APPLICATIONS OF THERMOFLUID DYNAMICS
THERMOFLUID DYNAMICS
项目类别:物理
APPLICATIONS OF THERMOFLUID DYNAMICS II


DATA:

Material supplied:
- Heat transfer data sheet

Unless otherwise stated in the Question the following values
may be assumed:
- Air behaves as an ideal gas with constant specific heat
capacities:
cp  1005 J/(kgK) and cv  718J/(kgK)  R  287J/(kgK)
- Density of liquid water   1000kg/m3
- Gravitational field strength g  9.805 N/kg
- The Stefan-Boltzmann constant = 5.67  10-8 W/m2 K4





Q1(a) A plane surface is provided with an array of straight
rectangular fins of length and thickness 25 mm and 1.5 mm
respectively. The fins are spaced on a 3.5 mm pitch. The
fins are made of a material with a thermal conductivity of
100 W/m K, and the heat transfer coefficient at all exposed
surfaces is 300 W/m2K. The fin base temperature is 95oC
and the ambient fluid is at 25oC.

(i) Find the correct range for the overall surface efficiency
of the array

(a) 30%-40%
(b) 50%-60%
(c) 80%-90%
(d) None of the above
(4 marks)

(ii) Find the correct range for the heat transferred to the
fluid per square metre of primary surface.

(a) 10-15 kW/m2
(b) 17-22 kW/m2
(c) 5-7 kW/m2
(d) None of the above
(2 marks)

Q1(b) (i) Is a proposed heat pump for domestic space heating
possible:
- using an ambient heat source at 10C,
- with a pump motor power input of W = 200W, and
- delivering Qd = 1kW at a space temperature of 20C?
Please identify the correct statement.

(a) Clausius inequality gives a value in the range of (0.5
to 0.60) W/K and it is possible.
(b) Clausius inequality gives a value in the range of (-0.6
to -0.50) W/K and it is possible.
[MEC2003]

5
(c) Clausius inequality gives a value in the range of (-0.2
to -0.40) W/K and it is possible.
(d) Clausius inequality gives a value in the range of (0.5
to 0.60) W/K and it is not possible.
(4 marks)

(ii) With the same ambient source and extraction rate, and
with the same motor, it is proposed to split the 1kW
delivered heat equally between space heating at the
same temperature of 20C and water heating at 40C.
Identify the correct statement.

(a) Clausius inequality gives a value in the range of (-0.6
to -0.55) W/K and it is possible.
(b) Clausius inequality gives a value in the range of (-0.6
to -0.55) W/K and it is not possible.
(c) Clausius inequality gives a value in the range of (-0.5
to -0.40) W/K and it is possible.
(d) Clausius inequality gives a value in the range of (0.4
to 0.50) W/K and it is not possible.

(3 marks)

Q1(c) Modifications to a chemical process will require 120,000
kg/h of toluene to be heated from 15oC to a temperature of
at least 55oC. A steam-heated shell-and-tube exchanger is
available. It has 100 steel tubes arranged in a single pass.
The tube dimensions are: outside diameter 17 mm, inside
diameter 15 mm, length 5.5 m. Saturated steam at 3 bar is
used on the shell side.
Take the shell side heat transfer coefficient ho = 8000 W/m2
K. Take the fouling factor to be 0.001 m2.K /W on both sides
of the tube.
Physical properties of toluene at the mean temperature of
(15 + 55)/2 = 35oC are: density = 870 kg/m3, specific heat
[MEC2003]
6
= 1.8 kJ/kg K, viscosity = 280 × 10−6 N.s/m2, thermal
conductivity = 0.15 W/m.K.

Take the thermal conductivity of steel as 50 W/m.K.

(i) Estimate the correct range within which the mean velocity
within the tube lies:

(a) 2.0 m/s – 3.0 m/s
(b) 3.5 m/s – 4.0 m/s
(c) 1.0 m/s – 1.5 m/s
(d) None of the above
(2 marks)

(ii) Estimate the correct range of the Reynolds number for
the tube flow and nature of the flow:

(a) 2000-3000, laminar flow
(b) 50000-80000, turbulent flow
(c) 15000-20000, turbulent flow
(d) 100000-200000, turbulent flow
(2 marks)

(iii) Estimate the correct range of the overall heat transfer
coefficient for the internal surface:

(a) 400W/m2.K-500 W/m2.K
(b) 550 W/m2.K-600 W/m2.K
(c) 3000 W/ m2.K-3500 W/m2.K
(d) None of the above
(3 marks)

(iv) Estimate the correct range of the log mean temperature
difference:

(a) 70oC-80oC
(b) 90oC-100oC
(c) 110oC-120oC
(d) 130oC-140oC
[MEC2003]

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(3 marks)
(v) Is the heat exchanger suitable for duty?

(a) Yes
(b) No
(2 marks)


Q2. A cylindrical vessel of diameter 2.0 m contains molten metal
whose surface temperature is 1600 K; the height of the vessel
above the level of the liquid metal is 1.0 m and the vessel is in
large surroundings at a mean temperature of 300 K. The
cylindrical sides of the vessel are insulated. The emissivity of
the liquid metal surface is 0.3. Assume steady state conditions.



Fig. Q2


Let us consider the molten metal surface as surface 1. The
opening is taken to be surface 2. The curved cylindrical surface
is taken to be surface 3.




[MEC2003]
8

(i) Identify the correct set of view factors (identify the choice
that is the closest to your answer)

(a) F11 = 0.0; F12 = 0.38; F13 = 0.62; F21 = 0.38;
F22 = 0.0; F23 = 0.62; F31 = 0.31; F32 = 0.31; F33 = 0.38

(b) F11 = 0.0; F12 = 0.18; F13 = 0.82; F21 = 0.18;
F22 = 0.0; F23 = 0.82; F31 = 0.41; F32 = 0.41; F33 = 0.18

(c) F11 = 0.0; F12 = 0.75; F13 = 0.25; F21 = 0.75;
F22 = 0.0; F23 = 0.25; F31 = 0.13; F32 = 0.13; F33 = 0.74

(d) F11 = 0.0; F12 = 0.5; F13 = 0.5; F21 = 0.5;
F22 = 0.0; F23 = 0.5; F31 = 0.5; F32 = 0.5; F33 = 0.0

(6 marks)

(ii) Identify the correct [M][J] = [S] matrix (identify the choice
that is the closest to your answer):

(a) [
3.33 −0.887 −1.4467
−0.887 3.33 −1.4467
−0.31 −0.31 0.62
] [
J1
J2
J3
] = [
371589.1
459.27
0
]

(b) [
3.33 −0.887 −1.4467
0.0 1.0 0.0
−0.31 −0.31 0.62
] [
J1
J2
J3
] = [
371589.1
459.27
0
]

(c) [
1.0 0.0 0.0
−0.887 3.33 −1.4467
−0.31 −0.31 0.62
] [
J1
J2
J3
] = [
459.27
371589.1
0
]

(d) None of the above

(10 marks)

[MEC2003]

9

(iii) Estimate the correct range of radiation heat transfer from
the molten surface:

(a) 140 kW/m2 -150 kW/m2
(b) 90 kW/m2 - 100 kW/m2
(c) 280 kW - 350 kW
(d) 420 kW - 450 kW

(4 marks)

(iv) Estimate the correct range of average temperature of the
vessel wall above the metal surface.

(a) 500oC – 700oC
(b) 800 K – 1100 K
(c) 1200oC – 1500oC
(d) None of the above


(5 marks)
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