thermofluid lab 2-part a
TRANSCRIPT
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UNIVERSITI TEKNOLOGI MARA
FACULTY OF
MECHANICAL
ENGINEERING
________________________________________________________________________
Program : Bachelor Of Engineering ( Hons ) Mechanical
Course : Thermalfluids Lab II
Code : MEC 554
________________________________________________________________________
TURBOMACHINARY
TITLE : Compressible flow in converging‐diverging nozzle
1.
OBJECTIVE
To study the pressure‐mass flow rate characteristic for convergent‐divergent duct.
To demonstrate the phenomena of choking.
2. THEORY
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3. EQUIPMENT
The experiment
apparatus
consists
of
a compressible
flow
bench
equip
with
digital
pressure
sensors.
4. Experiment guidelines
Follow the instructions explain by the instructor regarding how to operate the experiment apparatus.
Before starting the experiment, make sure that there is no blockage or object around the convergent‐
divergent nozzle that will interfere with the air flow into the nozzle. Connect the three pressure tap to the
appropriate pressure sensors. Start the experiment from zero velocity and then increase the air velocity
through the nozzle at a constant increment step (eg. 200 rpm) until reaching the maximum air velocity.
Make sure that you record the 3 pressure reading at the nozzle opening, throat and exit for each air velocity
step. Repeat the experiment by decreasing the air velocity from maximum until zero velocity. The air
velocity can be adjusted by changing the rpm of the air blower.
(Experimental parameters can be adjusted according to the conditions and available apparatus at the
time the experiment is conducted.)
5. Data
1.
Calculate the mass flow rate values and the remaining parameters required using the formula
given.
2. Plots the following graphs:
a. vs (P0 – P2) b. vs P2 c.
vs (P0 – P3)
d. vs P3 e. (P0 – P2) vs (P0 – P3)
3.
Comment and analyze the graphs. Compared the maximum values for and the minimum for P2/P0 from the trial with the theoretical values.
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Experiment ID: Date:
Ambient air temperature : Air density:
Atmospheric pressure : Air specific heat ratio:
Convergent‐divergent nozzle specifications:
No.
reading RPM P1 P2 P3 (P0 ‐ P1) (P0 – P2) (P0 – P3) 2 1 [krpm] [kg/s]
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UNIVERSITI
TEKNOLOGI
MARA
FACULTY
OF
MECHANICAL
ENGINEERING ________________________________________________________________________
Program
:
Bachelor
Of
Engineering
(
Hons
)
Mechanical
Course : Thermalfluids Lab II
Code
:
MEC
554
________________________________________________________________________
TURBOMACHINARY
TITLE
:
Performance
of
Pump
1.
OBJECTIVE
To obtain the performance characteristics for a variable speed centrifugal pump operating at 3 different
impeller
speeds.
The
pump
performance
characteristics
that
will
be
study
are
pressure
jump,
power
requirement, flow rate influence and pump speed influence.
2. THEORY
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3. EQUIPMENT
The experiment apparatus consists of a water flow bench and centrifugal pump rigged with sensors to
measures water pressure, flow‐rate, pump speed, pump torque and electric power consumed by the pump.
4. Experiment guidelines
Follow the instructions explain by the instructor regarding how to operate the experiment apparatus.
Set the bench to only allow the water to flow through only one centrifugal pump. Power on the correct
pump. Allow the system to reach a steady flow condition before recording the pressures, flow rate, pump
speed, pump torque and pump power. The speed of the pump is control by rotating the pump speed control
dial on the control panel. To collect data for 3 different pump speeds, set the speed control dial to 100%,
75% and 50%.
For every pump speed, collect at least 5 data points based on variable flow‐rate. The flow‐rate can be
adjusted using the water flow control valve situated at the highest point of the bench. The flow meter can
be used as a guidance on setting the amount of water flow passing through the pump.
(Experimental parameters can be adjusted according to the conditions and available apparatus at the
time the experiment is conducted.)
5. Data
1. Record the performance characteristic values in a table. Other performance characteristic that can
not be gained directly can be calculated using the formula given in the theory section. (Be careful
on the parameters unit.)
2. Plot the performance graph (Please refer to the graph shown in the theory section). The
performance curves that are of interest are power curve, efficiency curve and pump head curve.
3.
Analyze and discuss the plots.
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Experiment ID: Date:
Pump Speed, N: rpm
rad/s
Water temperature :
Water density :
No. Electric
motor Pump Input Pump output
Efficiency,
ηPower,
Pm
Torque,
Tshaft
Shaft
Power,
Wshaft
Volume
flow
rate, Q
Inlet pressure,
P1
Discharge
pressure, P2
Water
head,
hp
Output
power,
Pf
[kW] [Nm] [kW] % % [m] [kW] [100%]
1
2
3
4
5
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Experiment ID: Date:
Pump Speed, N: rpm
rad/s
Water temperature :
Water density :
No. Electric
motor Pump Input Pump output
Efficiency,
ηPower,
Pm
Torque,
Tshaft
Shaft
Power,
Wshaft
Volume
flow
rate, Q
Inlet pressure,
P1
Discharge
pressure, P2
Water
head,
hp
Output
power,
Pf
[kW] [Nm] [kW] % % [m] [kW] [100%]
1
2
3
4
5
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Experiment ID: Date:
Pump Speed, N: rpm
rad/s
Water temperature :
Water density :
No. Electric
motor Pump Input Pump output
Efficiency,
ηPower,
Pm
Torque,
Tshaft
Shaft
Power,
Wshaft
Volume
flow
rate, Q
Inlet pressure,
P1
Discharge
pressure, P2
Water
head,
hp
Output
power,
Pf
[kW] [Nm] [kW] % % [m] [kW] [100%]
1
2
3
4
5
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UNIVERSITI TEKNOLOGI MARA
FACULTY OF MECHANICAL ENGINEERING ________________________________________________________________________
Program : Bachelor Of Engineering ( Hons ) MechanicalCourse : Thermalfluids Lab IICode : MEC 554
HEAT TRANSFER LABORATORY SHEET
TITLE : HEAT CONDUCTION SIMPLE BAR
1. OBJECTIVE
Investigate Fourier’s law for linear conduction of heat along a simple bar.
2. THEORY
If a plane wall of thickness (x) and area ( A) and thermal
conductivity (k) supports a temperature difference (T) then theheat transfer rate by conduction is given by the equation:
dx
dT Ak Q
Assuming a constant thermal conductivity throughout thematerial and a linear temperature distribution, this is:
x
T Ak Q
3. EQUIPMENT
The equipment is shown in the figure below.
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4. Experiment Guideline
Select an intermediate position for the heater power control (e.g. 10 W) and allow sufficient time fora steady state to be achieved before recording the temperature (T) at all 9 sensor points (T1 to T9)
and the input power reading on the wattmeter (Q ). Remember to measure the distance between
each temperature sensors. This procedure should be repeated for other input powers (e.g. 20 Wand 30W) up to the maximum setting of the control. After each change, sufficient time must beallowed to achieve steady conditions.
5. DATA
HEATER SAMPLE REGION COOLER
x (mm) 0 10 20 30 40 50 60 70 80
x (m) 0 0.01 0.02 0.03 0.04 0.05 0.06 0.07 0.08
Test
#
Q (W)
T1
(°C)
T2
(°C)
T3
(°C)
T4
(°C)
T5
(°C)
T6
(°C)
T7
(°C)
T8
(°C)
T9
(°C)
A
B
C
1. Plot the temperature profile along the entire length. This should reveal three distinct sections ofstraight lines (corresponding to the heater, brass sample, and cooler) having a slope of
approximately T/x.2. Convert the measured temperatures to degrees Kelvin by the following formula:
15.273
C T K T
3. Calculate the cross-sectional area (A) of the circular cylinder by using the equation:
2
4d A
4. The brass sample region is the region of interest. Ignore all other temperature measurementsexcept T4, T5, and T6 and calculate the thermal conductivity of the brass. This is the slope of thestraight line in the brass sample region alone (plotted in 1), given by the equation:
K m
W units
T
x
A
Qk
5. Find published values of brass in books or on the Internet. Compare the value you obtainedwith these values. Which type of brass does your results best compare with (e.g. yellow brass,red brass etc.)? Discuss any source of error in your measured results. Students shouldcomment on how changing the average temperature affects the thermal conductivity.
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Experiment ID:
HEATER SAMPLE REGION COOLER
x (mm)
x (m)
Test
#
Q (W)
T1
(°C)
T2
(°C)
T3
(°C)
T4
(°C)
T5
(°C)
T6
(°C)
T7
(°C)
T8
(°C)
T9
(°C)
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3. EQUIPMENT
Control rectangular heated surfaces will be used to study heat transfer through forced convection.The surfaces are shown in the figure below. The finned surface consists of 9 fins that are each 0.1m high and 0.068 m wide. The pinned surface consists of 17 pins that each have a diameter of0.013 m and are 0.068 m long. (Make sure that you observed and take measurement of the surfacegeometry when you performed the experiment to confirmed the actual dimensions.)
4. Experiment guidelines
Place the heat exchanger into the test duct and record the ambient temperature (T ). Set the heaterpower control to 75 W. Allow the temperature to rise to 80°C then adjust the heater power control to20 W. This will prepare the heat exchanger for the experimental condition needed.To collect the heat exchanger surface temperature reading, start the stopwatch, wait 5 minute andrecord surface temperature (Ts).Repeat the steps above to obtained data for other conditions (eg. air velocity 0 m/s, 1 m/s, 2m/s….). To introduce air flow in the duct, turn the fan speed control to start the fan. Adjust the fanspeed control to give the desired air velocity. The air velocity can be measure using a thermalanemometer.
The experiment can be repeated for different type of heat exchanger.
(Experimental parameters can be adjusted according to the conditions and available apparatus at the time
the experiment is conducted.)
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Experiment ID:
Surface geometry:
Ambient airtemperature, T∞ :
Power input, :
Air velocity [m/s] Heater Temperature, Ts [
0C]
Ts - T∞ [0C] H [ W/(m·0C)]
Experiment ID:
Surface geometry:
Ambient airtemperature, T∞ :
Power input, :
Air velocity [m/s]Heater Temperature,
Ts [0C]
Ts - T∞ [0C] H [ W/(m·
0C)]
Experiment ID:
Surface geometry:
Ambient airtemperature, T∞ :
Power input, :
Air velocity [m/s]Heater Temperature,
Ts [0C]
Ts - T∞ [0C] H [ W/(m·
0C)]