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- 4. An experimental test rig is used to examine two-phase flow regimes in horizontal pipelines. A particular experiment involved uses air and water at a temperature of 25°C, which flow through a horizontal glass tube with an internal diameter of 25.4 mm and a length of 40 m. Water is admitted at a controlled rate of 0.026 kgs-¹ at one end and air at a rate of 5 x 104 kgs¹ in the same direction. The density of water is 1000 kgm3, and the density of air is 1.2 kgm-³. Determine the mass flow rate, the mean density, gas void fraction, and the superficial velocities of the air and water. Answer: 0.02605 kgs-1, 61.1 kgm ³, 0.94, 0.822 ms-1, 0.051 ms-14. An experimental test rig is used to examine two-phase flow regimes in horizontal pipelines. A particular experiment involved uses air and water at a temperature of 25°C, which flow through a horizontal glass tube with an internal diameter of 25.4 mm and a length of 40 m. Water is admitted at a controlled rate of 0.026 kgs¹ at one end and air at a rate of 5 x 104 kgs-¹ in the same direction. The density of water is 1000 kgm 3, and the density of air is 1.2 kgm 3. Determine the mass flow rate, the mean density, gas void fraction, and the superficial velocities of the air and water. Answer: 0.02605 kgs-¹, 61.1 kgm-³, 0.94, 0.822 ms-¹, 0.051 ms-¹3. Vertical turbines are to be used for flocculation in a water treatment plant with a design flow rate of 189,270 m³/day. Flocculation is to be designed with two trains and five compartments per train. The total detention time in this process is to be 25 minutes, and the average temperature of the water flowing into the plant is 10°C. The velocity gradient in the first compartment is to be 70 s¹. Make the following design decisions for the first compartment: a) Determine the dimensions of the compartment. b) Determine the diameter of the impeller. c) Determine the water power required. d) Determine the maximum rotational speed. e) Estimate the pumping capacity of the impeller and circulation time in the tank.
- 3. A natural gas is flowing through a long distance smooth pipeline (1 m in diameter) at a constant temperature. The gas enters the pipeline at a velocity of 12 m s-1 and at the temperature and pressure of 20 °C and 690 kPa, respectively. Compressors and coolers are provided every 15 km along the pipeline to recompress and cool the gas to its initial temperature and pressure. Calculate the theoretical power requirement to compress the gas by each compressor. Assume that the compression is an adiabatic frictionless process and the work done by the compressor on unit mass of gas is given by: AW = Pout vdP [J kg-¹] Pin where Pin and Pout are the pressures at the inlet and outlet of the compressor, respectively, and vis the specific volume of gas. Hint: see Coulson and Richardson, Volume 1, Section 8.3.4, page 347-351. Specific heat ratio y (= C₂/C₂) = 1.3 [Ans. 845631 W]S CE - Oil is transported from A to B along a pipe of constant diameter. The pipe is inclined at 50° to the horizontal and B is at the higher elevation. Considering the flow from A to B, which statement is correct? O The pressure head is decreasing and the velocity head is increasing. O The pressure head is increasing and the velocity head is decreasing. O The pressure head and velocity head are both increasing. O The pressure head is decreasing and the velocity head is constant. O The pressure head and velocity head are both decreasing. P Type here to search 0022 10°C Sunny AG A Q0 ENG 16/02/2022 DELL Esc F6 FB num 2 4€ E R Y F G J K ck D %23 B N M end V page page up ctri alt gr alt4- Consider the fully developed flow of glycerin at 40°C through a 70-m-long, 2-cm-diameter, horizontal, circular pipe. If the flow velocity at the centerline is measured to be 6 m/s, determine: a. the velocity profile b. the pressure difference across this 70-m-long section of the pipe, c. the useful pumping power required to maintain this flow. For glycerin at 40°C, μ = 0.3073 kg/m.s, p=1252 kg/m³ D = 2 cm 70 m 6 tri/s Glycerine
- RefrigerationSaturated liquid water is flowing at a mass flow rate of m = 6 kg/s through a smooth, horizontal tube with a rectangular cross-section. Cross-section of rectangle: w= 0.2 m , h= 0.3m and tube length L= 40 m The wall of the tube is maintained at a constant temperature of T = 85°C and the water enters the tube at a mean temperature of T_m,i = 27 °C. a.) What's the average convection coefficient between the water and the tube wall. Assume water temp is T = 85°C b.) What's the exit temperature of the water and the c.) Rate of heat transfer to the water?What’s the answer for this please ?
- Q2. Forced convective heat transfer coefficient depends on type of flow (True/False)answer=correctA petroleum crude oil having a density of 892 kg/m3 is flowing through the piping arrangement shown at a total rate of 1.388 x 10-3 m3/s entering pipe 1. The flow divides equally in each of pipes 3. The steel pipes are schedule 40 pipe. Calculate the following SI units.(a) The total mass flow rate in pipes 1 and 3. Ans. 1.238 kg/s, 0.619 kg/s(b) The average velocity in 1, 2 and 3. Ans. 0.641 m/s (pipe 1), 0.528 m/s (pipe 3)(c) The mass velocity G in 1. Ans. 572 kg/m-s2Pipe 1: 2-in pipe, D1 = 2.067 in Pipe 2: 3-in pipe, D2 = 3.068 in Pipe 3: 1 ½ - in pipe, D3=1.610 in

