Unit Operations of Chemical Engineering
Unit Operations of Chemical Engineering
7th Edition
ISBN: 9780072848236
Author: Warren McCabe, Julian C. Smith, Peter Harriott
Publisher: McGraw-Hill Companies, The
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Chapter 12, Problem 12.3P
Interpretation Introduction

Interpretation:

The overall heat transfer coefficient based on the inside area of the pipe and the heat flux based on the outside area is to be calculated.

Concept introduction:

The heat transfer coefficient is calculated using an appropriate Nusselt correlation.

For high Reynolds number in the straight round tubes and pipes, the following correlation is used to calculate the heat transfer coefficient:

  hi=0.023Re0.2Pr2/3CpG

The overall heat transfer coefficient based on the inside area of the pipe is calculated using the following equation:

  Ui=11/hi+xw/kmDiDL+1/hoDiDo

The relationship between overall heat transfer coefficient based on inside and outside area is given by the following expression:

  UoDo=UiDi

The heat flux based on the outside area is calculated using the following equation:

  qA=UoT1T2

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Chapter 12 Solutions

Unit Operations of Chemical Engineering

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Unit Operations of Chemical Engineering
Chemical Engineering
ISBN:9780072848236
Author:Warren McCabe, Julian C. Smith, Peter Harriott
Publisher:McGraw-Hill Companies, The