Pressure variation with altitude in a static compressible fluid (e.g. air) with constant temperature gradient: ________________________________________________________________________ Basic equation: dp H H gdH (1) This equation cannot be integrated since variation of with height is not known. Assume air is ideal: pH RTH (2) dp H dH g pH RTH (3) TH T0 H (4) H From (1) & (2): In the troposphere: where = temperature lapse rate = 6.5 x 10-3 K/m = 6.5 K/km from (3) & (4): dp H g dH pH R T0 H (5) d T0 H dH dH pH p0 d T0 H dpH g H d T0 H g p ln pH pH ln T0 H 0 pH R 0 T0 H R H 0 g p H T0 H R p0 T0 g T H R T0 H H p RT p T0 H 0 H 0 0 RTH p 0 p 0 T0 H T0 T0 g 1 H T0 H R 0 T0 - 1- 1 Variation of pressure with altitude in a static compressible fluid (e.g. air) at constant temperature Lower stratosphere ( 11km H 20.1km ): TH 56.5o C const T * Note: air is still treated as ideal. dpH g g p H dH ln pH pH HH * * i i pH RT RT p H e pi g H Hi RT * Temperature lapse rate in the atmosphere under polytropic conditions Static fluid: dp gdz (1) Polytropic relationship: (n= polytropic index) p n const (2) Assume air is ideal: p RT (3) From (2): p const n dp const n n 1 d dp From (3): p n n n 1 d dp np d nRTd (4) dp R dT RTd (5) From (4) & (5): dp R dT d 1 n dp 1 R dT dp R dT n n 1 n From (1) & (6): - 2- (6) n dp gdz R dT n 1 dT n 1 g n R dz Note: (i) for adiabatic conditions: n = k; k: adiabatic index (k = Cp / Cv) (ii) n = 1 in the lower stratosphere dT 0 dz T const Variation of pressure with altitude in the atmosphere under polytropic conditions Basic pressure-height relationship: Assume air to be ideal: dp H H gdz (1) p H H RTH (2) Temperature variation with altitude: n 1 g TH T0 z n R (3) (1) divided by (2): dp H g dz pH RTH (4) with (3), (4) becomes dp H g dz pH R n 1 g T0 n R z pH p0 (5) dp H g Z dz pH R 0 n 1 g T0 n R z - 3- ln pH g n R Z p 0 R n 1 g 0 n 1 g n 1 g d T0 T0 z z n R n n R ln T0 n 1 g n 1 T0 n R z n n 1 g n 1 n T z 0 n 1 n R pH n 1 g 1 z p0 T0 n RT0 Note: the above is valid only in the troposphere. In the lower stratosphere, n = 1; the above will “blow up” Forces due to liquid pressure on plane submerged surfaces: FR : resultant force due to liquid pressure C: centriod of area z Atmospheric pressure Free surface of liquid O Liquid density = dA h h dF FR y edge view of plane y x dy C(x,y) y P(x’,y’) P: centre of pressure (i.e. point of application of FR) - 4- dA A A A A A Note: P is always below C unless the surface is horizontal in which case P = C Need: magnitude of FR direction of FR line of action of FR No shearing stresses in a static fluid; forces will be normal to surface independent of the orientation of the surface dF pdA (the negative on right-hand side of equation indicates that the direction of dF is opposite to dA ) Note: positive direction of dA is the outward drawn normal to the area Resultant force: FR A dF p dA A Pressure-height relationship in a static fluid: dp g dh (h is positive downward from the free surface) At the free surface i.e. at h = 0, p = patm also, = const (liquid) p patm z h dp g dh 0 h dF h=ysin p patm gh p patm g y sin FR p atm g y sin dA p atm dA g sin A A FR k A p atm dA k g sin FR patm dA g sin A A y dA k A y dA - 5- y d A A Recall A y dA : first moment of area of surface about the x-axis y dA y A A FR patm A g sin y A patm A gh A using gauge pressures: FR gh A pA (*) NOTE: (*) is based upon the assumption that pressure at the free surface of the liquid is atmospheric. More on this soon -- imaginary free surface = const means that (*) is valid only for a single homogeneous liquid Point of application of resultant force (centre of pressure) Resultant force is equivalent to the individual forces if the moment of the resultant about any axis is the same as the sum of the moments of the individual forces about the same axis r ' FR r dF r pdA A A r ' i x' j y ' ,r i x j y, dA dA k ,FR FR k i x' j y' F k i x j y pdAk R A k j FR x'i FR y' j x pdA i y pdA A A y' FR y pdA, x' FR x pdA A A j y-location of centre of pressure y' A y pdA FR y' A y p A atm g y sin dA patm g y sin A p atm y dA g sin y 2 dA A p atm A g y sin A p atm y A g sin I x p atm A g y sin A - 6- i NOTE: y 2 dA is the second moment of area about the x-axis Parallel-Axis Theorem: I x I x y 2 A dA y’ B’ B C y C: Centroid d A’ A Moment of inertia with respect to the AA’ axis 2 I y 2 dA, y y ' d , I y ' d dA A A I A y' 2 dA 2d y' dA moment of inertia with respect to centroidal axis A d2 dA A first moment of area with respect to BB’ = 0 since BB’ = I A y'dA y A and y 0 I I d2 A y' Ay p patm Ay g sin I x y 2 A patm A g sin yA y' y g atm g sin y A patm g sin y Ix h y A patm g sin y - 7- g sin I x A patm g sin y y' y p patm p Ix Ay where p patm gh using gauge pressures, y' y Similarly: x ' x Ix Ay p patm I xy p Ay Using gauge pressures, x ' x where I xy : product of inertia I xy Ay NOTE: 1) y and x are referred to the origin at the free surface 2) product of inertia may be positive or negative unlike Ix or Iy and Ixy = 0 when one or both axes are axes of symmetry Example An elliptical gate covers the end of a pipe 4m indiameter. If the gate is hinged at the top, what normal force, F, is required to open the gate when the water free surface is 8m above the top of the pipe and the pipe is open to atmosphere on the other side? Neglect the weight of the gate. water 8m Resultant hydrostatic force on gate z FR p A 5m Gauge pressures: Patm F FR gh A FR 1000 9.81 10 Hinge 4 5 1541 . MN 2 2 y m n n m - 8- 4m Location of centre of pressure along the y-axis b 3 1 a3b Ix a2 4 y' y 12.5 12.5 y A 12.5 a b 50 8 10 12 5 y ' 12.625 m Taking moments about the hinge M 0 H FR y H F 5 0 1541 . 12.625 10 F 5 0 F 1541 . 2.625 0.809 MN 5 APPROACH #1 Determination of the hydrostatic force on a curved submerged body Consider the following case: Fig. 3.6 (Fox & McDonald) Patm z dA dAx dAy y dAz x dF pdA - 9- a “Hydrostatic force acts, as in plane submerged surface, normal to surface. However, differentiation due to pressure on each element of the surface acts in a different direction because of the surface curvature” Differential force: dFR pdA Resultant force: FR pdA A FR i FRx j FRy k FRz FRx dFx FR i p dA i p dA cos x x p dAx A Similarly A A Ax FRy p dA cos y p dAy A Ay FRz p dA cos z p dAz A Az : angle between A and respective unit vectors A : angle between and respective unit vectors It is convenient to obtain the components of FR first and then FR can be expressed as the vector sum of the components Line of action of each component of FR r ' x i FRx r dFx i r ' y j FRy r dFy j r ' z k FRz r dFz k e.g. 2-D curved submerged surface - 10- z z dA FRz dAy FRy z’ y z’ dAz z’ y’ dA y dA j dA 1 cos 2 dAz dA k dA 1 cos 3 dA k dA1 cos 3 dAcos 3 dA j dA1 cos 2 dAcos 2 3 k 2 j dA dAcos =-dAcos2=dAy dAsin =dAcos3 =dAz ALTERNATIVE APPROACH dA=wds dAv=dAsin y p = y dF A dFy dy dFx dA ds x B dx dAh=dAcos y Enlarged view of dA - 11- Consider a 2-D curved surface AB as shown above. It is convenient to determine the horizontal and vertical components of the hydrostatic force and to obtain the resultant vectorially from the components. dF ywds dFx ywds sin ydAv -subscript v means projection of area to a vertical plane Fx ydAv ydAv y Av Note: ydA yA Fx p Av (magnitude of Fx) y' y Ix y Av w Fx dFy yw ds cos y dAh --subscript h means projection of area to a horizontal plane dFy dV Fy V - 12- x dAx dA y dAy Ah Ay Line of action n x'Fy Wi xi' i 1 Wi: contribution to the weight of liquid by part i y = axn y x’ Fx y’ x FR Fy y dF h b dA x a METHOD #1 dF p dA FR dF pdA A A - 13- Fy FR j p dA j pb dAy h=(b-y) j Fx b ydyw y 0 dAx Fx FR i pdAb i pdAx i x dAy ph Fy b y dx w b 0 Fy h dAy ; Fx h dAx Line of action y x’ x Fy dA x x' i Fy j xi dF j x' Fy k k x p dAy A A x' F y x b ywdx b 0 x' b 0 x b y wdx Fy y ' j Fx i y j dFx i - 14- Fy pbottom A b a w V n x' Fy Wi xi i 1 y h b Fy w x a a METHOD #2 Projection of surface onto plane made up of y & w results in a plane area; this area is acted upon by the x-component of the resultant force Fx p A Fx h A A bw w y’ y' y Ix yA b Fx - 15- h