Elementary Principles of Chemical Processes, Binder Ready Version
Elementary Principles of Chemical Processes, Binder Ready Version
4th Edition
ISBN: 9781118431221
Author: Richard M. Felder, Ronald W. Rousseau, Lisa G. Bullard
Publisher: WILEY
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Chapter 10, Problem 10.6P
Interpretation Introduction

(a)

Interpretation:

The time taken for benzene to reach the desired point should be calculated.

Concept introduction:

The relation between mass, volume and density is as follows:

m=Vρ

In terms of mass rate, it is written as follows:

m˙=Vtρ

Rearranging,

t=Vm˙ρ

The volume can be calculated using the following formula:

V=πr2L2

Interpretation Introduction

(b)

Interpretation:

Suppose the flowrate into the tank is unknown. A sight gauge on the tank allows determination of the liquid level, and instructions are to stop the flow when the tank contains 3000kg. The value of h at which this needs to be done should be calculated.

Concept introduction:

The relation between mass, volume and density is as follows:

m=Vρ

In terms of mass rate, it is written as follows:

m˙=Vtρ

Rearranging,

t=Vm˙ρ

The volume can be calculated using the following formula:

V=πr2L2

Interpretation Introduction

(c)

Interpretation:

The flowrate into the tank should be estimated when h has an approximate value of 50 cm, and (dh/dt) =1cm/min.

Concept introduction:

Mass balance equation is as follows:

Accumulation= Input – Output + Generation – Consumption

Chain rule is as follows:

dVdt=dVdh×dhdt

Interpretation Introduction

(d)

Interpretation:

To explain the reason for the drum to provide better performance than feeding a signal proportional to the flowrate directly to the control valve that would cause the valve to close if the flowrate drops below the set point and to open if the flowrates rises above that point.

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Q. VI: An equimolar liquid mixture of benzene and toluene is separated into two product streams by distillation. At each point in the column some of the liquid vaporizes and some of the vapor stream condenses. The vapor leaving the top of the column, which contains 97 mole% benzene, is completely condensed and split into two equal fractions: one is taken off as the overhead product stream, and the other (the reflux) is recycled to the top of the column. The overhead product stream contains 89.2% of the benzene fed to the column. The liquid leaving the bottom of the column is fed to a partial reboiler in which 45% of it is vaporized. The vapor generated in the reboiler (the boilup) is recycled to become the rising vapor stream in the column, and the residual reboiler liquid is taken off as the bottom product stream. The compositions of the streams leaving the reboiler are governed by the relation, YB/(1 - YB) XB/(1 - XB) = 2.25 where YB and XB are the mole fractions of benzene in the…
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