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Water Temperature: 298K Density: 1000kg/m 3 Viscosity: 0.91 CP 0.00091N.s/m 2 Test Section Diameter: 10.25 MM 0.01025m Area (M) : 0.008252m 2

The document contains experimental data measuring the flow rate of water through a test section with varying heights. Key parameters recorded include water temperature, density, viscosity, test section diameter, area, quantity and time of water collected, mean velocity, Reynolds number, inlet and outlet heads, friction head loss, friction factor, and volume flow rate. Graphs of log(V) versus log(hf) were to be plotted from the experimental data.

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0% found this document useful (0 votes)
75 views3 pages

Water Temperature: 298K Density: 1000kg/m 3 Viscosity: 0.91 CP 0.00091N.s/m 2 Test Section Diameter: 10.25 MM 0.01025m Area (M) : 0.008252m 2

The document contains experimental data measuring the flow rate of water through a test section with varying heights. Key parameters recorded include water temperature, density, viscosity, test section diameter, area, quantity and time of water collected, mean velocity, Reynolds number, inlet and outlet heads, friction head loss, friction factor, and volume flow rate. Graphs of log(V) versus log(hf) were to be plotted from the experimental data.

Uploaded by

AfifaFarooq
Copyright
© © All Rights Reserved
We take content rights seriously. If you suspect this is your content, claim it here.
Available Formats
Download as DOCX, PDF, TXT or read online on Scribd
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Water Temperature: 298K

Density: 1000kg/m^3
Viscosity: 0.91 cp ; 0.00091N.s/m^2
Test Section Diameter: 10.25 mm; 0.01025m
Area(m) : 0.008252m^2

Height (cm)

15

20

25

30

35

Quantity of
water
collected Q(l)

Trial1

0.380

0.270

0.305

0.205

0.305

Trial2

0.475

0.315

0.260

0.200

0.300

Time taken to
collect water
t(s)

Trial1

2.7

1.9

2.5

2.4

4.1

Trial2

4.0

2.5

3.0

2.2

4.0

Trial1

8.444
4

8.5263

7.320
0

5.1250

4.463
4

Trial2

7.125

7.5600

5.200
0

5.4546

4.500
0

Qavg

7.784
7

8.0431
5

6.260
0

5.2898

4.481
7

Mean Velocity
V (m/s)

0.015
723

0.0165
698

0.012
896

0.0108
976

0.009
233

Log V

1.795
85

1.7806
8

1.889
54

1.9626
7

2.034
66

Reynolds Number
Re

177.1

186.64

145.2
6

122.75

103.9
98

Log Re

2.248
22

2.2710
0

2.162
15

2.0890
22

2.017
024

Inlet Head
h1(mm)

325

347

367

393

410

Oulet Head
h2 (mm)

115

168

219

285

334

Friction Head Loss


hf(mm)

210

179

148

108

76

Log hf

2.322
22

2.2528
6

2.170
262

2.0334
24

1.880
814

Friction Factor

0.361

0.3429

0.440

0.5213

0.615

Volume Flow
Rate
Q (l/min)

f'

378

06

589

85

396

Log f'

0.442
04

0.4682
5

0.355
97

0.2828
4

0.210
85

Sample Calculation
1. Area= (/4)*D^2
= 0.008252
2. Q= Volume/ Time
= 0.380/0.045 = 8.4444
3. Mean Velocity = Qave/A
= 7.7847*(0.001/60)/0.008252
= 0.015723
4. Log (V) = log (0.015723) = -1.79585
5. Re = Density*Mean velocity*Diameter/Viscosity
= 1000*0.015723*0.01025/0.00091
= 177.1
6. Log (Re) = log (177.1) = 2.24822
7. Hf = h1-h2
= 325-115
= 210
8. Log (Hf) = log (210) = 2.32222

9. f`= 64/ Re
= 64/177.1
= 0.361378
10. Log (f`) = log(0.361378) = -0.442039

Data to be graphed
Log(V)
Log(hf)

-1.79585
2.32222

-1.78068
2.25286

-1.88954
2.170262

-1.96267
2.033424

-2.03466
1.880814

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