A stirred tank blending process with a constant liquid holdup of 2m³ is used to blend two streams whose densities are both approximately 900 kg/m³. The density does not change during mixing a. Assume that the process has been operating for a long period of time with flow rates of w₁ = 500 kg/min and w₂= 200 kg/min, and feed compositions (mass fractions) of x₁ = 0.4 and x2 = 0.75. What is the steady state value x b. Suppose that w₁ changes suddenly from 500 to 400 kg/min and remains at the new value. Determine an expression for x (t) and plot it 23 c. Repeat part (b) for the case where w₂ (instead of w₁) changes suddenly from 200 to 100 kg/min and remains there d. Repeat part (c) for the case where x₁ suddenly changes from 0.4 to 0.6 e. For parts (c) and (d), plot the response x(t) and the normalized response, XN XN(t) = x(t) = x(0) x(∞) - x(0) Where x(0) is the initial steady-state value of x(t) and x(∞) is the final steady-state value which is different for each part Note: T = υρ W is the same for question c, d and e 29

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
Question
A stirred tank blending process with a constant liquid holdup
of 2m³ is used to blend two streams whose densities are both
approximately 900 kg/m³. The density does not change
during mixing
a. Assume that the process has been operating for a long
period of time with flow rates of w₁ = 500 kg/min and w₂=
200 kg/min, and feed compositions (mass fractions) of x₁ =
0.4 and x2 = 0.75. What is the steady state value x
b. Suppose that w₁ changes suddenly from 500 to 400 kg/min
and remains at the new value. Determine an expression for
x (t) and plot it
23
Transcribed Image Text:A stirred tank blending process with a constant liquid holdup of 2m³ is used to blend two streams whose densities are both approximately 900 kg/m³. The density does not change during mixing a. Assume that the process has been operating for a long period of time with flow rates of w₁ = 500 kg/min and w₂= 200 kg/min, and feed compositions (mass fractions) of x₁ = 0.4 and x2 = 0.75. What is the steady state value x b. Suppose that w₁ changes suddenly from 500 to 400 kg/min and remains at the new value. Determine an expression for x (t) and plot it 23
c. Repeat part (b) for the case where w₂ (instead of w₁)
changes suddenly from 200 to 100 kg/min and remains
there
d. Repeat part (c) for the case where x₁ suddenly changes
from 0.4 to 0.6
e. For parts (c) and (d), plot the response x(t) and the
normalized response, XN
XN(t)
=
x(t) = x(0)
x(∞) - x(0)
Where x(0) is the initial steady-state value of x(t) and x(∞)
is the final steady-state value which is different for each part
Note: T =
υρ
W
is the same for question c, d and e
29
Transcribed Image Text:c. Repeat part (b) for the case where w₂ (instead of w₁) changes suddenly from 200 to 100 kg/min and remains there d. Repeat part (c) for the case where x₁ suddenly changes from 0.4 to 0.6 e. For parts (c) and (d), plot the response x(t) and the normalized response, XN XN(t) = x(t) = x(0) x(∞) - x(0) Where x(0) is the initial steady-state value of x(t) and x(∞) is the final steady-state value which is different for each part Note: T = υρ W is the same for question c, d and e 29
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