This paper outlines the core engineering principles for Module 3: Process Piping Hydraulics, Sizing, and Pressure Rating, covering the two independent design functions: fluid flow design (sizing) and pressure-integrity design (rating). 1. Fluid Flow Design & Hydraulic Sizing
Step 1 – Hydraulic Sizing
Try 6-inch Sch 40:
ID = 6.065 in = 0.5054 ft. Area = 0.2006 ft².
Velocity = (500 gpm * 0.002228 ft³/s/gpm) / 0.2006 = 5.55 ft/s (acceptable).
Re = (62.4 * 5.55 * 0.5054) / (1 * 0.000672) = ~260,000 (turbulent).
Friction factor f (from Moody, ε=0.00015 ft) ≈ 0.017.
Head loss hf = 0.017 * (500/0.5054) * (5.55²/(2*32.2)) = 8.1 ft.
ΔP = 8.1 ft * 0.433 psi/ft = 3.5 psi.
That’s well under 15 psi. Try 4-inch Sch 40:
ID = 4.026 in, v = 12.3 ft/s (high but possible).
hf ≈ 26 ft → ΔP = 11.3 psi (acceptable).
→ Select 4-inch Sch 40. This paper outlines the core engineering principles for
Total pressure drop = friction losses + static head + dynamic losses. Minimum girth weld efficiency and component ratings must
Tagline: Master the flow, fit, and force behind industrial piping systems. Step 1 – Hydraulic Sizing Try 6-inch Sch 40: ID = 6
Minor Losses: Pressure drops from valves and fittings are accounted for using the K-factor method or the Equivalent Length method.
The primary goal of this module is to ensure that a piping system can handle required flow rates while maintaining structural integrity under operational pressure. It focuses on two distinct but interdependent design functions: Fluid Flow Design (Sizing): Determining the minimum internal diameter ( cap I cap D