Sahawatthanakit (1988) Co., Ltd.
SAHAWATTHANAKIT(1988) · Make It Smart
Free tool

Sacrificial anode sizing calculator

Enter the steel surface area to protect, the design life and the environment → get the current demand, the total anode mass and the number of anodes, calculated to DNV-RP-B401 and ISO 12696 — enough to set a budget and ask for a quotation.

Site data

e.g. hull below the waterline · the immersed face of piles · buried pipe surface (the metal area in contact with water or soil)

The sounder the coating, the fewer anodes you need (coating breakdown factor fc = 0.35)

Only the metals suited to the selected environment are offered · DNV-RP-B401 · TIS 3359-2565

Preliminary result

Anodes required
51 anodes
at 10 kg each = 510 kg installed
Net anode mass required
503 kg
M = I·t·8760 / (u·ε)
Current demand (mean)
6.13 A
initial 13.13 · final 8.75 A
Which condition governs
Mass: 51End-of-life current: 18
Both conditions must be met, so the larger count wins — here mass governs (there is enough current, but enough metal must remain to corrode away over the whole life)
Acceptance criterion
−850 mV vs Cu/CuSO₄ (−800 mV in anaerobic soil) per NACE SP0169 / ISO 15589
Standards: DNV-RP-B401 · TIS 3359-2565

Preliminary estimate for budgeting and enquiry only — computed from the standard formulas (DNV-RP-B401 / ISO 12696 / NACE SP0169) using mid-range current densities and coating breakdown factors. Actual figures depend on a site survey, water temperature and velocity, soil resistivity, the geometry and resistance of the selected anode model, and electrical continuity. Corrosion protection of hulls, piers, bridges, and load-bearing structures affects safety and service life — a design engineer must review and certify the system before purchase and installation.