fundamentals of engineering supplied-reference handbook - Ventech!
fundamentals of engineering supplied-reference handbook - Ventech!
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