Belt Filter Press — Dewatering Model

Plant: — Scenario: — Generated: — Sprategy — Field Operations
SPRATEGY

Belt Filter Press Calculator

Sludge dewatering — mass balance, loading and cost
Dry solids
dry tons / day
Polymer
lb product / day
Cake produced
wet tons / day
Throughput / press
lb dry / hr
Cost per dry ton
polymer only
Parameters — open a section to adjust, close it when you're done
1

Sludge feed

Start here. Everything downstream is driven by how much dry solid material arrives each day.
  • The feed rate is per press. Total plant flow is that figure multiplied by the number of presses running.
  • Presses do not run 24 hours — the operating hours set how long that flow actually happens.
  • Solids concentration matters enormously. The same flow at 2% versus 4% solids is half the dry tonnage.
20GPM per press220
Typical municipal spec range is 80 to 140 GPM per press. This is not total plant flow.
1presses12
How many are running simultaneously, not how many you own.
4hours24
Sludge accumulates around the clock, but dewatering is a scheduled operation.
0.5%% by weight8%
Thickened sludge to a belt press is typically 2 to 5%.
1.00sg1.10
Municipal sludge is close to water, 1.00 to 1.05.
Show the math — how feed becomes dry tons
2

Press performance

What the press achieves. Cake solids and capture rate are the two results a belt press is judged on.
  • Cake solids is how dry the output is. Higher means less material to haul away.
  • Capture rate is the fraction of solids that end up in the cake. Whatever escapes returns to the plant headworks in the filtrate and gets processed again.
10%% solids in cake40%
Belt presses typically reach 18 to 28%. Contract minimums are often 20%.
70%% captured99.5%
Solids lost here recirculate and add load back onto the plant.
0.5mmetres3.5m
Common sizes are 1.0, 1.5, 2.0 and 2.5 metres.
Show the math — cake and filtrate
3

Polymer and cost

Cost per dry ton is the number that matters, not price per pound. A product at half the price but half the active content needs twice the weight, so it costs the same or more. Set the dose from a jar test where you can.
1lb active / dry ton25
Belt press range is usually 4 to 12 lb active per dry ton.
10%% active100%
Dry polymer 85 to 95%. Emulsion 25 to 50%. Solution 5 to 15%.
$0.25$ per lb$6.00
Delivered cost of the commercial product, not the active fraction.
200days365
Show the math — polymer demand and cost
4

Report details

optional — appears on the printout
Process flow
Sludge in
Dry solids
dry tons / day
+ polymer
Belt press
presses running
Cake out
filtrate
To headworks
gal / day
Daily output
Dry solids processed
dry tons / day
Polymer consumed
lb product / day
Dewatered cake
wet tons / day
Water removed
gal / day filtrate
Performance checks
Throughput per press
lb dry solids / hr / press
Common contract minimum: 2,000 lb/hr
Cake solids
% solids in dewatered cake
Typical target: 20% or better
Solids capture
% of solids ending in cake
Typical target: 95% or better
Daily mass balance
Streamlb / daytons / daygal / dayNote
Annual summary
Dry tons per year
dry tons
Polymer per year
lb product
Annual polymer cost
USD per year
Cake hauled per year
wet tons
disposal volume
These are engineering estimates. Confirm measured sludge density, actual operating hours, polymer dose from a jar test, and equipment capacity before using these figures for purchasing, bidding or design.

Belt press guide

What a belt filter press does

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.

Dry tons — the unit everything runs on

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.

dry lb/day = flow (GPM) × hours × 60 × 8.34 × specific gravity × solids% dry tons/day = dry lb/day ÷ 2000

The 8.34 is the weight of one gallon of water in pounds.

Feed rate is per press, not total

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.

total flow = GPM per press × presses running

Why cake solids matters so much

Cake solids sets how much material you actually haul away.

wet cake (tons/day) = dry tons captured ÷ (cake solids% ÷ 100)

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.

Capture rate and recycle

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.

recycle multiplier ≈ 1 ÷ capture rate

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.

Throughput per press

lb dry / hr / press = dry lb/day × capture ÷ (hours × presses)

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.

Hydraulic and solids loading

MeasureTypical limit
Hydraulic loading25 – 40 GPM per metre of belt width
Solids loading400 – 1,200 lb/hr per metre of belt width

Exceeding these causes washout — sludge squeezes out at the sides and capture drops sharply.

Polymer: active content versus price

lb product per dry ton = active dose ÷ (active% ÷ 100) cost per dry ton = lb product per dry ton × $ per lb

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.

Typical polymer doses

Equipmentlb active / dry ton
Gravity belt thickener3 – 10
Belt filter press4 – 12
Centrifuge8 – 25

Common troubleshooting

Relationship to the jar test

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.