5. Estimate the friction pressure gradient in a 10.15 cm bore unheated horizontal pipe for the following conditions: Fluid-propylene Pressure 8.175 bar Temperature-7°C Mass flow of liquid-2.42 kg/s. Density of liquid-530 kg/m³ Mass flow of vapour-0.605 kg/s. Density of vapour-1.48 kg/m³
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- A saturated steam at 410K is being transported in a pipeline (brass drawing tubing) at a rate of 1 grams/second. Pipe has inside diameter of 0.025 m . The tube is 100m long. The pressure at the entrance is 80kPa. What is the % of pressure drop? (use Perry's Handbook for the properties and constants) R = 8314J/kgmol.K; MW=18.02g/molWhat is the friction loss in cm of water in a 2.44m diameter chimney 61m high up which gas is flowing at 9.14 m/sec? Gas density is 0.6776 kg/m3.EX in Asteel of speçific weight cy lin der (1"diametar andiz" Long) (8) =490 1b fI Ft3 fall be Cause of its own weight, at q uniform slig htly 9. rate of on5 HIs in side a tube of larger diameter.A Castor- oil film M = 6x lo -3 16 between t-s Constant thihness and the tube between of %3D is the cylinder Determine the cleamanCe (y) in ft the Cylinder and the tube-
- On a single plot, show curves that show the relationship between the pressure generated by thepump as a function of flow rate of water at 20 °C through the three branches of the piping systemshown below (delta P on the y axis and flow rate on the x axis; therange of the pressure should be 0 to ~1 MPa). Pipe inner diameter: 0.03 mPipe material: copperTypical mass flow rate of interest: 0.5 kg/sIgnore minor losses of tee's at points A and B and any features of branch 3Consider minor losses of two 90° elbows in branch 2A pressure drop of 500 kPa is measured over 200 m of a horizontal length of 8-cm- diameter cast iron pipe transporting water at 20–C, friction factor is 0.026 and kinematic viscosity of the water is 1.004*10-6 Fined: 1. The relative roughness. 2. The head loss. 3. The average velocity. 4. Reynolds number. 5. Volume flow rate.A pressure drop of 500 kPa is measured over 200 m of a horizontal length of 8-cm-diameter cast iron pipe transporting water at 20–C, friction factor is 0.026 and kinematic viscosity of the water is 10-6 Fined:1. The relative roughness.2. The head loss.3. The average velocity.4. Reynolds number.5. Volume flow rate.
- Discuss a case study of control volume analysis inside a piping system. A variation in flow direction should be considered in the analysis.1. Heated air at 1 atm and 35°C is to be transported in a 150-m-long circular plastic duct at a rate of 0.35 m³/s (Fig. 1). If the head loss in the pipe is not to exceed 20 m, using the Colebrook equation and consulting with the FE Reference Handbook and appropriate table(s) for equations and properties. Write a Matlab code to determine the i. ii. iii. iv. minimum diameter of the duct, the friction factor, average flow velocity and Reynolds number of the flow 0.35 m³/s air D -150 m Fig 1The thrust of a shaft is taken by a collar bearing provided with a forced rication system. The lubrication system maintains a film of oil of ilerm thickness between the surface of the collar and the bearing The aemal and intemal diameters of collar are 16 and 12 cms respectively. The thickness of oil film is 0.02 cms. and coefficient of viscosity is 0.91 poise. Find the horse-power lost in overcoming friction when the shaft is ntated at a speed of 350 r.p.m. Skult.
- In some high-rise buildings, water is stored in an elevatedtank on the roof to minimize pressure fluctuations inthe system. Consider water that is pumped through a 10-cmsteel pipe to the roof of a 200-m-tall building; the pump ison the ground floor. For a water temperature of lOOC and aflow of 0.02 m3/s, what is the pressure at the pump discharge(in kPa)?Pls do neatly nd correctlyQ2l Calculate size of each part for the air conditioning ducts system shown in Figure(1) by using equilibrium pressure drop method. The velocity of air in main duct 7 m/s. Tabulate the results (velocity value, rate of pressure drop, circular diameter, and air flow rate) for each part, then convert circular ducts to equivalent rectangle ducts at height 300 mm for all system. 0.5 m³/s E 5m A D 0.5m³/s 3m B Figure (1) 3m 3m 5m C 1 m³/s