Jar test both
Run a parallel jar test on your actual water. Record dose, settled turbidity, final pH and sludge volume for each.
Comparison
Alum is cheaper per tonne. PAC is usually cheaper per cubic metre treated. Here is where each one genuinely wins, including the cases where alum is still the right call.
| Parameter | Polyaluminium chloride (PAC) | Alum (aluminium sulphate) |
|---|---|---|
| Active Al2O3 | 28–30% solid, 10–12% liquid | Approx. 17% solid, 7–8% liquid |
| Typical dose | Roughly one third to one half of alum dose | Baseline reference |
| Effective pH range | Approx. 5.0–9.0 — wide | Approx. 6.5–7.5 — narrow |
| Alkalinity consumed | Low — often no supplement needed | High — usually needs lime or soda ash |
| pH depression | Mild, tunable via basicity | Pronounced |
| Cold water performance | Good | Poor — a known weakness |
| Floc characteristics | Dense, fast-settling, shear-resistant | Lighter, slower to settle |
| Sludge volume | Lower, dewaters better | Higher, wetter cake |
| Sulphate added to water | None | Significant — matters for RO feed and concrete exposure |
| Price per tonne | Higher | Lower |
| Cost per m³ treated | Usually lower | Usually higher once alkalinity and sludge are counted |
Alum wins on the invoice and loses on the plant. If PAC costs more per tonne but you dose a third to a half as much, the chemical cost per cubic metre is already close — before you count anything else.
Then add what alum brings with it. Alum consumes roughly two to three times more alkalinity, so many plants dose lime or soda ash purely to hold pH; that is a second chemical, a second dosing system, and a second line on the operating budget. Alum also produces more sludge, and that sludge holds more water, so you dewater and dispose of more of it.
There is also the sulphate question. Alum adds sulphate to the treated water. Where that water feeds reverse osmosis, or where the distribution network runs through concrete infrastructure, added sulphate is not neutral.
Where alum still wins: very high turbidity raw water where sheer bulk of coagulant is what is needed, plants with abundant natural alkalinity and no pH constraint, and sites with existing alum infrastructure where the switching cost outweighs the running saving. Those cases are real — just less common than the price-per-tonne comparison suggests.
Decision process
Run a parallel jar test on your actual water. Record dose, settled turbidity, final pH and sludge volume for each.
Include the lime or soda ash the alum option needs to hold pH. It is frequently the deciding number.
Compare settled sludge volume and, if you can, dewatered cake solids. Disposal is a real cost in the UAE.
If your raw water alkalinity is low or seasonal, alum's pH depression is a live operating risk.
Convert everything to cost per cubic metre treated. Price per tonne is not a decision input.
Run one tonne of PAC through the plant for a fortnight before committing to a supply agreement.
FAQ
For most water treatment applications in this region, yes — lower dose, wider pH range, much lower alkalinity consumption, denser floc and less sludge. Alum can still be more economical for very high turbidity water where alkalinity is abundant.
Typically one third to one half of the alum dose, depending on water chemistry. Confirm the ratio for your water with a parallel jar test rather than assuming a rule of thumb.
Usually yes. Dosing pumps, lines and tanks need to be PAC-compatible — HDPE, PVC, FRP or rubber-lined steel. Recalibrate pump stroke for the lower dose and re-optimise flash mix.
Per tonne, yes. Per cubic metre of water treated, usually less, once you account for the lower dose, reduced alkalinity chemical and lower sludge disposal cost.
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