Inflection Point Engineering Piping Design Guide

Pipe Sizing

Chapter from the Piping Design Guide.

PIPE SIZE SELECTION METHODOLOGY

Recommended Velocity Limits by Service

Service Min Velocity Max Velocity Economic Velocity Erosion Limit Notes Pipe Material
Liquid — general 3 ft/s 10 ft/s 5-7 ft/s 15 ft/s for CS Avoid low velocity (sedimentation) Carbon steel
Liquid — pump suction 1 ft/s 5 ft/s 2-4 ft/s N/A Low velocity critical for NPSH Carbon steel
Liquid — pump discharge 5 ft/s 15 ft/s 7-10 ft/s 15 ft/s Higher velocity OK downstream Carbon steel
Liquid — gravity drain 1 ft/s 3 ft/s 1.5-2 ft/s N/A Partial flow — size for self-venting Carbon steel
Steam — saturated 50 ft/s 100 ft/s 60-80 ft/s 150 ft/s ΔP drives sizing for long runs Carbon steel
Steam — superheated 80 ft/s 175 ft/s 100-150 ft/s 200 ft/s Higher velocity acceptable Alloy per temp
Gas / vapor — general 30 ft/s 80 ft/s 40-60 ft/s 100 ft/s Erosion limit with solids lower Carbon steel
Gas — compressor suction 30 ft/s 60 ft/s 40-50 ft/s N/A Minimize ΔP for compressor Carbon steel
Gas — compressor discharge 40 ft/s 100 ft/s 60-80 ft/s Erosion velocity Higher P allows higher velocity CS or alloy
Two-phase 15 ft/s 60 ft/s 20-40 ft/s Erosion calc req'd API RP 14E for erosional velocity Service-dependent
Flare header 0.2 Mach 0.5 Mach 0.3-0.4 Mach Mach 0.7 absolute max Sonic velocity = noise + vibration Carbon steel
Relief valve inlet N/A Mach 0.5 N/A N/A ΔP < 3% set pressure Carbon steel
Relief valve outlet N/A Mach 0.8 N/A N/A Reaction force consideration Carbon steel

Pressure Drop Guidelines

Service Max ΔP/100 ft Total System ΔP Limit Basis Notes
Process liquid (general) 0.5-2.0 psi Per system hydraulics Economics Balance pipe cost vs. pump energy
Pump suction 0.1-0.5 psi Keep NPSHA adequate NPSH Critical — minimize friction loss
Cooling water 0.5-1.5 psi Per pump head available System design Long runs may need larger pipe
Steam (100 psig) 0.5-1.0 psi 5-10% of supply P Economics Excessive ΔP = low delivery P
Process gas / vapor 0.1-0.5 psi Per compressor ΔP budget Compressor power Every psi of ΔP = more HP
Gravity drain Elevation-driven Must be self-draining Slope ≥ 1/8"/ft Partial full, ensure venting

Source: Piping_Design_Guide_v1.xlsx · sheet “Pipe Sizing”