FLUID MECHANICS-EBOOK>I<
2nd Edition
ISBN: 2819480256061
Author: HIBBELER
Publisher: INTER PEAR
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Chapter 10, Problem 72P
To determine
The flow rate in each branch.
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Chapter 10 Solutions
FLUID MECHANICS-EBOOK>I<
Ch. 10 - Prob. 1FPCh. 10 - Water at a temperature of 25°C is pumped through...Ch. 10 - Water at a temperature of 25°C flows through a...Ch. 10 - SAE 10W30 oil flows from one tank to another when...Ch. 10 - The tank is filled with water at a temperature of...Ch. 10 - Prob. 1PCh. 10 - Prob. 2PCh. 10 - Prob. 3PCh. 10 - Prob. 4PCh. 10 - Determine the flow of methane at T = 68°F in ft3/h...
Ch. 10 - Water in the old 15-in.-diameter concrete drain...Ch. 10 - Water at 20°C flows upwards through the...Ch. 10 - Water at 60°F is delivered horizontally through a...Ch. 10 - A horizontal 40-ft-long galvanized iron pipe...Ch. 10 - Air at 80°F flows through the commercial steel...Ch. 10 - If the pressure drop along the 10-ft-long...Ch. 10 - Prob. 12PCh. 10 - Prob. 13PCh. 10 - Determine the greatest air flow Q through the...Ch. 10 - Water in the concrete detention pond is to be...Ch. 10 - Water is pumped from the river through a...Ch. 10 - Prob. 17PCh. 10 - Prob. 18PCh. 10 - The 20-mm-diameter copper coil is used for a solar...Ch. 10 - Water at T = 70°F flows through the...Ch. 10 - Prob. 21PCh. 10 - A 450-ft-long horizontal commercial steel pipe...Ch. 10 - Air at 60°F is transported by the fan at the rate...Ch. 10 - A cast iron pipe having a diameter of 100 mm is...Ch. 10 - A cast iron pipe having a diameter of 100 mm is...Ch. 10 - Water at 70°F flows through the 3-in.-diameter...Ch. 10 - Prob. 27PCh. 10 - A 150-mm-diameter galvanized iron pipe is used to...Ch. 10 - Prob. 29PCh. 10 - Water at 80°F is pumped from the well through a...Ch. 10 - Prob. 31PCh. 10 - Prob. 32PCh. 10 - A 75-mm-diameter galvanized iron pipe, having a...Ch. 10 - Prob. 34PCh. 10 - Prob. 35PCh. 10 - Prob. 36PCh. 10 - Prob. 37PCh. 10 - Prob. 38PCh. 10 - Prob. 39PCh. 10 - Prob. 40PCh. 10 - Prob. 41PCh. 10 - Sewage, assumed to be water where ρ = 998.3 kg/m3,...Ch. 10 - Sewage, assumed to be water where ρ = 998.3 kg/m3,...Ch. 10 - Determine the power the pump must supply in order...Ch. 10 - Prob. 45PCh. 10 - Prob. 46PCh. 10 - Prob. 47PCh. 10 - Prob. 48PCh. 10 - Prob. 49PCh. 10 - The sump pump is required to lift water from the...Ch. 10 - The submersible pump is used to fill the...Ch. 10 - Prob. 52PCh. 10 - Prob. 53PCh. 10 - The pressure of air in a large tank at A is 40...Ch. 10 - The 100-mm-diameter commercial steel pipe...Ch. 10 - The 100-mm-diameter commercial steel pipe...Ch. 10 - Prob. 57PCh. 10 - Water flows at 900 gal/min through the...Ch. 10 - Water at 20°C flows through the 20-mm-diameter...Ch. 10 - Water at 80°F flows at 5 ft/s through the...Ch. 10 - Water at 80°F flows at 5 ft/s through the...Ch. 10 - Water at 15°C is pumped from the reservoir A into...Ch. 10 - Water at 80°F flows from the large reservoir...Ch. 10 - Water at 50°F flows through the 2-in.-diameter...Ch. 10 - An automatic sprinkler system for a yard is made...Ch. 10 - Water at 70°F is pumped through the two commercial...Ch. 10 - Prob. 67PCh. 10 - Prob. 68PCh. 10 - Water at 25°C is pumped into the galvanized iron...Ch. 10 - Prob. 70PCh. 10 - The two water tanks are connected together using...Ch. 10 - Prob. 72PCh. 10 - Prob. 73P
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- A gas mixture with a molar analysis of 40% CH4 (methane) and 60% air enters a control volume operating at steady state at location 1 with a mass flow rate of 5 kg/min, as shown in the figure below. Air enters as a separate stream at 2 and dilutes the mixture. A single stream exits with a mole fraction of methane of 5%. Assume air has a molar analysis of 21% O2 and 79% N2. (CH4, Air) m₁ = = 5 kg/min Air (21% O2, 79% N₂) 3 + (5% CH4, 95% Air)arrow_forwardA. Calculate the cutting time if the length of cut is 24 in., the feed rate is 0.030 ipr, and the cutting speed is 80 fpm. The allowance is 0.5 in and the diameter is 8 in. B. Calculate the metal removal rate for machining at speed of 80 fpm, feed of 0.030 ipr, at a depth of 0.625 in. Use data from the previous problem.arrow_forwardConsider 0.65 kg of N2 at 300 K, 1 bar contained in a rigid tank connected by a valve to another rigid tank holding 0.3 kg of CO2 at 300 K, 1 bar. The valve is opened and gases are allowed to mix, achieving an equilibrium state at 290 K. Determine: (a) the volume of each tank, in m³. (b) the final pressure, in bar. (c) the magnitude of the heat transfer to or from the gases during the process, in kJ. (d) the entropy change of each gas and of the overall system, in kJ/K.arrow_forward
- A gas mixture with a molar analysis of 40% CH4 (methane) and 60% air enters a control volume operating at steady state at location 1 with a mass flow rate of 5 kg/min, as shown in the figure below. Air enters as a separate stream at 2 and dilutes the mixture. A single stream exits with a mole fraction of methane of 5%. Assume air has a molar analysis of 21% O2 and 79% N2. (CH4, Air) m₁ = = 5 kg/min Air (21% O2, 79% N₂) 3 + (5% CH4, 95% Air)arrow_forwardA gas mixture with a molar analysis of 40% CH4 (methane) and 60% air enters a control volume operating at steady state at location 1 with a mass flow rate of 5 kg/min, as shown in the figure below. Air enters as a separate stream at 2 and dilutes the mixture. A single stream exits with a mole fraction of methane of 5%. Assume air has a molar analysis of 21% O2 and 79% N2. (CH4, Air) m₁ = = 5 kg/min Air (21% O2, 79% N₂) 3 + (5% CH4, 95% Air)arrow_forwardArgon (Ar), at T₁ = 350 K, 1 bar with a mass flow rate of m₁ 3 kg/s enters the insulated mixing chamber shown in the figure below and mixes with carbon dioxide (CO2) entering as a separate stream at 575 K, 1 bar with a mass flow rate of 0.5 kg/s. The mixture exits at 1 bar. Assume ideal gas behavior with k = 1.67 for Ar and k = 1.25 for CO2. Argon (Ar) P₁ = 1 bar mT For steady-state operation, determine: (a) the molar analysis of the exiting mixture. (b) the temperature of the exiting mixture, in K. (c) the rate of entropy production, in kW/K. Insulation 3 + Mixture exiting P3 = 1 bar 2+ Carbon dioxide (CO2) T₂ = 575 K P2 = 1 bar m2 = 0.5 kg/sarrow_forward
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