contains 5 mol y Ntz and its to 0.3 moly. at 293K gas stream monia content is reduced absorphion tower packed 1.013 X10S pa. a. The inkt pure ملعد wałe ow is 63 Kg mol/h and he szkg mol/h, The 0.75m. The intet ges flow is diameter coffichent mo! film 0.0739 kg wer is mass K ya P and %3D are 1/s.m3. fraction. mo !/ S.m3 . mol frachon. 0.169 Kg he design methode fox nture s, naz dilute ges tower helgh wstag 'ya towes helg hd usirg wlate he alati he
contains 5 mol y Ntz and its to 0.3 moly. at 293K gas stream monia content is reduced absorphion tower packed 1.013 X10S pa. a. The inkt pure ملعد wałe ow is 63 Kg mol/h and he szkg mol/h, The 0.75m. The intet ges flow is diameter coffichent mo! film 0.0739 kg wer is mass K ya P and %3D are 1/s.m3. fraction. mo !/ S.m3 . mol frachon. 0.169 Kg he design methode fox nture s, naz dilute ges tower helgh wstag 'ya towes helg hd usirg wlate he alati he
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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Transcribed Image Text:A
Contains S mol y Ntz cund its
0.3 moly
gas.
stream
ammonia
content
is
اععبيلعر
to
packed
absorp hion
at 293K
in
tower
pure wałer
he
X10s Pa .
inlt
لعدبا
1.013
The
Flow
to tal
63 kg
mol/ h
and
is
szkg mol/h, The
0.75m. The
k ya
$ and
mol fracton.
fox
intet
ges flow is
diameter
is
rower
film
mass
mansfes
mol /s.m3
= 0.169 Ka mo l/ sim3. mol fracHon.
cofficlent
0.0739kg
are
mol
fraction.
K'na =
0.169 kg
design methade
a
dilute gas
minture s,
Calculate
Calculate
tower helgh
using 'ya
me
he
tower
helyht using k'ya
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