A process stream contains species 1 and species 2. A relatively pure liquid stream containing mostly species 2 is obtained by a single-stage liquid/vapor separation unit. Specifications on the equilibrium compasitions are x-=0.02 and y=0.950. Use the data given below to determine T(K) and P(bar) for the separator. Iny, = 0,93x3 |Inyy0.93x7 InPpat (bar) =A T(K) A1=10.08 B=2572.0 and A2=11.63 B-6254 489.6 K; 0.24 bar Ob. 240.6 K; 5.3 bar Oc. 890 K; 2.4 bar d. 120 K; 1.66 bar 10509142007 4705
A process stream contains species 1 and species 2. A relatively pure liquid stream containing mostly species 2 is obtained by a single-stage liquid/vapor separation unit. Specifications on the equilibrium compasitions are x-=0.02 and y=0.950. Use the data given below to determine T(K) and P(bar) for the separator. Iny, = 0,93x3 |Inyy0.93x7 InPpat (bar) =A T(K) A1=10.08 B=2572.0 and A2=11.63 B-6254 489.6 K; 0.24 bar Ob. 240.6 K; 5.3 bar Oc. 890 K; 2.4 bar d. 120 K; 1.66 bar 10509142007 4705
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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A process stream contains species 1 and species 2. A relatively pure liquid stream containing mostly species 2 is obtained by a
single-stage liquid/vapor separation unit. Specifications on the equilibrium compositions are x=0.02 and y=0.950. Use the data
given below to determine T(K) and P(bar) for the separator.
Iny = 0.93x3
lny0.93x
InPat (bar) =A
T(KY
A1=10.08 Bj=2572.0 and A2=11,63 B 6254
Oa.
489.6 K; 0.24 bar
O b. 240.6 K; 5.3 bar
890 K; 2.4 bar
Od. 120 K; 1.66 bar
10509142007-4705
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