Consider flow over a flat plate for which it is desired to determine the average heat transfer coefficient over the short span x 1 to x 2 , h ¯ 1 − 2 , where ( x 2 − x 1 ) ≪ L . Provide three different expressions that can be used to evaluate h ¯ 1 − 2 in terms of (a) the local coefficient at x = ( x 1 + x 2 ) / 2 , (b) the local coefficients at x 1 and x 2 , and (c) the average coefficients at x 1 and x 2 . Indicate which of the expressions is approximate. Considering whether the flow is laminar, turbulent, or mixed, indicate when it is appropriate or inappropriate to use each of the equations.
Consider flow over a flat plate for which it is desired to determine the average heat transfer coefficient over the short span x 1 to x 2 , h ¯ 1 − 2 , where ( x 2 − x 1 ) ≪ L . Provide three different expressions that can be used to evaluate h ¯ 1 − 2 in terms of (a) the local coefficient at x = ( x 1 + x 2 ) / 2 , (b) the local coefficients at x 1 and x 2 , and (c) the average coefficients at x 1 and x 2 . Indicate which of the expressions is approximate. Considering whether the flow is laminar, turbulent, or mixed, indicate when it is appropriate or inappropriate to use each of the equations.
Solution Summary: The author calculates the heat rate per unit width for the shortest span from x_1 to
Consider flow over a flat plate for which it is desired to determine the average heat transfer coefficient over the short span
x
1
to
x
2
,
h
¯
1
−
2
,
where
(
x
2
−
x
1
)
≪
L
.
Provide three different expressions that can be used to evaluate
h
¯
1
−
2
in terms of (a) the local coefficient at
x
=
(
x
1
+
x
2
)
/
2
,
(b) the local coefficients at
x
1
and
x
2
,
and (c) the average coefficients at
x
1
and
x
2
.
Indicate which of the expressions is approximate. Considering whether the flow is laminar, turbulent, or mixed, indicate when it is appropriate or inappropriate to use each of the equations.
The correlation below is used to calculate the heat transfer coefficients for forced convection
owing to laminar flow outside flat plates.
k0.67 (vp)0.5 co.33
h = 0.644
D0.5µ0.17
Where h is in W/m²-K
v is in m/s
p is in kg/m³
Cp is in J/kg-K
D is in m
µ is in Pa-s
What units must the constant 0.644 have?
What should be the value of the constant when all units are
converted to English units (masses in lbm, lengths in ft, temperatures in oR,
times in h, energies in Btu)?
Q1/ Consider the following fluids, each with a velocity of u = 9 m/s and a temperature of
10°C, in cross flow over a 10-mm diameter cylinder maintained at 50°C. Calculate the rate
of heat transfer per unit length for saturated water?
***** 2
Satu
Dety
PP Liquid
3149 9920
4.246 996.0
528 9040
7.354 902.1
393 9901
Nu 0.3+1
Endalay Specific
Heal
Veputation
0.62 Re2 Pro
[1 + (0.4/Pypa[1+ (282,000)
aper
0.0231
2402 4180
00304
4378
0.0397 2419 4178
0.0612 2407 4179
00655 2335 4180
tree
Thermal
Coductivity
THAY
Liquid Vapor Le
Dynamic Vacosity
1870
Vapor
Liquid
0607 0.0186 0110 0.90710
1875 0615 0.0169 0.796 101 100110
1880 BAZ3 0.0192 0720x10 1016 10
1825 0.631 0.5196 0653x10 103150
1832 0437 0.0000 0596x10104610
Fran
www.
Lignon
A'IN
Ligad Vaper
614 1.00 0.24710
542 100 0234-10
4.83 1.00 0.337x10
4.32 100 0377x10
191 100 0415-10
Air at 22˚C and at atmospheric pressure flows over a flat plate at a velocity of 1.65 m/s. If the length
of the plate is 2.179 m and its temperature is 98 ˚C, Calculate Heat rate by using exact and approximate
methods both. What is the %age difference of the heat transfer rate values by these methods? Take
width of the plate as unity.
Properties given at 60˚C are as follows:
Density: 1.058 kg/m3
, cp = 1.005 kJ/kg˚C, k= 0.02897 w/m˚C, Kinematic viscosity is 18.97 × 10-6 m2
/s
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