The velocity distribution for a laminar, incompressible flow of a Newtonian fluid in a long vertical tube is as follows: ... (P₁-PDR² [1 - (²-) ² ] where V₂ is the z-component of velocity, R is the radius of the tube, L is the length of the tube, μ is the viscosity of the fluid, and r is the radial distance from the center-line of the tube. If a fluid whose density is 1,200 kg per cubic meter and viscosity is 0.0001 Pascal-second is travelling along a circular tube of cross sectional area of 1 cm², owing to a pressure gradient of 1 kiloPascal per meter, the average velocity in meter/sec is Blank 1 m/s.

Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Chapter1: Introduction
Section: Chapter Questions
Problem 1.1P
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The velocity distribution for a laminar, incompressible flow of a Newtonian fluid in a long
vertical tube is as follows:
(P₁-PD)R² [1 - (-) ² ]
Vz
4μL
where V₂ is the z-component of velocity, R is the radius of the tube, L is the length of the tube, "
is the viscosity of the fluid, and r is the radial distance from the center-line of the tube.
If a fluid whose density is 1,200 kg per cubic meter and viscosity is 0.0001 Pascal-second is
travelling along a circular tube of cross sectional area of 1 cm², owing to a pressure gradient of
1 kiloPascal per meter, the average velocity in meter/sec is Blank 1 m/s.
Transcribed Image Text:The velocity distribution for a laminar, incompressible flow of a Newtonian fluid in a long vertical tube is as follows: (P₁-PD)R² [1 - (-) ² ] Vz 4μL where V₂ is the z-component of velocity, R is the radius of the tube, L is the length of the tube, " is the viscosity of the fluid, and r is the radial distance from the center-line of the tube. If a fluid whose density is 1,200 kg per cubic meter and viscosity is 0.0001 Pascal-second is travelling along a circular tube of cross sectional area of 1 cm², owing to a pressure gradient of 1 kiloPascal per meter, the average velocity in meter/sec is Blank 1 m/s.
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