API 610 vs ANSI/ASME B73.1: Pump Standards Compared
A detailed comparison of API 610 and ANSI/ASME B73.1 reveals how each standard governs centrifugal pump design, testing, and documentation. Understanding their…
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Illustrative duty point — use the System Curve calculator for your data.
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Gateway calculation
Combine static elevation, pipe losses, vessel pressure, and velocity head in one defensible system requirement.
TDH = (hd − hs) + (hfd + hfs) + (Pd − Ps)·K / SG + Δhv
K is the pressure-to-head constant: 2.31 ft per psi (US) or 10.2 m per bar (SI), for water at SG = 1.
For preliminary sizing and educational use. Verify final design against manufacturer performance curves and applicable codes; final designs should be reviewed by a licensed professional engineer.
A defensible workflow
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A detailed comparison of API 610 and ANSI/ASME B73.1 reveals how each standard governs centrifugal pump design, testing, and documentation. Understanding their…
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