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Fluid Mechanics.

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Presentation on theme: "Fluid Mechanics."β€” Presentation transcript:

1 Fluid Mechanics

2 Component Head Loss The Minor Loss Coefficient, K:-

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5 Combined Head Loss Equation
(Total head loss)=(Pipe head Loss)+(Component head loss) β„ŽπΏ= 𝑝𝑖𝑝𝑒𝑠 π‘“βˆ— 𝐿 𝐷 βˆ—( 𝑣 2 2βˆ—π‘” ) + π‘π‘œπ‘šπ‘π‘œπ‘›π‘’π‘›π‘‘π‘  πΎβˆ—( 𝑣 2 2βˆ—π‘” ) = 𝑣 2 2βˆ—π‘” βˆ— 𝑝𝑖𝑝𝑒𝑠 π‘“βˆ—( 𝐿 𝐷 ) + π‘π‘œπ‘šπ‘π‘œπ‘›π‘’π‘›π‘‘π‘  𝐾

6 Example If oil (Ξ½ = 4 Γ— 10-5 m2/s; S = 0.9) flows from the upper to the lower reservoir at a rate of m3/s in the 15 cm smooth pipe, what is the elevation of the oil surface in the upper reservoir?

7 Solution Minor head loss coefficients:- entrance = Ke = 0.5
bend = Kb = 0.19 outlet = KE = 1.0 𝐴𝑝= Ξ  4 βˆ— 𝑑𝑝 2 = βˆ— = π‘š 2 𝑣= 𝑄 𝐴𝑝 = =1.58π‘š/𝑠 𝑅𝑒= π‘‰βˆ—π· 𝑣 = 1.58βˆ—0.15 4βˆ— 10 βˆ’5 =5925

8 The flow is turbulent Assume e=0 𝑓= ( log 10 ( 𝑒 3.7βˆ—π· 𝑅𝑒 0.9 ) ) 2 = 0.25 ( log 10 ( 0 +( )))^2 =0.036 Head Loss:- β„ŽπΏ= 𝑣 2 2βˆ—π‘” βˆ— 𝑝𝑖𝑝𝑒𝑠 π‘“βˆ—( 𝐿 𝐷 ) + π‘π‘œπ‘šπ‘π‘œπ‘›π‘’π‘›π‘‘π‘  𝐾

9 β„ŽπΏ= βˆ—9.80 βˆ— 0.036βˆ— βˆ— β„ŽπΏ=6.255π‘š 𝑃1 Ι£ +𝑧1+ 𝑣1 2 2βˆ—π‘” +β„Žπ‘= 𝑃2 Ι£ +𝑧2+ 𝑣2 2 2βˆ—π‘” +β„Žπ‘‘+β„ŽπΏ Where Hp=ht=0 V1=v2=0 P1=P2=Patm=0 𝑧1=𝑧2+β„ŽπΏ= =136.25π‘š

10 Non-Round Conduits If the conduit is not a pipe it is a square, triangle or any other shapes we replace the diameter by the hydraulic diameter. π·β„Ž= 4βˆ—πΆπ‘Ÿπ‘œπ‘ π‘  π΄π‘Ÿπ‘’π‘Ž π‘Šπ‘’π‘‘π‘‘π‘’π‘‘ π‘π‘’π‘Ÿπ‘–π‘šπ‘’π‘‘π‘’π‘Ÿ For Example and rectangular tube with L(Length) and W(wide) the hydraulic diameter will be:- π·β„Ž= 4βˆ—πΏβˆ—π‘Š 2(𝐿+π‘Š) = 2βˆ—πΏβˆ—π‘Š (𝐿+𝑀)

11 Example Air (T = 20Β°C and p = 101 kPa absolute) flows at a rate of 2.5 m3/s in a horizontal, commercial steel, HVAC duct. (Note that HVAC is an acronym for heating, ventilating, and air conditioning.) What is the pressure drop in inches of water per 50 m of duct?

12 Solution 𝐴=πΏβˆ—π‘Š=0.6βˆ—0.3=0.18 π‘š 2 𝑣= 𝑄 𝐴 = 2.5 0.18 = 13.89π‘š 𝑠
π·β„Ž= 4βˆ—πΏβˆ—π‘Š 2βˆ—(𝐿+π‘Š) = 4βˆ—0.6βˆ—0.3 2βˆ—( ) =0.4π‘š 𝑅𝑒= π‘‰βˆ—π·β„Ž 𝑣 = 13.89βˆ— βˆ— 10 βˆ’6 =368000 The flow is turbulent 𝑒= π‘š

13 𝑓= ( log 10 ( 𝑒 3.7βˆ—π·β„Ž 𝑅𝑒 0.9 ) ) 2 = 0.25 ( log 10 ( ( βˆ—0.4 )+( )))^2 =0.015 β„ŽπΏ=π‘“βˆ— 𝐿 π·β„Ž βˆ— 𝑣 2 2βˆ—π‘” = βˆ— βˆ—9.81 =18.6π‘š

14 π‘ƒπ‘™π‘œπ‘ π‘ =Οβˆ—π‘”βˆ—β„ŽπΏ=1.2βˆ—9.814βˆ—18.6=220π‘ƒπ‘Ž 1000βˆ—9.81βˆ—β„Žπ‘€=220 β„Žπ‘€=0.0224π‘š=2.24π‘π‘š=0.883π‘–π‘›π‘β„Ž

15 Pumps a centrifugal pump is a machine that uses a rotating set of blades situated within a housing to add energy to a flowing fluid.

16 Pump Curve

17 Example A pump is to be used to transfer crude oil (! = 2 Γ— 10!4 lbf-s/ft2, 1 = 0*86) from the lower tank to the upper tank at a flow rate of 100 gpm. The loss coefficient for the check valve is 5.0. The loss coefficients for the elbow and the inlet are 0.9 and 0.5, respectively. The 2-in. pipe is made from commercial steel (e = 0*002in.) and is 40 ft long. The elevation distance between the liquid surfaces in the tanks is 10 ft. The pump efficiency is 80%. Find the power required to operate the pump.

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19 Solution

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22 Pipes in Parallel The Losses is equal in both branches as the energy different in point (1) and point (2) is equal according to Energy equation.

23 β„ŽπΏ1=β„ŽπΏ2 𝑓1βˆ— 𝐿1 𝐷1 βˆ— 𝑣1 2 2βˆ—π‘” =𝑓2βˆ— 𝐿2 𝐷2 βˆ— 𝑣 βˆ—π‘” ( 𝑉1 𝑉2 ) 2 = 𝑓2βˆ—πΏ2βˆ—π·1 𝑓1βˆ—πΏ1βˆ—π·2 𝑉1 𝑉2 = ( 𝑓2βˆ—πΏ2βˆ—π·1 𝑓1βˆ—πΏ1βˆ—π·2 ) 1/2

24 Example A piping system consists of parallel pipes as shown in the following diagram. One pipe has an internal diameter of 0.5 m and is 1000 m long. The other pipe has an internal diameter of 1 m and is 1500 m long. Both pipes are made of cast iron (e = 0.26 mm). The pipes are transporting water at 20C (ρ= 1000 kg/m3, v= 10^-6 m2/s). The total flow rate is 4 m3/s. Find the flow rate in each pipe and the pressure drop in the system. There is no elevation change. Neglect minor losses.

25 Solution

26 Take 𝑓1=0.017 π‘Žπ‘›π‘‘ 𝑓2=0.0145 π‘Žπ‘  π‘–π‘›π‘–π‘‘π‘Žπ‘™ 𝑔𝑒𝑒𝑠𝑠

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