EBK INTRODUCTION TO CHEMICAL ENGINEERIN
EBK INTRODUCTION TO CHEMICAL ENGINEERIN
8th Edition
ISBN: 9781259878091
Author: SMITH
Publisher: MCGRAW HILL BOOK COMPANY
Question
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Chapter 7, Problem 7.57P

(A)

Interpretation Introduction

Interpretation:

The labeled flow diagram should be drawn.

Concept Introduction:

Hydrocarbon gas enters at 500 o C and it is combined with light oil at 25 o C.

The combined stream leaves at 200 o C

Hydrocarbon gas Temperature, T1=500 oC

Light oil Temperature, T2 = 25 oC

Exit Combined stream Temperature, T3= 200 oC

(B)

Interpretation Introduction

Interpretation:

D/F ratio should be determined.

Concept Introduction:

The general energy balance of the mixing process is given as below for an adiabatic vessel: -

  F.Cpgas.(T3T1)+D.[ΔHlv+CPoil.(T3T2)]=0

Where,

CPgas = Molar heat capacity of hydrocarbon gas=150 J/(mol.K)

CPoil = Molar heat capacity of light oil = 200 J/(mol.K)

R = Universal Gas Constant

T1 =Inlet temperature of Hydrocarbon gas = 500oC

T2 =Inlet temperature of Light oil = 25oC

T3 =Inlet temperature of Mixed stream = 200oC

  ΔH lv = Change in Enthalpy = 35000 J/mol at 25 oC

F = Molar feed rate of hydrogen gas

D = Molar feed rate of light oil

(c)

Interpretation Introduction

Interpretation:

To explain the advantage of using a liquid rather than cooler gas

Concept Introduction:

Quenching is defines as rapid cooling of a substance using a medium such as oil in this case.

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