Ideal Fluids in Motion • Ideal Fluid: Steady Flow, Incompressible Flow, Non viscous Flow, Irrotational Flow. • The Equation of Continuity: If a fluid is incompressible, its density ρ is constant throughout. Thus the volume of fluid entering a tube at one end per unit of time must be equal to the volume of fluid leaving the other end per unit time. In the time Δt we have A1v1Δt = A2v2Δt. ΔV = v2A2Δt ΔV = v1A1Δt A1v1 = A2v2 (continuity equation) RV = Av = volume flow rate = constant Rm = ρRV = ρAv = mass flow rate = constant • Bernoulli’s Equation: Application of W = ΔKE + ΔU: W = ( P1 A1 )Δx1 − ( P2 A2 )Δx2 = ( P1 − P2 )ΔV = ( P1 − P2 ) ( P1 − P2 ) M ρ = 12 M (v22 − v12 ) + Mg ( y2 − y1 ) F1 = P1A1 P1 + 12 ρv12 + ρgy1 = P2 + 12 ρv22 + ρgy2 R. Field 10/29/2013 University of Florida M M ρ M F2 = P2A2 Δx2 = v2Δt Δx1 = v1Δt PHY 2053 Page 1 Bernoulli’s Equation: Applications • Bernoulli’s Equation: P + ½ρv2 + ρgy = constant P1 + 12 ρv12 + ρgy1 = P2 + 12 ρv22 + ρgy2 (conservation of energy for a fluid) v1 >> v2 • Constant Height (y1 = y2): P + ½ρv2 = constant P1 + 12 ρv12 = P2 + 12 ρv22 P1 << P2 v1 P1 v2 P2 Air Foil If the speed of a fluid element increases as the element travels along a horizontal streamline, the pressure of the fluid must ΔP = P − P = 1 ρ (v 2 − v 2 ) 2 1 1 2 2 decrease, and conversely. • Example (velocity of efflux): Area A1 y-axis We can use Bernoulli’s equation to calculate the speed of efflux, v2, from a horizontal orifice (and area A2) located a depth h below the water level of a large talk (with area A1). P1 + ρv + ρgy1 = P2 + ρv + ρgy2 1 2 2 1 P1 = P2 = Patm v2 = 1 2 v1 = v2A2/A1 2 2 v1 (2) v = v + 2 gh = ( A2 / A1 ) v + 2 gh 2 2 h (1↔2) 2 1 2 2 gh ⎯⎯⎯→ 2 gh (Torricelli’s Law) (1 − ( A2 / A1 ) 2 ) A2 << A1 R. Field 10/29/2013 University of Florida (1) PHY 2053 2 2 ρ v2 y=0 Area A2 Page 2 Bernoulli’s Equation: Application • Venturi Meter: A Venturi meter is used to measure the flow of a fluid in a pipe. The meter is constructed between two sections of a pipe, the cross-sectional area A of the entrance and exit of the meter matches the pipe’s cross-sectional area. Between the entrance and exit, the fluid (with density ρ) flows from the pipe with speed V and then through a narrow “throat” of crosssectional area a with speed v. A manometer (with fluid of density ρM) connects the wider portion of the meter to the narrow portion. What is V in terms of ρ, ρM, h, a, and A? P1 + ρV = P2 + ρv 1 2 2 1 2 2 C VA = va (1↔2) v = VA / a ⎛ A2 ⎞ 2 2 gh V ⎜⎜ 2 − 1⎟⎟ = ( P1 − P2 ) = (ρM − ρ ) ρ ⎝a ⎠ ρ PC = P1 + ρg ( d + h) = P2 + ρgd + ρ M gh (C↔C) 2 P1 − P2 = ( ρ M − ρ ) gh R. Field 10/29/2013 University of Florida d PHY 2053 ⎛ρ ⎞ 2 gh⎜⎜ M − 1⎟⎟ ρ ⎝ ⎠ V= 2 A ⎛ ⎞ ⎜ ⎟ −1 ⎝a⎠ Page 3 Bernoulli’s Equation: Application • Siphon: The figure shows a siphon, which is a device for removing liquid from a container. Tube ABC must initially be filled, but once this is done, liquid will flow until the liquid surface of the container is level with the tube opening A. With what speed does the liquid emerge from the tube at C? What is the greatest possible height h1 that a siphon can lift water? Patm + ρV = PA + ρv − ρgd 1 2 2 2 1 2 VA = va (S↔A) V = va / A ⎛ a ⎞ 2 1 Patm = PA + 12 ρv 2 ⎜⎜1 − 2 ⎟⎟ − ρgd ⎯a⎯ ⎯ → P + ρ v − ρgd A 2 << A ⎝ A ⎠ 2 PA + 12 ρv 2 − ρgd = Patm + 12 ρv 2 − ρg (d + h2 ) 1 2 ρv 2 = ρg (d + h2 ) A = Area of container a = area of tube S y=0 V (A↔C) v PB + 12 ρv 2 + ρgh1 = Patm + 12 ρv 2 − ρg (d + h2 ) v = 2 g (d + h2 ) ( P − PB ) − (d + h2 ) h1 = atm ρg R. Field 10/29/2013 University of Florida PHY 2053 (h1 ) max (B↔A) P = atm − (d + h2 ) ρg v Page 4