The value, in detail
$11.3M a year, and where each dollar comes from
The same $11.3M two ways: by cause, and by the kind of cost it removes. Every priced line belongs to exactly one category, so no dollar is counted twice.
By cause
Phosphoric acid filter line B is sending phosphate to the …$5.1M
Cooling tower A drains about 2.6× the water it needs to$2.5M
Sulfuric acid train C is burning extra power and losing st…$2.1M
The demineralised water plant is wasting more of its feed$1.6M
Cooling tower B's fans are working much harder for the sam…$46k
By kind of cost
| Cost removed | Annual change | Of what the plant uses | $ / yr | Comes from |
|---|
| Water consumption | 2,964,888 m³ | 13% of 22,599,365 m³ | $2,816,644 | Cooling tower A, The demineralised water plant |
| Wastewater sent to treatment | 2,964,888 m³ | — | $1,185,955 | Cooling tower A, The demineralised water plant |
| Treatment chemicals | 29,016 kg | 10% of 278,704 kg | $86,866 | Cooling tower A |
| Electrical energy | 10,207 MWh | 3% of 375,140 MWh | $489,943 | The demineralised water plant, Cooling tower B's fans are working much harder for the same cooling, Sulfuric acid train C |
| Steam recovered | 119,881 t | — | $1,678,337 | Sulfuric acid train C |
| Production and yield | 6,181 t phosphate | 0.3% of 1,868,623 t phosphate | $5,068,700 | Phosphoric acid filter line B |
| Overall annual saving | | | $11,326,446 | |
"Of what the plant uses" compares each saving with the quantity measured in this record, scaled to a year of 8,059 operating hours. Electrical energy is set against the metered load in the data, not the whole site.
The water balance still closes
A saving that does not respect conservation of water is not a saving. For the largest water cause, evaporation is fixed by the heat the tower has to reject, so only the drained water, and the fresh water that replaces it, can change.
| Tower A, per hour | Today | At the twin's reuse | Change |
|---|
| Evaporation, set by the heat the tower must reject | 813 m³/h | 813 m³/h | unchanged |
| Drift loss from the tower | 9.2 m³/h | 9.2 m³/h | unchanged |
| Water drained to keep salts down | 369 m³/h | 144 m³/h | −225 m³/h |
| Fresh water drawn | 1,192 m³/h | 967 m³/h | −225 m³/h |
| Times the water is reused | 3.1× | 6.3× | matches its twin |
| Check: fresh water = evaporation + drift + drain | 1,192 m³/h | 967 m³/h | the balance closes |
How confident to be
78% of the total rests on quantities read directly from the plant's instruments, such as concentrations, flows and power. The rest uses a physical assumption, such as the tower's drift loss. Prices are the plant's own unit costs; the table shows how far the total moves if each is wrong by the range tested.
| Price | Used | Range tested | Total moves by |
|---|
| Phosphate price | $820/t | $615–1025 | −$1.3M to +$1.3M |
| Water price | $0.95/m³ | $0.57–1.33 | −$1.2M to +$1.2M |
| Steam and fuel value | $14/t | $8–20 | −$671k to +$671k |
| Effluent treatment cost | $0.4/m³ | $0.20–0.60 | −$593k to +$593k |
| Electricity price | $0.048/kWh | $0.034–0.062 | −$147k to +$147k |
The biggest single uncertainty is the phosphate price. It drives 45% of the total. The quantities are measured either way; only their price is in question, and one invoice settles it.
What is not counted
The headline excludes the unconfirmed lead (up to $344,821/yr), any benefit from the instrumentation below, avoided failures, operator time and the effect of cleaner operation on downstream production. All are real; none is claimed.