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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
Water “t”

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
Water “t”

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

  1. 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.
  2. 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.

  1. The differences between the exponents “n=0.989” obtained from the power regression fit and the theoretical value of 2.0 is 1.011.
  1. 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.
  1. The potential sources of error are:-
  2. Systematic error: – in this, calibration of the instrument may not be done properly.
  3. Human Error: – While taking reading, if we add or remove masses, this is always associated.

Assumptions:

  1. It is based on Newton’s second law; a so first assumption was there has to be unbalanced force.
  2. Fluid is incompressible and steady.

REFERENCES

 

  1. Engineering Fluid Mechanics by John Wiley and Sons,11 Edition.
  2. Pelton Wheel Water Turbine, Ron Amberger’s