| Stream | lb / day | tons / day | gal / day | Note |
|---|
A belt press squeezes water out of conditioned sludge between two porous belts. Sludge enters as a thin liquid, typically 2 to 5% solids, and leaves as a handleable cake at roughly 18 to 28% solids. The water that comes out, called filtrate, returns to the head of the plant.
A dry ton is the weight of the solid material only, ignoring the water it is suspended in. It is used because solids concentration varies day to day, but the actual mass of material you have to dewater is what drives polymer demand, press loading and cake production.
The 8.34 is the weight of one gallon of water in pounds.
Specifications quote GPM per press. Total plant flow is that figure multiplied by the number of presses running. Getting this backwards is the most common mistake when modelling a belt press system.
Cake solids sets how much material you actually haul away.
At 20% solids each dry ton becomes 5 wet tons. At 25% it becomes 4. At 30%, about 3.3. Two percentage points of cake dryness can move hauling cost more than any polymer saving.
Whatever solids do not report to the cake leave in the filtrate and return to the plant headworks, where they are captured again and sent back to dewatering. At steady state this multiplies the real solids load.
At 95% capture that is 1.05, so about 5% extra handling. At 85% it is 1.18 — nearly a fifth more work for the same incoming sludge.
Most municipal contracts set a minimum, commonly 2,000 lb of dry solids per hour per press. If you fall short, you are either running too many presses for the load or too many hours. Both are fixable operationally.
| Measure | Typical limit |
|---|---|
| Hydraulic loading | 25 – 40 GPM per metre of belt width |
| Solids loading | 400 – 1,200 lb/hr per metre of belt width |
Exceeding these causes washout — sludge squeezes out at the sides and capture drops sharply.
This is why comparing polymers on price per pound is misleading. A 45% active product at $0.95 costs more per dry ton than a 90% active product at $1.50, because you need more than twice the weight.
| Equipment | lb active / dry ton |
|---|---|
| Gravity belt thickener | 3 – 10 |
| Belt filter press | 4 – 12 |
| Centrifuge | 8 – 25 |
Bench jar tests set the starting dose. Full-scale presses apply different shear and residence time, so expect to re-optimise on the machine, usually within a couple of pounds per dry ton of the bench answer.