Problem 5: Determine a) the weight of the water contained in the conical nozzle and b) the anchoring force required to hold in place the nozzle attached to the end of a lab sink faucet, when the water flowrate is 10 gal/min. The nozzle weight is 0.2 lb. The nozzle inlet and exit inside diameters are 0.6 and 0.2 in., respectively. The nozzle axis is vertical and the axial distance between sections (1) and (2) is 1.2 in. The pressure at section (1) is 68 psig and water exits as free jet from section-2. Neglect viscous effects. Given: pwter = 1.94 slugs/ft'; 1 gallon = 0.1336 ft’; Assume: Steady, incompressible flow; y axis vertically upward; uniform velocity distribution at (1) and (2);

Elements Of Electromagnetics
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Problem 5: Determine a) the weight of the water contained in the conical nozzle and b) the
anchoring force required to hold in place the nozzle attached to the end of a lab sink faucet, when
the water flowrate is 10 gal/min. The nozzle weight is 0.2 lb. The nozzle inlet and exit inside
diameters are 0.6 and 0.2 in., respectively. The nozzle axis is vertical and the axial distance
between sections (1) and (2) is 1.2 in. The pressure at section (1) is 68 psig and water exits as free
jet from section-2. Neglect viscous effects. Given: pwaer = 1.94 slugs/ft; 1 gallon = 0.1336 ft';
Assume: Steady, incompressible flow; y axis vertically upward; uniform velocity distribution at
(1) and (2);
D7 =
0.6 in.
Section (1)
1.2 in.
Section (2).
FD2 = 0.2 in.
Q= 10 gal/min
Transcribed Image Text:Problem 5: Determine a) the weight of the water contained in the conical nozzle and b) the anchoring force required to hold in place the nozzle attached to the end of a lab sink faucet, when the water flowrate is 10 gal/min. The nozzle weight is 0.2 lb. The nozzle inlet and exit inside diameters are 0.6 and 0.2 in., respectively. The nozzle axis is vertical and the axial distance between sections (1) and (2) is 1.2 in. The pressure at section (1) is 68 psig and water exits as free jet from section-2. Neglect viscous effects. Given: pwaer = 1.94 slugs/ft; 1 gallon = 0.1336 ft'; Assume: Steady, incompressible flow; y axis vertically upward; uniform velocity distribution at (1) and (2); D7 = 0.6 in. Section (1) 1.2 in. Section (2). FD2 = 0.2 in. Q= 10 gal/min
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