Jet trajectory and flow through an orifice | Bài báo cáo học phần Fluid Mechanics Lab | Trường Đại học Quốc tế, Đại học Quốc gia Thành phố Hồ Chí Minh

(1) Start the pump of the hydraulic bench and adjust the flow so the level in the tank stays just above the overflow pipe in the tank. (2) Allow conditions to stabilize and use the hydraulic bench to measure the flow. Record the Head inside the tank. (3) Reduce the inlet flow (supply from the hydraulic bench) so that the head falls by about 30 mm. (4) Allow conditions to stabilize and use the hydraulic bench to measure the flow. Record the Head inside the tank. Tài liệu giúp bạn tham khảo, ôn tập và đạt kết quả cao. Mời bạn đón xem.  

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Jet trajectory and flow through an orifice | Bài báo cáo học phần Fluid Mechanics Lab | Trường Đại học Quốc tế, Đại học Quốc gia Thành phố Hồ Chí Minh

(1) Start the pump of the hydraulic bench and adjust the flow so the level in the tank stays just above the overflow pipe in the tank. (2) Allow conditions to stabilize and use the hydraulic bench to measure the flow. Record the Head inside the tank. (3) Reduce the inlet flow (supply from the hydraulic bench) so that the head falls by about 30 mm. (4) Allow conditions to stabilize and use the hydraulic bench to measure the flow. Record the Head inside the tank. Tài liệu giúp bạn tham khảo, ôn tập và đạt kết quả cao. Mời bạn đón xem.  

32 16 lượt tải Tải xuống
Department of Civil Engineering
International University (IU)
Instructor: Prof. Pham Ngoc.
Date of submission: 14/04/2017
FLUID MECHANICS LABORATORY
JET TRAJECTORY AND FLOW THROUGH AN
ORIFICE
Group’s members:
Nguyễn Văn Tú CECEIU15054
Lê Nhật Tú CECEIU15013
Nguyễn Dương Tấn Son CECEIU15044
Trương Nguyên Vũ CECEIU15033
Nguyễn Quốc Thắng CECEIU15048
Experiment 1: Head and Flow Relaonship
I. Objecves:
The objecves of the experiment are:
- to understand the relaonship between head and ow for an orice
- to show how the coecient of discharge varies with ow.
- to use the head and ow relaonship to nd the average coecient of
discharge for the orice.
The coecient of discharge C
d
is the rao of the actual discharge to that which
would take place if the jet discharged at the idea velocity without any reducon of
area. The actual discharge Q is given by: (1)
and if the jet discharged at the idea velocity u
o
over the orice area A
o
, the the
discharge Q
o
would be: (2)
d
=
Ao 2gHo
or (5)
Q kH
o
k
C
d
=
where k C d A o 2g => Ao 2g
II. Experimental Apparatus
The experimental apparatus consists of the following parts:
So, from the denion of the coecient of discharge,
Q u A
(3)
or in terms of quanes measured experimentally,
Q= C
d
A
o
2gH
o =
C
d
Q
o
Q
C
(4)
Figure 1. General Layout
Table 2. Technical Details
Item Details
Dimensions and weight 700 mm high x 700 mm long x 400 mm front to
(assembled) back. 10 kg including nozzles.
Manometer scale 100 mm to 390 mm
1 division = 0.1 mm
Pitot Micrometer
1 complete turn = 1 mm
Set of four Orice / Nozzles See Figure 2
Figure 2. Dimensions of the Orice / Nozzle
Dimension in mm
Datum = Distance to internal surface of tank when mounted vercally
III. Procedure
(1) Start the pump of the hydraulic bench and adjust the ow so the level in the
tank stays just above the overow pipe in the tank.
(2) Allow condions to stabilize and use the hydraulic bench to measure the ow.
Record the Head inside the tank.
(3) Reduce the inlet ow (supply from the hydraulic bench) so that the head falls
by about 30 mm.
(4) Allow condions to stabilize and use the hydraulic bench to measure the ow.
Record the Head inside the tank.
(5) Repeat for decreasing value of head in about 30 mm steps, giving about eight
results over the height of the manometer scale, each me recording head and
ow.
IV. Data Analysis
1.90E-04
1.70E-04
2.90E-04
2.10E-04
2.30E-04
2.50E-04
2.70E-04
0.8
0.85
0.9
0.95
1
1.05
1.1
1.15
Flow
Graph 1: Relaonship Between Coecient of Discharge And Flow
Graph 2: Relaonship Between Flow And Head
Graph 3: Relaonship Between Flow and Head
½
0.15
0.14
0.16
0.17
0.18
0.19
0.2
1.70E-04
1.90E-04
2.10E-04
2.30E-04
2.50E-04
2.70E-04
2.90E-04
Relaonship Between Flow And Head
Head
0.39
0.36
0.37
0.38
0.4
0.41
0.42
0.43
0.44
1.70E-04
1.90E-04
2.10E-04
2.30E-04
2.50E-04
2.70E-04
2.90E-04
Relaonship Between Flow and Head1/2
Head1/2
The slope of the linear results is 1.64x10
-3
The average (mean) coecient of discharge for the orice is 1.152
V. Conclusion
The experiment succeeds in fulling its objecves:
- to understand the relaonship between head and ow for an orice:
- to show how the coecient of discharge varies with ow
- to use the head and ow relaonship to nd the average coecient of
discharge for the orice.
The error in C
d
is determined by the error in measuring Q and H. Furthermore,
Q = where V is the volume collected in me t, the error of Q is determined by the
error in collecng me t.
Experiment 2: Horizontal Jet Trajectory
I. Objecve:
The objecve of the experiment is to understand the horizontal discharge
characteriscs of an orice or nozzle.
II. Theory:
Trajectory from Horizontal
Figure 3. Trajectory from Horizontal
The jet emerges from the nozzle at a velocity u
c
. At any point P in its trajectory it is
subject to gravitaonal acceleraon (g) in the vercal direcon, and has a steady
velocity component in the horizontal direcon. As gravity aects its path, the
trajectory should be parabolic. The head (H
o
) of water in the tank will aect the
horizontal distance travelled and therefore the curvature of the jet.
Consider a ‘packet’ of water that has travelled a distance x from the vena
contracta to point P in t seconds. It travels at velocity u
c
in the horizontal direcon,
(6)
And over the same me in the vercal direcon:
(7)
Eliminang t from the two equaons gives
(8)
and
(9)
and (10)
or (11)
and (12)
Where the head in the tank (H
o
) stays constant, you can nd an average value for
the velocity coecient from a chart of and x (see Figure 4). The chart should give
linear results. The inverse value of the gradient (m) of this chart substuted back
into Equaon 13 should give this average.
So: (13)
Note: Units of x, y and H
o
must be idencal (mm or metres)
Figure 4. Chart to help Find Velocity Coecient
III. Experimental Apparatus
Shown in part 3 of Experiment 1.
IV. Procedure
(1) Set the tank for a constant head.
Note: the head of this experiment will be the head of water with respect to
the centre line of the nozzle. The manometer measures with respect to the
boom of the base plate – roughly 22 mm lower.
(2) Refer to the base plate drawing in Technical Details to allow for this.
(3) Adjust the depth pins so they just touch the surface of the jet without
disturbing it.
(4) Mark the posions of the top of the pins onto the chart paper.
(5) Slowly reduce the head in the tank and note how it aects the jet.
(6) Switch o the water supply.
V. Data Analysis
Table 1: Report Table
Graph 1 is a chart of y
1/2
against x. Using the results of the h experiment which
is near to the predicted result to create the chart.
Head: 230 (mm)
x (mm)
Actual y
(
mm
)
y
2
1
/
(mm)
Predicted y (mm
)
0
225
0
15.0332
221
40
14.8660
1.74
205
14.3178
80
6.95
181
13.4536
120
15.65
153
12.3693
160
27.83
127
200
11.2694
43.47
9.7467
95
240
62.60
280
7.874
62
85.21
Graph 2 is a chart of the actual ow and the predicted. The predicted ow from
this experiment calculaon is quite close to what the ow is actually is. This can
be seen in Graph 2 below.
200
0
40
80
120
160
240
280
7
9
11
13
15
A chart of of the value
against x posion
A chart of of the value against x posion
Graph 1:
Chart of y
1
/2
against x
Graph 2: Actual Flow and predicted ow
VI. Conclusion
The experiment succeeds in fullling its objecve which is to understand the
horizontal discharge characteriscs of an orice or nozzle. Specically, the
experiment succeeds in using collected data to produce a predicted ow that is
quite close to the actual ow, which can be seen in Graph 2.
The dierent between the y predicted and the y actual may occurs because the
error in H
o
values or the error when reading the y values from the plong board.
0
80
120
160
200
240
280
40
0
50
100
150
200
250
228
221
207
186
161
130
92
58
0
1.74
6.95
15.65
27.83
43.47
62.6
85.21
| 1/13

Preview text:


Department of Civil Engineering International University (IU) Instructor: Prof. Pham Ngoc.
Date of submission: 14/04/2017
FLUID MECHANICS LABORATORY
JET TRAJECTORY AND FLOW THROUGH AN ORIFICE Group’s members: Nguyễn Văn Tú CECEIU15054 Lê Nhật Tú CECEIU15013
Nguyễn Dương Tấn Son CECEIU15044
Trương Nguyên Vũ CECEIU15033
Nguyễn Quốc Thắng CECEIU15048
Experiment 1: Head and Flow Relationship I. Objectives:
The objectives of the experiment are:
- to understand the relationship between head and flow for an orifice
- to show how the coefficient of discharge varies with flow.
- to use the head and flow relationship to find the average coefficient of discharge for the orifice.
The coefficient of discharge Cd is the ratio of the actual discharge to that which
would take place if the jet discharged at the idea velocity without any reduction of
area. The actual discharge Q is given by: (1)
and if the jet discharged at the idea velocity uo over the orifice area Ao, the the discharge Qo would be: (2)
So, from the definition of the coefficient of discharge, (3) Q u A
or in terms of quantities measured experimentally, (4)
Q= C d A o 2gHo = C dQ o Q C d = Ao 2gHo or (5) Q kH o k Cd = where
k C d A o 2g => Ao 2g
II. Experimental Apparatus
The experimental apparatus consists of the following parts:
Figure 1. General Layout
Table 2. Technical Details Item Details
Dimensions and weight 700 mm high x 700 mm long x 400 mm front to (assembled)
back. 10 kg including nozzles. Manometer scale 100 mm to 390 mm 1 division = 0.1 mm Pitot Micrometer 1 complete turn = 1 mm Set of four Orifice / Nozzles See Figure 2
Figure 2. Dimensions of the Orifice / Nozzle Dimension in mm
Datum = Distance to internal surface of tank when mounted vertically III. Procedure
(1) Start the pump of the hydraulic bench and adjust the flow so the level in the
tank stays just above the overflow pipe in the tank.
(2) Allow conditions to stabilize and use the hydraulic bench to measure the flow.
Record the Head inside the tank.
(3) Reduce the inlet flow (supply from the hydraulic bench) so that the head falls by about 30 mm.
(4) Allow conditions to stabilize and use the hydraulic bench to measure the flow.
Record the Head inside the tank.
(5) Repeat for decreasing value of head in about 30 mm steps, giving about eight
results over the height of the manometer scale, each time recording head and flow.
IV. Data Analysis
Relationship Between Coefficient of Discharge And Flow 1.15 1.1 1.05 1 0.95 0.9 0.85 0.8 1.70E-04 1.90E-04 2.10E-04 2.30E-04 2.50E-04 2.70E-04 2.90E-04 Flow
Graph 1: Relationship Between Coefficient of Discharge And Flow
Relationship Between Flow And Head 2.90E-04 2.70E-04 2.50E-04 2.30E-04 2.10E-04 1.90E-04 1.70E-04 0.14 0.15 0.16 0.17 0.18 0.19 0.2 Head
Graph 2: Relationship Between Flow And Head
Relationship Between Flow and Head1/2 2.90E-04 2.70E-04 2.50E-04 2.30E-04 2.10E-04 1.90E-04 1.70E-04 0.36 0.37 0.38 0.39 0.4 0.41 0.42 0.43 0.44 Head1/2
Graph 3: Relationship Between Flow and Head ½
The slope of the linear results is 1.64x10-3
The average (mean) coefficient of discharge for the orifice is 1.152 V. Conclusion
The experiment succeeds in fulling its objectives:
- to understand the relationship between head and flow for an orifice:
- to show how the coefficient of discharge varies with flow
- to use the head and flow relationship to find the average coefficient of discharge for the orifice.
The error in Cd is determined by the error in measuring Q and H. Furthermore,
Q = where V is the volume collected in time t, the error of Q is determined by the error in collecting time t.
Experiment 2: Horizontal Jet Trajectory I. Objective:
The objective of the experiment is to understand the horizontal discharge
characteristics of an orifice or nozzle. II. Theory:
Trajectory from Horizontal
Figure 3. Trajectory from Horizontal
The jet emerges from the nozzle at a velocity uc. At any point P in its trajectory it is
subject to gravitational acceleration (g) in the vertical direction, and has a steady
velocity component in the horizontal direction. As gravity affects its path, the
trajectory should be parabolic. The head (Ho) of water in the tank will affect the
horizontal distance travelled and therefore the curvature of the jet.
Consider a ‘packet’ of water that has travelled a distance x from the vena
contracta to point P in t seconds. It travels at velocity uc in the horizontal direction, (6)
And over the same time in the vertical direction: (7)
Eliminating t from the two equations gives (8) and (9) and (10) or (11) and (12)
Where the head in the tank (Ho) stays constant, you can find an average value for
the velocity coefficient from a chart of and x (see Figure 4). The chart should give
linear results. The inverse value of the gradient (m) of this chart substituted back
into Equation 13 should give this average. So: (13)
Note: Units of x, y and Ho must be identical (mm or metres)
Figure 4. Chart to help Find Velocity Coefficient
III. Experimental Apparatus
Shown in part 3 of Experiment 1. IV. Procedure
(1) Set the tank for a constant head.
Note: the head of this experiment will be the head of water with respect to
the centre line of the nozzle. The manometer measures with respect to the
bottom of the base plate – roughly 22 mm lower.
(2) Refer to the base plate drawing in Technical Details to allow for this.
(3) Adjust the depth pins so they just touch the surface of the jet without disturbing it.
(4) Mark the positions of the top of the pins onto the chart paper.
(5) Slowly reduce the head in the tank and note how it affects the jet.
(6) Switch off the water supply. V. Data Analysis Table 1: Report Table Head: 230 (mm) Actual y x (mm) ( mm )
y 1 /2 (mm) Predicted y (mm ) 0 225 15.0332 0 40 221 14.8660 1.74 80 205 14.3178 6.95 120 181 13.4536 15.65 160 153 12.3693 27.83 200 127 11.2694 43.47 240 95 9.7467 62.60 280 62 7.874 85.21
Graph 1 is a chart of y1/2 against x. Using the results of the fifth experiment which
is near to the predicted result to create the chart.
A chart of of the value against x position 15 13 11 9 7 0 40 80 120 160 200 240 280
A chart of of the value against x position
Graph 1: Chart of y 1 /2 against x
Graph 2 is a chart of the actual flow and the predicted. The predicted flow from
this experiment calculation is quite close to what the flow is actually is. This can
be seen in Graph 2 below. 250 228 221 207 200 186 161 150 130 100 92 85.21 62.6 58 50 43.47 27.83 0 0 1.74 6.95 15.65 0 40 80 120 160 200 240 280
Graph 2: Actual Flow and predicted flow VI. Conclusion
The experiment succeeds in fulfilling its objective which is to understand the
horizontal discharge characteristics of an orifice or nozzle. Specifically, the
experiment succeeds in using collected data to produce a predicted flow that is
quite close to the actual flow, which can be seen in Graph 2.
The different between the y predicted and the y actual may occurs because the
error in Ho values or the error when reading the y values from the plotting board.