter = DT = 4.2 ft 1 2 1 DP 2 1 0.00459 From Eq. (6-102), = 1+ = 1+ = 1010 . KW 3 1 - DT 3 1 - 0.930 4.2 Therefore, KW = 1/1.010 = 0.990 Superficial gas velocity at 70% of flooding from above = 20 ft/s for NOR PAC. Superficial gas velocity at 70% of flooding from above = 13 ft/s for Montz Gas viscosity = 0.012 cP and gas density = 0.0370 lb/ft3. From Eq. (6-114), for NOR PAC, N ReV = uV DP V (20)(0.012)(0.03...
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## This note was uploaded on 09/08/2008 for the course CHE 244 taught by Professor Selebi during the Spring '06 term at Lehigh University .

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