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
Question
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Chapter 6, Problem 6.1P
Interpretation Introduction

Interpretation: The maximum length of the pipe for different inlet conditions is to be determined.

Concept introduction: The length between the starting and the end point of a pipe is known as the maximum length of the pipe. The maximum length for a given Mach number is given as,

  f ¯ LmaxrH=1γ(1Maa2-1-γ+12ln2{1+[(γ-1)/2]Maa2}Maa2(γ+1)) ....... (1)

The notations used here are,

  Maa = Mach number at the entrance of the pipe

  Lmax = Maximum length of the pipe

  rH = Hydraulic radius of pipe = D4

  γ = Heat capacity ratio

  f ¯ = Average friction factor

The Reynolds number is given as,

  Re = GDμ ....... (2)

The notations used here are,

G = Gas Mass velocity

D = Diameter of pipe

  μ = Viscosity of the fluid

The Mach number is given as,

  Ma=ua=SpeedoffluidSpeedofsound ....... (3)

The speed of sound is given as,

  a=γRTM ....... (4)

M = Molecular weight of the air

R = Universal gas constant

T = Temperature of the air

Expert Solution & Answer
Check Mark

Answer to Problem 6.1P

The maximum length for the inlet conditions of example 6.2 is 2383 ft and the maximum length for the inlet conditions of example 6.3 is 83.17 m.

Explanation of Solution

The data from example 6.2 are,

  G=61.61 lb/ft2.s .

  f ¯ LmaxrH=280 ....... (5)

The data for air at 540°F

  μ=2.8×10-5 Pa-s = 0.028 cP

  D=2 inch1 inch = 112ftD=212ft=0.1667ft

Substitute the value in equation (2),

  Re=(61.61lb/ft2.s)×(0.1667ft)(0.028cP)×(6.72×10-4)=5.46×105

Corresponding to the given Reynolds number the value of f = 0.0049 from chart of Re vs f.

f = f ¯ = 0.0049

rH = 0.1667ft4=0.0417ft

Substitute these values in equation (5),

  (0.0049)×Lmax(0.0417ft)=280Lmax=280×0.0417ft0.0049=2383ft

The data for the air is,

  M=0.029kg/molR=8.314J/mol.KT=288Kγ=1.4

Substitute these values in equation (4),

  a=(1.4)×8.314J/mol.K×288K0.029kg/mola=340m/s

From example 6.3, the data useful is,

  q=0.265m3/sA=0.00442m2u=qA=0.265m3/s0.00442m2=60m/s

Substitute the value of u and a in equation (3),

  Ma=60m/s340m/s=0.176

Other data from example 6.3,

  f=f ¯=0.0044rH=0.01875m

Substitute the data in equation (1),

  (0.0044)Lmax(0.01875m)=11.4(1(0.176)2-1-1.4+12ln2{1+[(1.4-1)/2](0.176)2}(0.176)2(1.4+1))(0.0044)Lmax(0.01875m)=0.7143(32.283-1-1.2ln2.01240.0743)(0.0044)Lmax(0.01875m)=19.517Lmax=(0.01875m)(0.0044)×19.517Lmax=83.17m

Conclusion

The maximum length for the inlet conditions of example 6.2 is 2383 ft and the maximum length for the inlet conditions of example 6.3 is 83.17 m.

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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