DAP / NPK SimulatorSTOICHIOMETRY · RAW MATERIALS · GRANULATED PRODUCT
Stoichiometric model v1.2.0
DAP · GRANULATED FERTILIZER

DAP / NPK stoichiometric balance

Balance feasible
Granulated product output
31.25 t/h
247,500 tonnes / year
Resulting N–P₂O₅–K₂O
18.1 · 46.2 · 0.0
2.21% S · 1.5% moisture
Fresh raw materials
37.54 t/h
Includes additives · excludes process water
Mass closure residual
0.000000 kg/t
Fresh feed − product − vapour − losses

Raw-material consumption → granulated product

Editable wet-product targets. Fresh feed is shown separately from internal recycle.

Document-calibrated reference

Filler is calculated from the entered acid assay; no single reference filler value is available.

Fresh materialZero-loss kg/t¹Current as-fed kg/tPure / nutrient kg/t²Plant t/hPlant t/day
Phosphoric acid solution888.462901.769468.92028.180676.327
Ammonia feed221.182224.523223.4007.016168.392
Sulphuric acid solution56.22456.22455.1001.75742.168
Muriate of potash0.0000.0000.0000.0000.000
Urea0.0000.0000.0000.0000.000
Dry ammonium sulphate (pure equivalent)0.0000.0000.0000.000
Filler16.87717.0940.53412.821
Coating agent1.8001.8000.0561.350
Defoamer0.0150.0150.0000.011
Fresh RM 37.54 t/hGranulated product 31.25 t/h · 750.0 t/dayInternal recycle 140.63 t/h

¹ Same formulation with 100% net nutrient recovery, with filler recalculated. ² Acid = P₂O₅, ammonia = NH₃, sulphuric acid = H₂SO₄, potash = K₂O and urea = N. All denominators use actual coated product. Water, vapour and unrecovered material are in Balances.

Granulated product output

Equivalent composition at the specified finished moisture.

Output parameterCalculated result
Finished output31.250 t/h · 750.0 t/day · 247,500 t/year
N – P₂O₅ – K₂O18.100 – 46.200 – 0.000 wt%
Ammoniacal N / ureic N18.100 / 0.000 wt%
Sulphur2.210 wt% (minimum target 0.00%)
Finished moisture1.50 wt%
Coating included in product1.800 kg/t
Size-classification basis1–4 mm · ideal screen cuts from source
Granulation circuitRequired flow is available at the entered screen splits
Quality not predictedMeasured PSD, crushing strength, caking and phase composition

Feed characteristics

Changing an assay recalculates the as-fed quantities.

The retained-mass equivalent includes suspended and dissolved impurities as one lumped mass.

Stoichiometric reaction basis

Salt allocation conserves atoms; these neutralization equations generate no net reaction water.

H₃PO₄ + NH₃ → NH₄H₂PO₄NH₄H₂PO₄ + NH₃ → (NH₄)₂HPO₄H₂SO₄ + 2 NH₃ → (NH₄)₂SO₄

Potash and urea contribute their assayed nutrients. Filler closes the product mass budget. Free acid, excess NH₃, negative filler space and water shortage are reported as infeasible conditions.

Stoichiometric formulation · document-calibrated consumptionSteady-state model · assumptions remain traceable