FLUID MECHANICS
IMPULSE MOMENTUM PRINCIPLE TEST
RESULTS AND DISCUSSION
Flat Plate |
|||||||
Nozzle diameter |
0.008 |
m |
|||||
Area of nozzle |
5.0265 x10-5 |
m2 |
|||||
Density of water |
998 |
kg/m3 |
|||||
Deflector angle “a (degrees) |
Mass Applied on spring “W” |
Volume of water |
Time to Collect |
Flow Rate “Q” |
Experimental force (Direct Force) |
Theoretical Force (Indirect Force) |
|
degrees |
kg |
L |
M3 |
s |
m3/s |
N |
N |
0 |
0 |
0 |
0 |
0 |
0.0000 |
|
|
0 |
0.1 |
15 |
0.015 |
66.08 |
0.0002 |
0.981 |
1.0231 |
0 |
0.2 |
15 |
0.015 |
46.09 |
0.0003 |
1.962 |
2.1030 |
0 |
0.3 |
15 |
0.015 |
38.6 |
0.0004 |
2.943 |
2.9983 |
0 |
0.4 |
15 |
0.015 |
33.75 |
0.0004 |
3.924 |
3.9219 |
0 |
0.5 |
20 |
0.02 |
40.47 |
0.0005 |
4.905 |
4.8491 |
0 |
0.6 |
20 |
0.02 |
36.53 |
0.0005 |
5.886 |
5.9515 |
0 |
0.7 |
20 |
0.02 |
33.75 |
0.0006 |
6.867 |
6.9723 |
0 |
0.8 |
25 |
0.025 |
39.62 |
0.0006 |
7.848 |
7.9053 |
0 |
0.85 |
25 |
0.025 |
37.52 |
0.0007 |
8.3385 |
8.8149 |
|
|
|
|
Average |
0.0005 |
4.8505 |
4.9488 |
Table 1 Data collected in laboratory and calculated forces for the Flat Plate
Fig.1 Plot Direct and Indirect Force for the flat plate
Fig.2 Plot Direct Force vs volume flow rate” Q” for the flat plate
HEMISPHERICAL CUP |
|||||||
Nozzle diameter |
0.008 |
m |
|||||
Area of nozzle |
5.0265 x10-5 |
m2 |
|||||
Density of water |
998 |
kg/m3 |
|||||
Deflector angle “a (degrees) |
Mass Applied on spring “W” |
Volume of water |
Time to Collect |
Flow Rate “Q” |
Experimental force (Direct Force) |
Theoretical Force (Indirect Force) |
|
degrees |
kg |
L |
M3 |
s |
m3/s |
N |
N |
0 |
0 |
0 |
0 |
0 |
0.0000 |
|
|
0 |
0.1 |
15 |
0.015 |
66.08 |
0.0002 |
0.981 |
2.0461 |
0 |
0.2 |
15 |
0.015 |
46.09 |
0.0003 |
1.962 |
4.2059 |
0 |
0.3 |
15 |
0.015 |
38.6 |
0.0004 |
2.943 |
5.9966 |
0 |
0.4 |
15 |
0.015 |
33.75 |
0.0004 |
3.924 |
7.8439 |
0 |
0.5 |
20 |
0.02 |
40.47 |
0.0005 |
4.905 |
9.6981 |
0 |
0.6 |
20 |
0.02 |
36.53 |
0.0005 |
5.886 |
11.9030 |
0 |
0.7 |
20 |
0.02 |
33.75 |
0.0006 |
6.867 |
13.9446 |
0 |
0.8 |
25 |
0.025 |
39.62 |
0.0006 |
7.848 |
15.8105 |
0 |
0.85 |
25 |
0.025 |
37.52 |
0.0007 |
8.3385 |
17.6299 |
|
|
|
|
Average |
0.0005 |
4.8505 |
9.8976 |
Table 2 Data collected in laboratory and calculated forces for the Hemispherical Plate
Fig.3 Plot Direct and Indirect Force for the hemispherical plate
Fig.4 Plot Direct Force vs volume flow rate”Q” for the hemispherical plate
Lower 95.0% |
Upper 95.0% |
Standard Error |
-0.203736216 |
0.288197694 |
0.104019 |
0.927310645 |
1.015889726 |
0.01873 |
Table 3 Upper and lower 95% confidence data for the flat plate
Lower 95.0% |
Upper 95.0% |
Standard Error |
-0.203736216 |
0.288197694 |
0.104019 |
0.463655322 |
0.507944863 |
0.009365 |
Table 4 Upper and lower 95% confidence data for the hemispherical plate
Fig.5 Plot Direct Force vs volume flow rate” Q” for the flat plate
Fig.6 Plot Direct Force vs volume flow rate” Q” for the hemispherical plate
Flat Plate |
Hemispherical Sphere |
||
Q |
Direct Force |
Q |
Direct Force |
m3/s |
N |
m3/s |
N |
|
|
||
1 |
0.989 |
1 |
0.989 |
1.4 |
1.379484798 |
1.4 |
1.3794848 |
2.2 |
2.157010817 |
2.2 |
2.15701082 |
3.1 |
3.027980031 |
3.1 |
3.02798003 |
3.9 |
3.799786434 |
3.9 |
3.79978643 |
Table 5 Calculating direct force with the curve for the both flat and hemispherical plate
CONCLUSION
- For flat plate, the maximum and a minimum indirect force for flat plate was 8.8149 N and 1.0231 N respectively. While the maximum and minimum direct forces were 0.981 N and 8.3385 N respectively. For the hemispherical plate, the maximum and minimum indirect force for the flat plate was 17.629 N and 2.0461 N respectively. While the maximum and minimum direct forces were 8.3385 N and 0.981 N respectively.
- The linear equation obtained F direct = 0.948 F indirect + 0.109. The squared value of R is 0.997. The value of slope (b) is 0.948
The differences between the values of the slope “b” obtained from the regression and the theoretical value of 1.0 is 0.052.
- The differences between the exponents “n=0.989” obtained from the power regression fit and the theoretical value of 2.0 is 1.011.
- The overall average for the ratio from the table 6 is 2.270652416. Compared to average value are 2.0. The Difference is 0.2706.
- The potential sources of error are:-
- Systematic error: – in this, calibration of the instrument may not be done properly.
- Human Error: – While taking reading, if we add or remove masses, this is always associated.
Assumptions:
- It is based on Newton’s second law; a so first assumption was there has to be unbalanced force.
- Fluid is incompressible and steady.
REFERENCES
- Engineering Fluid Mechanics by John Wiley and Sons,11 Edition.
- Pelton Wheel Water Turbine, Ron Amberger’s