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fundamentals of engineering supplied-reference handbook - Ventech!

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The Field Equation is derived when the energy equation is<br />

applied to one-dimensional flows.<br />

Assuming no friction losses and that no pump or turbine<br />

exists between sections 1 and 2 in the system,<br />

p<br />

γ<br />

2<br />

2<br />

2<br />

V<br />

+ + z<br />

2g<br />

2<br />

2<br />

1<br />

p1<br />

V<br />

= + + z1<br />

, where<br />

γ 2g<br />

p1, p2 = pressure at sections 1 and 2,<br />

V1, V2 = average velocity <strong>of</strong> the fluid at the sections,<br />

z1, z2 = the vertical distance from a datum to the sections<br />

(the potential energy),<br />

γ = the specific weight <strong>of</strong> the fluid (ρg), and<br />

g = the acceleration <strong>of</strong> gravity.<br />

FLUID FLOW<br />

The velocity distribution for laminar flow in circular tubes<br />

or between planes is<br />

⎡ 2<br />

⎛ r ⎞ ⎤<br />

v = vmax<br />

⎢1<br />

− ⎜ ⎟ ⎥ , where<br />

⎢⎣<br />

⎝ R ⎠ ⎥⎦<br />

r = the distance (m) from the centerline,<br />

R = the radius (m) <strong>of</strong> the tube or half the distance<br />

between the parallel planes,<br />

v = the local velocity (m/s) at r, and<br />

vmax = the velocity (m/s) at the centerline <strong>of</strong> the duct.<br />

vmax = 1.18V, for fully turbulent flow<br />

(Re > 10,000)<br />

vmax = 2V, for circular tubes in laminar flow and<br />

vmax = 1.5V, for parallel planes in laminar flow, where<br />

V = the average velocity (m/s) in the duct.<br />

The shear stress distribution is<br />

τ<br />

τ<br />

w<br />

=<br />

r<br />

R<br />

, where<br />

τ and τw are the shear stresses at radii r and R respectively.<br />

46<br />

FLUID MECHANICS (continued)<br />

The drag force FD on objects immersed in a large body <strong>of</strong><br />

flowing fluid or objects moving through a stagnant fluid is<br />

2 A<br />

CDρV<br />

FD<br />

= , where<br />

2<br />

CD = the drag coefficient (see page 55),<br />

V = the velocity (m/s) <strong>of</strong> the undisturbed fluid, and<br />

A = the projected area (m 2 ) <strong>of</strong> blunt objects such as<br />

spheres, ellipsoids, disks, and plates, cylinders,<br />

ellipses, and air foils with axes perpendicular to the<br />

flow.<br />

For flat plates placed parallel with the flow<br />

CD = 1.33/Re 0.5 (10 4 < Re < 5 × 10 5 )<br />

CD = 0.031/Re 1/7 (10 6 < Re < 10 9 )<br />

The characteristic length in the Reynolds Number (Re) is<br />

the length <strong>of</strong> the plate parallel with the flow. For blunt<br />

objects, the characteristic length is the largest linear<br />

dimension (diameter <strong>of</strong> cylinder, sphere, disk, etc.) which is<br />

perpendicular to the flow.<br />

AERODYNAMICS<br />

Airfoil Theory<br />

The lift force on an airfoil is given by<br />

2<br />

CLρV AP<br />

FL<br />

=<br />

2<br />

CL = the lift coefficient<br />

V = velocity (m/s) <strong>of</strong> the undisturbed fluid and<br />

AP = the projected area <strong>of</strong> the airfoil as seen from above<br />

(plan area). This same area is used in defining the drag<br />

coefficient for an airfoil.<br />

The lift coefficient can be approximated by the equation<br />

CL = 2πk1sin( α+β ) which is valid for small values <strong>of</strong><br />

α and β .<br />

k1 = a constant <strong>of</strong> proportionality<br />

α = angle <strong>of</strong> attack (angle between chord <strong>of</strong> airfoil and<br />

direction <strong>of</strong> flow)<br />

β = negative <strong>of</strong> angle <strong>of</strong> attack for zero lift.<br />

The drag coefficient may be approximated by<br />

2<br />

L<br />

C<br />

CD = CD∞+<br />

πAR<br />

CD∞ = infinite span drag coefficient<br />

2<br />

b Ap<br />

AR = =<br />

A 2<br />

c<br />

p

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