Applied Fluid Mechanics (7th Edition)
Applied Fluid Mechanics (7th Edition)
7th Edition
ISBN: 9780132558921
Author: Robert L. Mott, Joseph A. Untener
Publisher: PEARSON
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Chapter 16, Problem 16.14PP

Seawater (sg 5 1.03) enters a heat exchanger through a reducing bend connecting a 4 -in Type K copper tube with a 2 -in Type K tube. The pressure upstream from the bend is 825 kPa Calculate the force required to hold the bend in equilibrium. Consider the energy loss in the bend, assuming it has a resistance coefficient K of 3.5 based on the inlet velocity. The flow rate is 0.025   m 3 / s .

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For an inlet valve, the mass flow rate through the valve is 0.44 kg/s. The flow coefficient is 0.62 and the cylinder pressure is 105 kPa. Assume intake system pressure and temperature are 180 kPa and 527 K, the specific heat ratio is 1.3 and R =287 J / kg.K. The area of the valve is (SI unit): Select one: a. 2.30*10-3 O b. 3.45*10-2 O c. 1.43*10-3 O d. 1.75*10-3 O e. 0.85*10-2
4. A heat exchanger creates energy loss in the fluid system shown below. Water at 50°C flows vertically upward at a constant volume flow rate of 6 x 10-3 m³/s. A mercury manometer is used to measure pressure difference between points 1 and 2. Evaluate the total energy loss (in a unit of m) between points 1 and 2. Using the velocity in the inlet tube, evaluate the minor loss coefficient K corresponding to the heat exchanger. The pipe geometry and mercury manometer setup are indicated in the figure. In the figure, OD indicates the outer diameter of pipe. The specific weights of water and mercury are water = Pwater9 = 9.81 kN/m³ and 133.7 kN/m³, respectively. Ignore the volume flow rate of water into or out of the mercury manometer, but one cannot ignore the contribution of water to the manometer measurement. A Flow 1200 mm Y Water 100-mm OD X 3.5-mm wall steel hydraulic tube Heat exchanger. 1250 mm 350 mm Y Mercury -50-mm OD x 2.0-mm wall steel hydraulic tube
Example -5.2- It is required to pump cooling water from storage pond to a condenser in a process plant situated 10 m above the level of the pond. 200 m of 74.2 mm i.d. pipe is available and the pump has the characteristics given below. The head loss in the condenser is equivalent to 16 velocity heads based on the flow in the 74.2 mm pipe. If the friction factor = 0.003, estimate the rate of flow and the power to be supplied to the pump assuming n = 0.5 Q (m³/s) 0.0028 0.0039 0.005 0.0056 0.0059 Ah (m) 23.2 21.3 18.9 15.2 11.0

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