IstoT S 9 S 1 S ba HHHH 0.9 0.30.412 0.5 0.60 0.78 0.8 w bns 8.0 evineb of vit jon ob :9ton) bebivorq noismotni odt gniau zoniladito Santwa1C Firenoitslen 9rit lis9.9vode bebivorq noitsmotni srit sau teplo neob ever sw (snil best or bus 250il grit 19go 9rt n99w Exulten Istot gnimu226 298612 to 19dmyn mumifin art 21 tsrW nitsiaqo si to sno to sqola srt of betalen zi oite XU2411] Soits XLEDoodi ei todW 6760 DI 14.7 psia 0 0.1 0.2 lonstud-Isnsxeriolavə 0 H 1-Pentene/1-Hexene 0.2 61019 0.3 felioder bris 192nsbnos Istot sy sve doy bluow 2vs11 16 10 vrism woh 6991 91 936ią uoy bluew ys11 jadw JA Sony no biupil ajouborq amottod bas uteib erit 91A * diw noiss16092 6 1 26 19 1619 0.5 0.6 0.7 3) CU M6 SCV 0.8 0.9 (c) At what tray is the feed placed? Is it above or below that tray? (b) What is the vapor and liquid molar fractions at the third tray? and bottom products a liquid or vapor? (a) How many actual trays are present if there is a partial condenser and reboiler? Are the top Based on the following figure, answer the following questions :

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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1. Based on the following figure, answer the following questions:
(a) How many actual trays are present if there is a partial condenser and reboiler? Are the top
and bottom products a liquid or vapor?
(b) What is the vapor and liquid molar fractions at the third tray?
(c) At what tray is the feed placed? Is it above or below that tray?
0.9
(8) Cau M6 9CU 0.8
1
0.7
026 91 169 0.5
0.3
w bns 8.0
zib ert 91A (1
* ddiw noiss16092 6
ng brúpil ajouborq amottod bns
0991 91 956iq uoy bluw vsi11 Jadw 1A (5
ved joy bluow eysti 1610 vrism woH (E
0.2
0 H
1-Pentene/1-Hexene
0.1 0.2
lonstud-Insxerolavə
felioder bris 192rebnes Ietet si
gritsego si to sno to sqola erit of betalen zi oite XU24110H] Soits Xoodi ai tsdW (
Exuften Istot gnimu226 298512 to 19dmyn mumițin orld 21 1sdW (
(snil best arly bys 250 grit 1990 erlt newt
girenoitalen ort lis39.⁹vods bobivorq noitemotni srit sau terý zelo nesmob ever sw s
odt gniau zonil ziro Sent w670
jevneb of vij jon ob :9ton) bebivorq noismotni
o xulo16 diw 20.0=
0.3 0.412
14.7 psia
0.5
To psto
ng aus
HHHHH
S bor
S bo
s bo
1
Sb
vb
3
2
q IstoT
0.60
0.78 0.8
0.9
OPDIE DOIS MG MSUL IO SCUIGAG SUX'=
Transcribed Image Text:1. Based on the following figure, answer the following questions: (a) How many actual trays are present if there is a partial condenser and reboiler? Are the top and bottom products a liquid or vapor? (b) What is the vapor and liquid molar fractions at the third tray? (c) At what tray is the feed placed? Is it above or below that tray? 0.9 (8) Cau M6 9CU 0.8 1 0.7 026 91 169 0.5 0.3 w bns 8.0 zib ert 91A (1 * ddiw noiss16092 6 ng brúpil ajouborq amottod bns 0991 91 956iq uoy bluw vsi11 Jadw 1A (5 ved joy bluow eysti 1610 vrism woH (E 0.2 0 H 1-Pentene/1-Hexene 0.1 0.2 lonstud-Insxerolavə felioder bris 192rebnes Ietet si gritsego si to sno to sqola erit of betalen zi oite XU24110H] Soits Xoodi ai tsdW ( Exuften Istot gnimu226 298512 to 19dmyn mumițin orld 21 1sdW ( (snil best arly bys 250 grit 1990 erlt newt girenoitalen ort lis39.⁹vods bobivorq noitemotni srit sau terý zelo nesmob ever sw s odt gniau zonil ziro Sent w670 jevneb of vij jon ob :9ton) bebivorq noismotni o xulo16 diw 20.0= 0.3 0.412 14.7 psia 0.5 To psto ng aus HHHHH S bor S bo s bo 1 Sb vb 3 2 q IstoT 0.60 0.78 0.8 0.9 OPDIE DOIS MG MSUL IO SCUIGAG SUX'=
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