Provide the complete and detailed calculation of the Material Balance of the Distillation Column equipment below CW= 1425 kg/he 23 T= 350 K P= 1.66 atm T 350 K CHOH = 785.I1 04 kg/hr HO = 139 65 797 kg/hr 14 CHO =83. 144928 kg/ D-100 9. T= 358 K T338 K P= L8 atm H0=4858.21 kg/e T 355 K CH,O =8314.493 kghe P=1 66 am T=353 K CH,OH =7.9043S kg/h H0=9016 46l kg/hr

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
Section: Chapter Questions
Problem 1.1P
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Provide a material balance of each streams

Provide the complete and detailed calculation of the Material Balance of the Distillation
Column equipment below
CW= 1425 kg/he
23
T= 350 K
P= 1.66 atm
T 350 K
CHOH = 785.I1 04 kg/hr
HO = 139 65 797 kg/hr
14
CHO =83. 144928 kg/
D-100
9.
T= 358 K
T338 K
P= L8 atm
H0=4858.21 kg/h
T35S K
P=1 66 am
CH,0 =8314,493 kg/hư
T=353 K
CH,OH =7.9043S kg/h
HO=9016 46l kg/hr
CHO =8231.34skghe
Transcribed Image Text:Provide the complete and detailed calculation of the Material Balance of the Distillation Column equipment below CW= 1425 kg/he 23 T= 350 K P= 1.66 atm T 350 K CHOH = 785.I1 04 kg/hr HO = 139 65 797 kg/hr 14 CHO =83. 144928 kg/ D-100 9. T= 358 K T338 K P= L8 atm H0=4858.21 kg/h T35S K P=1 66 am CH,0 =8314,493 kg/hư T=353 K CH,OH =7.9043S kg/h HO=9016 46l kg/hr CHO =8231.34skghe
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