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VETOH 1 0.95 0.9 0.85 0.8 0.75 0.7 0.65 0.6 0.55 0.5 0.45 0.4 0.35 0.3 0.25 0.2 0.15 0.1 0.05 0 0 0.05 0.1 0.15 0.2 0.25 0.3 0.35 0.4 0.45 0.5 0.55 0.6 0.65 0.7 0.75 0.8 0.85 0.9 0.95 1 ΧΕΤΟΗ

VETOH 1 0.95 0.9 0.85 0.8 0.75 0.7 0.65 0.6 0.55 0.5 0.45 0.4 0.35 0.3 0.25 0.2 0.15 0.1 0.05 0 0 0.05 0.1 0.15 0.2 0.25 0.3 0.35 0.4 0.45 0.5 0.55 0.6 0.65 0.7 0.75 0.8 0.85 0.9 0.95 1 ΧΕΤΟΗ

Refrigeration and Air Conditioning Technology (MindTap Course List)
Refrigeration and Air Conditioning Technology (MindTap Course List)
8th Edition
ISBN:9781305578296
Author:John Tomczyk, Eugene Silberstein, Bill Whitman, Bill Johnson
Publisher:John Tomczyk, Eugene Silberstein, Bill Whitman, Bill Johnson
Chapter1: Heat, Temperature, And Pressure
Section: Chapter Questions
Problem 17RQ: Convert 22C to Fahrenheit.
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A distillation column with a total condenser and a partial reboiler is separating ethanol and
water at 1.0 atm. Feed is 0.32 mol fraction ethanol and it enters as a saturated liquid at 100
mol/s on the optimum plate. The distillate product is a saturated liquid with 80 mol% ethanol.
The condenser removes 5615 kW. The bottoms product is 0.05 mol fraction ethanol. Assume
CMO is valid.
(a) Find the number of equilibrium stages for this separation. [6 + PR]
(b) Find how much larger the actual reflux ratio, R, used is than Rmin, i.e. R/Rmin. [3]
Note: the heats of vaporization of ethanol and water are λe = 38.58 ௞௃
௠௢௟ and λw = 40.645 ௞௃
௠௢௟

VETOH 1 0.95 0.9 0.85 0.8 0.75 0.7 0.65 0.6 0.55 0.5 0.45 0.4 0.35 0.3 0.25 0.2 0.15 0.1 0.05 0 0 0.05 0.1 0.15 0.2 0.25 0.3 0.35 0.4 0.45 0.5 0.55 0.6 0.65 0.7 0.75 0.8 0.85 0.9 0.95 1 ΧΕΤΟΗ
Transcribed Image Text:VETOH 1 0.95 0.9 0.85 0.8 0.75 0.7 0.65 0.6 0.55 0.5 0.45 0.4 0.35 0.3 0.25 0.2 0.15 0.1 0.05 0 0 0.05 0.1 0.15 0.2 0.25 0.3 0.35 0.4 0.45 0.5 0.55 0.6 0.65 0.7 0.75 0.8 0.85 0.9 0.95 1 ΧΕΤΟΗ
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