Piping Design Guide
Chapter from the Piping Design Guide.
| 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 |
| 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”
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