Hydraulics
Transkript
Hydraulics
Hydraulics 25.02.2011 Exercise - 1 Q1. Water at 10°C flows in a 150 mm diameter pipe at a velocity of 5.5 m/sec. Is this flow laminar or turbulent? Re>4000 turbulent Re<4000 laminar 25.02.2011 Re IKU - Hydraulics - Murat Aksel V .D 2 Exercise - 1 25.02.2011 IKU - Hydraulics - Murat Aksel 3 Exercise - 1 Re V .D water(10C ) 1.307 x10 6 5.5 x0.15 Re 634000 6 1.307 x10 Re 634000 4000 Flow is turbulent! 25.02.2011 IKU - Hydraulics - Murat Aksel 4 Model-Velocity-Laminar Flow 25.02.2011 IKU - Hydraulics - Murat Aksel 5 Model-Velocity-Turbulent Flow 25.02.2011 IKU - Hydraulics - Murat Aksel 6 Model-Velocity 25.02.2011 IKU - Hydraulics - Murat Aksel 7 Model-Pressure 25.02.2011 IKU - Hydraulics - Murat Aksel 8 Exercise - 2 Gasoline is being discharged from a pipe, as shown in figure. The pipe roughness (ɛ) is 0.500 mm, and the pressure at point 1 is 2500 kPa. Find the pipe diameter needed to discharge gasoline at a rate of 0.10 m³/s. Neglect any minor losses. (SGgasoline = 719 kg/m³, μgasoline = 2.92x10¯⁴) 25.02.2011 IKU - Hydraulics - Murat Aksel 9 Exercise - 2 V12 P2 V22 z1 z2 hL 2g 2g P1 L V2 hL f D 2g Bernoulli Eq. Darcy-Weisbach Head Loss Eq. 965.5 V 2 V22 hL f 49.2 f D 2 x9.81 D 2500 V12 V22 V22 82.65 0 66.66 49.2 f 7060 19.62 19.62 D Q V .A Q V1. A1 V2 . A2 A1 A2 V1 V2 V22 f 0.332 D 25.02.2011 IKU - Hydraulics - Murat Aksel 10 Exercise - 2 V22 f 0.332 D V2 Q 0.1 2 0 . 1273 / D A2 D 2 / 4 0.1273 / D f 2 2 0.332 D D (0.04881 f )1/ 5 Assume f = 0.02 f 0.02 D 0.04881x0.02 1/ 5 0.25m V2 0.1273 / 0.252 2.037 m / s Re DV 719 x0.25 x 2.037 6 1 . 25 x 10 2.92 x104 25.02.2011 IKU - Hydraulics - Murat Aksel 11 Exercise - 2 0.0005m / D 0.0005 / 0.25 0.002 From Moody Diagram f = 0.0235 f 0.0235 D 0.04881x0.0235 1/ 5 0.2582m V2 0.1273 / 0.2582 2 1.91m / s 25.02.2011 IKU - Hydraulics - Murat Aksel 12 25.02.2011 IKU - Hydraulics - Murat Aksel 13
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