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Calculate the frictional pressure gradient –ΔPfs/L for a time independent non- Newtonian fluid in steady state flow in a cylindrical tube if the liquid density the inside diameter of the tube the mean velocity the point pipe consistency coefficient and the flow behavior index ρ = 1000 kg/m3 d = 0.08 m u = l.0 m / s K' = 2 Pa. s0.5 n' = 0.5.

Calculate the frictional pressure gradient –ΔPfs/L for a time independent non- Newtonian fluid in steady state flow in a cylindrical tube if the liquid density the inside diameter of the tube the mean velocity the point pipe consistency coefficient and the flow behavior index ρ = 1000 kg/m3 d = 0.08 m u = l.0 m / s K' = 2 Pa. s0.5 n' = 0.5.

Introduction to Chemical Engineering Thermodynamics
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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Calculate the frictional pressure gradient –ΔPfs/L for a time independent non- Newtonian fluid in steady state flow in a cylindrical tube if
the liquid density the
inside diameter of the tube
the mean velocity
the point pipe consistency coefficient and the flow behavior index
ρ = 1000 kg/m3 d = 0.08 m
u = l.0 m / s
K' = 2 Pa. s0.5
n' = 0.5.

P.6.2 Calculate the frictional pressure gradient -AP/L for a time independent non- Newtonian fluid in steady state flow in a cylindrical tube if the liquid density the inside diameter of the tube p= 1000 kg/m3 d = 0.08 m %3D the mean velocity the point pipe consistency coefficient K'=2 Pa. s0.5 and the flow behavior index u = 1.0 m / s n' = 0.5. %3D
Transcribed Image Text:P.6.2 Calculate the frictional pressure gradient -AP/L for a time independent non- Newtonian fluid in steady state flow in a cylindrical tube if the liquid density the inside diameter of the tube p= 1000 kg/m3 d = 0.08 m %3D the mean velocity the point pipe consistency coefficient K'=2 Pa. s0.5 and the flow behavior index u = 1.0 m / s n' = 0.5. %3D
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