| Mistake | Consequence | Mitigation | |---------|------------|-------------| | Ignoring viscosity | Underestimates ΔP | Always check Re | | Using average velocity in gas lines | Large ΔP error | Compressible flow equations | | Neglecting temperature derating | Overpressure rupture | Use design temp. + 25°C margin | | Oversizing without economic check | High capital cost | Run ΔP vs. cost trade-off |
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