Bath Make-up — Dilution (C₁V₁ = C₂V₂)
Convert concentrate to working solution.
If V₁=0, we compute V₁ = (C₂·V₂)/C₁ and water = V₂ − V₁.
Normality / Molarity Helpers
Quick prep for titrants and indicators.
FA / TA Titration & Ratio
For phosphating and conversion-coating bath control.
ppm ⇄ g/L ⇄ % w/v Converter
For accelerators (nitrite/nitrate/chlorate), metals, etc.
Replenishment Dosage
Add concentrate to restore target concentration after drop.
Addition (L) = ( (Ctgt − Ccurr) × Vbath ) / Cconc
Drag-out Loss Estimator
Estimate chemical loss via carry-over.
Approx: Volume dragged (L/h) ≈ Area × (thickness µm × 10⁻⁶ m) → m³/h → L/h; mass of active ≈ volume × (conc g/L).
Coating Weight (g/m²)
Weigh-strip-reweigh method.
Salt-Spray Quick Log
Record hours to first rust (Rf), creep at scribe, blistering notes.
Costing — Bath & per m²
Estimate chemical cost to prepare bath and treat area.
Cost/bath (₹) = (V × C / 1000) × Price; g/L→kg: ÷1000.
Sludge Factor Estimate
Rough sludge yield from coating formation & impurities.
Notes & Assumptions
- FA/TA factor “49” is common for phosphoric acid equivalence; confirm your method factors.
- Drag-out model is approximate; validate with plant measurements (weir, rinse analysis).
- Sludge % varies with steel grade, throughput, phosphate type, & filtration efficiency.
- Always corroborate calculator outputs with lab titration and on-line QA checks.