For the propylene-propane separation using distillation column, using the following thermodynamic properties and the relations given in the table, calculate: (a) the condenser duty, QC; (b) the reboiler duty, OR. Phase Enthalpy (h) Entropy (s) Flowrates Stream Feed (F) Overhead vapor (OV) Distillate (D) and Reflux (R) Bottoms (B) 15,528 28,400 13,456 15,239 kJ/kmol-K Kmol/h 3.28 25.68 -14.22 -2.45 268.8 L 178.2 108

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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For the propylene-propane separation using distillation column, using the following
thermodynamic properties and the relations given in the table, calculate:
(a) the condenser duty, QC;
(b) the reboiler duty, OR.
Phase Enthalpy (h) Entropy (s) Flowrates
Stream
Feed (F)
Overhead vapor (OV)
Distillate (D) and Reflux (R)
Bottoms (B)
15,528
28,400
13,456
15,239
kJ/kmol-K Kmol/h
3.28
25.68
-14.22
-2.45
268.8
L
178.2
108
Transcribed Image Text:For the propylene-propane separation using distillation column, using the following thermodynamic properties and the relations given in the table, calculate: (a) the condenser duty, QC; (b) the reboiler duty, OR. Phase Enthalpy (h) Entropy (s) Flowrates Stream Feed (F) Overhead vapor (OV) Distillate (D) and Reflux (R) Bottoms (B) 15,528 28,400 13,456 15,239 kJ/kmol-K Kmol/h 3.28 25.68 -14.22 -2.45 268.8 L 178.2 108
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