Object
To determine minor losses due to gradual expansion and constriction in the pipe diameter.
Apparatus
Fluid friction apparatus; Hydraulics bench and Stop watch.
![Word Image 2947 1](https://smartcivilengineers.com/wp-content/uploads/2024/06/word-image-2947-1.jpeg)
Fig. Fluid friction apparatus
Theory
- Gradual Expansion:
The value of loss coefficient for gradual expansion is function of the two radii, as shown below
![Word Image 2947 2](https://smartcivilengineers.com/wp-content/uploads/2024/06/word-image-2947-2.jpeg)
In the fluid friction apparatus, D1 = 17 mm and D2 = 28.4 mm, hence D1/D2 = 0.6, hence Ke
should be 0.15.
For sake of verification of the value of loss coefficient due to gradual expansion in the pipe diameter we use the relationship
V 2
where
hle
K 1
2g
e
(1)
hle = loss of head due to gradual expansion in the pipe diameter
V1 = velocity of flow at section-1 = Q/A1
where,Area of flow at section-1 =
A 2
41
1
d
3.14
4
(1.7)2
2.27
cm2
(since d1 = 17 mm = 1.7 cm)
Putting values in Eq.(1),
K 2g
1
V
e
2
.hle
2 981
(Q / 2.27)2
.hle
10108.2 hle
Q2
(2)
- Gradual Constriction:
Similarly, the value of loss coefficient for gradual constriction is function of the two radii, as shown below
![Word Image 2947 3](https://smartcivilengineers.com/wp-content/uploads/2024/06/word-image-2947-3.jpeg)
In the fluid friction apparatus, D1 = 28.4 mm and D2 = 17 mm, hence D2/D1 = 0.6, hence Kc
should be 0.06.
For sake of verification of the value of loss coefficient due to gradual constriction in the pipe diameter we use the relationship
V 2
where
hlc
K 2
2g
c
(3)
hlc = loss of head due to gradual constriction in the pipe diameter
V2 = velocity of flow at section-2 = Q/A2 where,Area of flow at section-2 =
A 2
2
d
42
3.14
4
(1.7)2
2.27
cm2
(since d2 = 17 mm = 1.7 cm)
Putting values in Eq.(3),
K 2g
2
V
c
2
.hlc
2 981
(Q / 2.27)2
.hlc
10108.2 hlc
Q2
(4)
Procedure
- Fill tank of hydraulics bench with clean water.
- Connect the fluid friction apparatus with hydraulics bench.
- Open the valve(s) that allows flow to the section under consideration and close all the irrelevant valves of the pipe friction apparatus.
- Connect the two ends of the tubes to the pressure tapping nipples at the either side of the pair of the elbows and the manometer.
- Slightly open the Flow control valve at the hydraulics bench.
- Remove air bubbles from the tubes by opening the Vent valve and Drain valves of differential manometer.
- Read the heads in the monometers corresponding to the pressure along entry and exit of the sections under consideration.
- Collect water in the volumetric measuring section of the hydraulics bench. Read the volume collected as well as time taken to collect that volume of water.
- Open the Flow control valve at the hydraulics bench slightly more for taking new reading.
- Repeat steps 7 and 8 to observe new readings.
- Carry out computations as per table below and compare the average value of Ke and
Kc with those given in literature as discussed above.
Observations and Calculations
S. No. | Discharge (cm3/sec) | Gradual Expansion | Gradual Constriction | |||||||||
| t | Q = | h1 | h2 | hle = h1 – h2 | Ke 10108.2 hle Q2 | h1 | h2 | hlc = h1 – h2 | Kc 10108.2 hlc Q2 | ||
(lit) | (cm3) | (sec) | (cm3/sec) | (cm) | (cm) | (cm) | (cm) | (cm) | (cm) | |||
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