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 5, Problem 5.12P
Interpretation Introduction

Interpretation: The pressure drop in the power plant and the power required is to be determined.

Concept introduction: The change in pressure across a pipe due to smoothness or roughness is known as the pressure drop. The pressure drop is given as,

  P1-P2=ρhf ....... (1)

The notations used here are,

  hf = Friction head loss

  ρ = Density of the fluid

The power for the system is given as,

  P=ρhfQ ....... (2)

The notations used here are,

P = Power developed by the duct

Q = Flow rate by the duct

The Reynolds number is given as,

  Re = ρV¯Dμ ....... (3)

The notations used here are,

  V¯ = Average velocity of the fluid

D = Diameter of duct

  μ = Viscosity of the fluid

  ρ = Density of fluid

Due to presence of elbow, valves, etc, there are some losses in the pipe which are counted in the energy balance equation. The head losses in the valve and elbow is given as,

  hf=(4fLD+Kf)V¯22g ....... (4)

f = Fanning friction factor

Kf = Loss coefficient in pipe fittings

L = Length of the duct

g = Acceleration due to gravity

The roughness parameter is given as, kD where k is roughness of the pipe. It shows how much friction is present in the pipe and with the help of the roughness parameter, f can be calculated from the friction factor chart.

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1. The settling chamber, shown schematically in Figure 2E1.1, is used as a primary separation device in the removal of dust particles of density 1500 kg/m³ from a gas of density 0:7 kg/m³ and viscosity 1.90 x 10-5 Pa s. Gas inlet Elevation Gas Gas exit exit H Collection surface -W Section X-X Dimensions: H=3m L = 10 m W=2m Figure 2E1.1 Schematic diagram of settling chamber Assuming Stokes' law applies, show that the efficiency of collection of particles of size x is given by the expression collection efficiency, x = x²8(pp - Pi)L 18μHU where U is the uniform gas velocity through the parallel-sided section of the chamber. State any other assumptions made. (b) What is the upper limit of particle size for which Stokes' law applies? (c) When the volumetric flow rate of gas is 0.9 m³/s, and the dimensions of the chamber are those shown in Figure 2E1.1, determine the collection efficiency for spherical particles of diameter 30 mm.
Can you answer this sequantially correct like show me the full process. Also, since it is chemical engineering related problem a perry's handbook is used. Thank you
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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