we also considered pressure driven flow of an incompressible Newtonian fluid (INF) through the annular gap between two horizontal coaxial cylinders as shown in the figure below: PO>PL a. Q= 12R₁ 2RO The correct equation was: TRAP (R₂)* 8μ L v₂(r) = Using this piece of information, calculate Vav (m/s) and then the Reynolds number for the following conditions: Glycerin at 20 °C, a very viscous fluid (1.4 Pa*s), is the INF in the annular space R₂ = 10 mm R₁ = 2 mm AP/L = 30 kPa/m Based on your calculation of the Reynolds number, what can you conclude about the existence of laminar flow conditions? 4μ . In b. The axial velocity profile v.(r) for the system described above is as follows: 1 ΔΡ R²-R² r ∙In in (Ro/R₂) Ro R²-² + Equation 7.98 from Vlachopoulos' book Using Excel (or another suitable software), plot the axial velocity profile for the conditions given in part a). In order to match the physical nature of the system, plot the axial velocity (v:(r)) on the x-axis and the radial distance (r) on the y-axis. The range of y values should be from 0 to +R₂-be VERY careful about what happens in the range of y values from 0 to +R₁.

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
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Question
we also considered pressure driven flow of an incompressible Newtonian fluid (INF) through the annular
gap between two horizontal coaxial cylinders as shown in the figure below:
PO>PL
co
TRAP
8μ L
2R₁
2R₁ 2RO
(R.)
Using this piece of information, calculate Vav (m/s) and then the Reynolds number for the following
conditions:
The correct equation was:
1-)
In
v₂(r) =
TO
Glycerin at 20 °C, a very viscous fluid (1.4 Pa*s), is the INF in the annular space
R. = 10 mm
R₁ = 2 mm
AP/L = 30 kPa/m
Based on your calculation of the Reynolds number, what can you conclude about the existence of laminar
flow conditions?
b. The axial velocity profile v.(r) for the system described above is as follows:
1 ΔΡ
4μ L
R² - R² r
Ro
∙In
In
(Ro/R₂)
R² −²+
Equation 7.98 from
Vlachopoulos' book
Using Excel (or another suitable software), plot the axial velocity profile for the conditions given in part a). In
order to match the physical nature of the system, plot the axial velocity (v:(r)) on the x-axis and the radial
distance (r) on the y-axis. The range of y values should be from 0 to +R₂-be VERY careful about what
happens in the range of y values from 0 to +R₁.
Transcribed Image Text:we also considered pressure driven flow of an incompressible Newtonian fluid (INF) through the annular gap between two horizontal coaxial cylinders as shown in the figure below: PO>PL co TRAP 8μ L 2R₁ 2R₁ 2RO (R.) Using this piece of information, calculate Vav (m/s) and then the Reynolds number for the following conditions: The correct equation was: 1-) In v₂(r) = TO Glycerin at 20 °C, a very viscous fluid (1.4 Pa*s), is the INF in the annular space R. = 10 mm R₁ = 2 mm AP/L = 30 kPa/m Based on your calculation of the Reynolds number, what can you conclude about the existence of laminar flow conditions? b. The axial velocity profile v.(r) for the system described above is as follows: 1 ΔΡ 4μ L R² - R² r Ro ∙In In (Ro/R₂) R² −²+ Equation 7.98 from Vlachopoulos' book Using Excel (or another suitable software), plot the axial velocity profile for the conditions given in part a). In order to match the physical nature of the system, plot the axial velocity (v:(r)) on the x-axis and the radial distance (r) on the y-axis. The range of y values should be from 0 to +R₂-be VERY careful about what happens in the range of y values from 0 to +R₁.
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I got 10^(-8) instead of 10^(-5) can someone tell me what I'm doing wrong or if my answer is correct?

Q
=
||
4
π10 mm
8x1.4 Pa.s
X
1 m
1000 mm
8.418 × 10
4
× 30
m³
3
S
X
Transcribed Image Text:Q = || 4 π10 mm 8x1.4 Pa.s X 1 m 1000 mm 8.418 × 10 4 × 30 m³ 3 S X
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