Flow Parameters
Theoretical Formulas
Basic Flow Equations
Continuity Equation:
$$Q = A \cdot V = \frac{\pi D^2}{4} \cdot V$$
Where: $Q$ = flow rate, $A$ = cross-sectional area, $V$ = velocity, $D$ = pipe diameter
Reynolds Number:
$$Re = \frac{\rho V D}{\mu} = \frac{V D}{\nu}$$
Where: $\rho$ = density, $\mu$ = dynamic viscosity, $\nu$ = kinematic viscosity
- Laminar flow: $Re < 2300$
- Transitional flow: $2300 < Re < 4000$
- Turbulent flow: $Re > 4000$
Friction and Pressure Drop
Darcy-Weisbach Equation:
$$\Delta P = f \cdot \frac{L}{D} \cdot \frac{\rho V^2}{2}$$
Where: $f$ = friction factor, $L$ = pipe length, $\Delta P$ = pressure drop
Friction Factor for Smooth Pipes (Blasius):
$$f = \frac{0.3164}{Re^{0.25}} \quad \text{for } Re < 10^5$$
Friction Factor for Rough Pipes (Colebrook-White):
$$\frac{1}{\sqrt{f}} = -2 \log_{10}\left(\frac{\varepsilon/D}{3.7} + \frac{2.51}{Re\sqrt{f}}\right)$$
Where: $\varepsilon$ = surface roughness
Turbulence and Flow Characteristics
Turbulence Intensity:
$$I = \frac{u'}{U} = \frac{0.16}{Re^{1/8}}$$
Where: $u'$ = RMS of velocity fluctuations, $U$ = mean velocity
Head Loss:
$$h_L = f \cdot \frac{L}{D} \cdot \frac{V^2}{2g}$$
Where: $h_L$ = head loss, $g$ = gravitational acceleration
Engineering Guidelines
Velocity Limits
- Water: 8-12 ft/s (2.4-3.7 m/s)
- Oil: 4-8 ft/s (1.2-2.4 m/s)
- Steam: 100-200 ft/s (30-60 m/s)
- Air: 2000-4000 ft/s (600-1200 m/s)
Pipe Selection
- Schedule 40: General purpose, lower pressure
- Schedule 80: Higher pressure applications
- Copper: Potable water, HVAC systems
- PVC: Chemical resistance, lower temperature