Chemical Engineering - Process Equipment and Plant Design - Discussion
Discussion Forum : Process Equipment and Plant Design - Section 1 (Q.No. 15)
15.
Overall distillation column efficiency for most of the refinery columns can be given by (for μ = 0.07 - 1.4 cp and relative volatility < 4) (where η = overall column efficiency, % μ = molal average viscosity of feed at average column temperature and pressure, cp Δp = pressure drop per tray, psi)
η = 17 - 61.1 log μ
η = 1.66 - 0.25 log μ
η = 0.25 log μ - 1.67
Discussion:
3 comments Page 1 of 1.
Emi said:
4 months ago
How to calculate this? Anyone please explain.
Kamal said:
4 years ago
How to calculate this? Explain the solution.
(1)
S P said:
5 years ago
How did you calculate? Will you please explain to me?
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