HW_6_solutions - n i t t P3.9 A laboratory test tank...

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Unformatted text preview: - ., n . i t t _, P3.9 A laboratory test tank contains seawater of salinity S and density ,0. Water enters the tank at conditions (S 1, ,01, A1, V1) and is assumed to mix immediately in the tank. Tank water leaves through an outlet A2 at velocity V2. If salt is a “conservative” property (neither created nor destroyed), use the Reynolds transport theorem to find an expression for the rate of change of salt mass Msalt Within the tank. Solution: By definition, salinity S = psalt/p. Since salt is a “conservative” substance (not consumed or created in this problem), the appropriate control volume relation is dMsal d . . dt tlsystem: p5 + 81112 — Slml = 0 dMs dt P3.13 The cylindrical container in Fig. P3. 13 1s 20 cm in diameter and has a conical contraction at the bottom with an exit hole 3 cm in diameter. The tank contains fresh water at standard sea-level conditions. If the water surface is falling at the Mt) nearly steady rate dh/dt z —0.072 m/s, estimate the average ve1001ty V from the bottom exit. _______________________ __ Fig. P 3. l 3 IV? Solution: We could simply note that dh/dz‘ is the same as the water velocity at the surface and use Q1 = Q2, or, more instructive, approach it as a control volume problem. Let the control volume encompass the entire container. Then the mass relation is dm d d 7: 7r 7W. = 0 = 91 deu) + = EwflwlDzh) |+ pzDthV, CV ' 72' 2 072 72' 2 72' D 2 6172 or p—D — + p—D ~V= 0 Cancel —: V = —— 4 dt 4 ex” ’0 4 (Dem) ( dt) Introduce the data: V = (206m)2[—(~0.072fl)] = 3.23 Ans. 3cm 5 s a, 9 , , e , P3.14 The open tank in the figure (3) * 3 contains water at 20°C. For i QrOOlm /S incompressible flow, (a) derive an +0) (2) analytic expression for dh/dz‘ in terms of h + (Q1, Q2, Q3). (b) If h is constant, D1=50m D2:7cm determine V2 for the given data if V1 = 3 m/s and Q3 = 0.01 m3/s. Solution: For a control volume enclosing the tank, d _ £01111: _ _ E[C_I[pd0]+P(Q2_Q1_Q3)—P 4 dt+p(Q2 Q1 Q3), solve E=M Answa) dt (ml/4) If h is constant, then Q2 = Q1+ Q3 2 0.01 +%(0.05)2 (3.0) = 0.0159 = €(007)2 V2, solve V2 = 4.13 m/s Ans. (b) P3.26 A thin layer of liquid, draining from an inclined plane, as in the figure, will have a laminar velocity profile u = Uo(2y/h — yZ/hz), where U0 is the surface velocity. If the plane has Width [3 into the paper, (a) deter—mine the volume rate of flow of the film. (b) Suppose that h = 0.5 in and the flow rate per foot of channel width is 1.25 gal/min. Estimate Uo in ft/s. Solution: (a) The total volume flow is computed by integration over the flow area: h 2 Q= IVndA= ]U,[2—y—y—]bdy=§Uobh Ans. (a) (b) Evaluate the above expression for the given data: 3 2 2 0.5 Q=1.25 2520002785 L=_Uobh=—Uo(i.0fi) —ft , mm s 3 3 12 ft solve for U0 2 0.10 — Ans. (b) \ S (/54, é , é/0%/// P3.36 The jet pump in Fig. P336 injects water at U1 2 40 m/s through a 3-in pipe and entrains a secondary flow of water U2 = 3 m/s in the annular region around the small pipe. The two flows become fully mixed down-stream, Where U3 is approximately constant. For steady incompressible flow, compute U3 in m/s. Solution: First modify the units: D1 = 3 in = 0.0762 m, D2 = 10 in = 0.254 m. For incompressible flow, the volume flows at inlet and exit must match: Q1+ Q2 = Q3, or: §(0.0762)2(40)+§[(0.254)2 —(0.0762)2](3) = §(0.254)2U3 Solve for Ans. U3 z 6.33 m/s P3.40 The water jet in Fig. P3.40 strikes normal to a fixed plate. Neglect gravity and friction, and compute the force F in newtons required to hold the plate fixed. Solution: For a CV enclosing the plate and the impinging jet, we obtain: ZFX : "F = mupuup + l’l’ldownudown — = ’mjur mi = ijVj Thus F = ijvj2 = (998)7r(0.05)2(8)2 z 500 N (- Ans. P3.41 In Fig. P3.41 the vane turns the water jet completely around. Find the maximum jet velocity V0 for a force Fo. Solution: For a CV enclosing the vane and the inlet and outlet jets, Fig. P3.41 2 Fx : #Fo : Iilloutuout _ 1hinuin : mjet (—VO) — mist (+V0) F0 Ans. Or: ——-—2‘ mot/4m. F0 = 2pOA V2 0 O, solve for V0: ...
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This note was uploaded on 02/02/2012 for the course CIEG 305 taught by Professor Schwartz,l during the Fall '08 term at University of Delaware.

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HW_6_solutions - n i t t P3.9 A laboratory test tank...

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