In the final stages of production, a pharmaceutical is sterilized by heating it from 25 to 75 ° C as it moves at 0. 2 m / s through a straight thin—walled stainless steel tube of 12 . 7 − mm diameter. A uniform heat flux is maintained by an electric resistance heater wrapped around the outer surface of the tube. If the tube is 10 m long. what is the required heat flux? It fluid enters the tube with a fully developed velocity profile and a uniform temperature profile. what is the surface temperature at the tube exit and at a distance of 0. 5 m from the entrance? Fluid properties may be approximated as ρ = 1000 kg/m 3 , c p = 4000 J/kg ⋅ K,m = 2 × 10 − 3 kg/s ⋅ m,k = 0.8 W/m ⋅ K , and P r = 1 0 .
In the final stages of production, a pharmaceutical is sterilized by heating it from 25 to 75 ° C as it moves at 0. 2 m / s through a straight thin—walled stainless steel tube of 12 . 7 − mm diameter. A uniform heat flux is maintained by an electric resistance heater wrapped around the outer surface of the tube. If the tube is 10 m long. what is the required heat flux? It fluid enters the tube with a fully developed velocity profile and a uniform temperature profile. what is the surface temperature at the tube exit and at a distance of 0. 5 m from the entrance? Fluid properties may be approximated as ρ = 1000 kg/m 3 , c p = 4000 J/kg ⋅ K,m = 2 × 10 − 3 kg/s ⋅ m,k = 0.8 W/m ⋅ K , and P r = 1 0 .
In the final stages of production, a pharmaceutical is sterilized by heating it from 25 to
75
°
C
as it moves at
0.
2 m
/
s
through a straight thin—walled stainless steel tube of
12
.
7
−
mm
diameter. A uniform heat flux is maintained by an electric resistance heater wrapped around the outer surface of the tube. If the tube is 10 m long. what is the required heat flux? It fluid enters the tube with a fully developed velocity profile and a uniform temperature profile. what is the surface temperature at the tube exit and at a distance of
0.
5 m
from the entrance? Fluid properties may be approximated as
ρ
=
1000
kg/m
3
,
c
p
=
4000
J/kg
⋅
K,m
=
2
×
10
−
3
kg/s
⋅
m,k
=
0.8
W/m
⋅
K
, and
P
r
=
1
0
.
In the final stages of production, a pharmaceutical is sterilized by heating it from 25 to 75°C as it moves at 0.17 m/s through a straight
thin-walled stainless steel tube of 12.7-mm diameter. A uniform heat flux is maintained by an electric resistance heater wrapped
around the outer surface of the tube. If the tube is 10 m long, what is the required heat flux? If fluid enters the tube with a fully
developed velocity profile and a uniform temperature profile, what is the surface temperature at the tube exit? Fluid properties may be
approximated as p = 1000 kg/m³, cp = 4000 J/kg-K₁ μ = 2 x 10°³kg/s-m, k = 0.8 W/m-K, and Pr = 10.
Determine the required heat flux, W/m²2.
q" = i
W/m²
Determine the surface temperature at the tube exit, in °C.
T₁,0 = i
°C
Physical Properties Mathematical Functions
In the final stages of production, a pharmaceutical is sterilized by heating it from 25 to 75°C as it moves at 0.19 m/s through a
straight thin-walled stainless steel tube of 12.7-mm diameter. A uniform heat flux is maintained by an electric resistance heater
wrapped around the outer surface of the tube. If the tube is 10 m long, what is the required heat flux? If fluid enters the tube with a
fully developed velocity profile and a uniform temperature profile, what is the surface temperature at the tube exit? Fluid properties
may be approximated as p = 1000 kg/m³, cp = 4000 J/kg-K, μ = 2 × 10-³ kg/s-m, k = 0.8 W/m-K, and Pr = 10.
Determine the required heat flux, W/m².
q'"
W/m²
Determine the surface temperature at the tube exit, in °C.
= i
°C
8,0
In the final stages of production, a pharmaceutical is sterilized by heating it from 25 to 75°C as it moves at 0.19 m/s through a straight
thin-walled stainless steel tube of 12.7-mm diameter. A uniform heat flux is maintained by an electric resistance heater wrapped
around the outer surface of the tube. If the tube is 10 m long, what is the required heat flux? If fluid enters the tube with a fully
developed velocity profile and a uniform temperature profile, what is the surface temperature at the tube exit? Fluid properties may be
approximated as p = 1000 kg/m³, c, = 4000 J/kg-K, µ = 2x 10-3 kg/s-m, k = 0.8 W/m-K, and Pr = 10.
Determine the required heat flux, W/m².
W/m2
Determine the surface temperature at the tube exit, in °C.
T =
°C
i
S,0
Physical Properties Mathematical Functions
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