It is desired to reduce the 2% CO, in 23 Ib/sec of a natural gas stream using absorption in aqueous diethylamine flowing at 40 lb/sec. Either 1 ½ in. Raschig rings or 1 ½ in. Pall rings are being considered for packing. A pressure drop of 0.25 in H2O/ft is desired to minimize foaming. Under operating conditions, the densities of the gas and the liquid are 2.8 and 63 Ib/ft³, respectively; the liquid viscosity is 2 centistokes. "Determine the flooding velocity and the tower's cross-sectional area using the succeeding procedures

Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Chapter1: Introduction
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It is desired to reduce the 2% CO, in 23 lb/sec of a natural gas stream using
absorption in aqueous diethylamine flowing at 40 lb/sec. Either 1 ½ in.
Raschig rings or 1 ½ in. Pall rings are being considered for packing. A
pressure drop of 0.25 in H2O/ft is desired to minimize foaming. Under
operating conditions, the densities of the gas and the liquid are 2.8 and 63
Ib/ft³, respectively; the liquid viscosity is 2 centistokes.
"Determine the flooding velocity and the tower's cross-sectional area using
the succeeding procedures
Transcribed Image Text:It is desired to reduce the 2% CO, in 23 lb/sec of a natural gas stream using absorption in aqueous diethylamine flowing at 40 lb/sec. Either 1 ½ in. Raschig rings or 1 ½ in. Pall rings are being considered for packing. A pressure drop of 0.25 in H2O/ft is desired to minimize foaming. Under operating conditions, the densities of the gas and the liquid are 2.8 and 63 Ib/ft³, respectively; the liquid viscosity is 2 centistokes. "Determine the flooding velocity and the tower's cross-sectional area using the succeeding procedures
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