(1)A stream of water of diameter d= 0.100 mflows steadily from a tank of diameter D= 1.00 m as shown in Fig. 1. Determine the flow rate, Q, needed from the inflow pipe if the water depth remains constant, h= 2.00 m. (2)Kerosene (SG = 0.850) flows through the Venturi meter shown in Fig. 2 with flowrates between 5.00103and 50.0103m3/s.Determine the range in pressure difference, P1P2needed to measure these flowrates.
(1)A stream of water of diameter d= 0.100 mflows steadily from a tank of diameter D= 1.00 m as shown in Fig. 1. Determine the flow rate, Q, needed from the inflow pipe if the water depth remains constant, h= 2.00 m. (2)Kerosene (SG = 0.850) flows through the Venturi meter shown in Fig. 2 with flowrates between 5.00103and 50.0103m3/s.Determine the range in pressure difference, P1P2needed to measure these flowrates.
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(1)A stream of water of diameter d= 0.100 mflows steadily from a tank of diameter D= 1.00 m as shown in Fig. 1. Determine the flow rate, Q, needed from the inflow pipe if the water depth remains constant, h= 2.00 m.
(2)Kerosene (SG = 0.850) flows through the Venturi meter shown in Fig. 2 with flowrates between 5.00103and 50.0103m3/s.Determine the range in pressure difference, P1P2needed to measure these flowrates.

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(1) A stream of water of diameter d= 0.100 m flows steadily from a tank of diameter D
= 1.00 m as shown in Fig. 1. Determine the flow rate, Q, needed from the inflow pipe if
the water depth remains constant, h = 2.00 m.
(1)
(2) Kerosene (SG
0.850) flows through the
Kerosene, SG = 0.85
D = 1.0 m
Venturi meter shown in Fig. 2 with flowrates
h = 2.0 m
D = 0.1 m
between 5.00x10-3 and 50.0×10-3 m²/s. Determine
(2) • D, = 0.06 m
(1)
|(2)
the range in pressure difference, P1- P2 needed to
0.005 m/s s Q s0.050 m³/s
measure these flowrates.
d = 0.10 m
Fig. 2
Fig. 1
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