Explanations & Calculations
- Assume the fluid is incompressible.
- Therefore, the flow rate is constant hence the velocity of the fluid at the enlargement can be calculated to be,
v2=A2A1v1=d22d12v1=9262×7ms−1=3.11ms−1
- With the head loss due to similar variations in pipe lines (as discussed here) the Bernoulli equation (energy equation) can be written as,
h1+2gv12+ρgP12gv12+ρgP1=h2+2gv22+ρgP2+hloss=2gv22+ρgP2+hloss⋯(1)
- Head loss could occur due to several reasons & that due to these kinds of variations is calculated as follows.
hloss=KL×2gv12−v22=0.133×2×9.8ms−2(7ms−1)2−(3.11ms−1)2=0.2669m
- Now using equation (1) the pressure can be calculated to be,
2(9.8)72+1000×9.8150kPaP2=2(9.8)3.112+1000×9.8P2+0.2669=17198.33kPa
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