Consider the horizontal V-L drum designed in Examples 23.4, 23.5, and 23.6. Based on the conditions at

Question:

Consider the horizontal V-L drum designed in Examples 23.4, 23.5, and 23.6. Based on the conditions at the operating design point (using NOL), determine the maximum size of gas bubble that would not rise to the liquid surface and be released to the vapor phase. Use a liquid viscosity of 700 × 10 kg/m/s.

Examples 23.4

Examples 23.5

Examples 23.6 Using the results from Examples 23.4 and 23.5, estimate the maximum size of droplet that will be entrained

Trajectory of falling droplet (2.5271.111)= 1.416 m NOL 1.111 m L-6.32 m Figure E23.6 Vessel sketch with

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Analysis Synthesis And Design Of Chemical Processes

ISBN: 9780134177403

5th Edition

Authors: Richard Turton, Joseph Shaeiwitz, Debangsu Bhattacharyya, Wallace Whiting

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Question Posted: Nov 09, 2023 02:00 AM

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Consider the horizontal V-L drum designed in Examples 23.4, 23.5, and 23.6. Based on the conditions at

Question:

Consider a horizontal drum used to separate a V-L mixture. The HHAL of the liquid is set at 0.8 Dves and the vapor and liquid properties are: P₁ = 1000 kg/m³, pg = 2.156 kg/m³, µg = 19.62 × 10¯ kg/m/s, vg = 3.865 m³/s. Determine the diameter of the drum, Dues.

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Analysis Synthesis And Design Of Chemical Processes

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