Skip to content

Slurry Dewatering Thickener and Filter Press Selection

Published: · Updated:
Slurry Dewatering Thickener and Filter Press Selection Guide

In a washing plant the water itself is not the problem; the problem is the fine material it carries. The slurry dewatering thickener and filter press selection discussion is usually set up on site as a contest between three options: settling pond, thickener and filter press. It is not a contest. The three perform different duties inside the same circuit, and what decides which of them is required is not machine capability but the constraints of the site.

How slurry dewatering thickener and filter press selection is framed

To compare them properly, separate what each one produces. A thickener settles solids by gravity, usually with flocculant assistance; its duty is to clarify a large volume of water and return it to the circuit while concentrating the solids into an underflow. That underflow has the consistency of a slurry or paste; producing a dry cake is not what a thickener is for. A filter press works by mechanical pressure, forcing out the water held between particles and leaving a handleable, stackable cake. A settling pond does both jobs slowly and at the cost of land: as the water stands still the fines settle to the bottom, the clear water above is drawn off, and the pond gradually fills and has to be cleaned out.

CriterionSettling pondThickenerFilter press
Working principleNatural settling in still waterAccelerated gravity sedimentationFiltration under mechanical pressure
Land requirementHighest, several ponds neededHigh, set by tank diameterLowest, modular and compact
Water recoveryPartial, losses to evaporation and seepageHigh, bulk volume returnedHighest, interstitial water squeezed out
Output consistencySludge that stays wet for yearsSlurry or pasteStackable solid cake
Flocculant demandUsually noneGenerally requiredDepends on upstream thickening
Operating burdenPeriodic pond desiltingContinuous dosing and monitoringBatch cycles, cloth maintenance

They are links in one circuit, not alternatives

In a modern washing circuit the most efficient arrangement is usually sequential. Slurry leaving the washer goes first to a thickener, where the bulk of the water is clarified and returned to the plant and the solids are concentrated. That concentrated underflow is pumped to a filter press, which produces a stackable cake and a filtrate clear enough to send back to the plant. The result approaches closed-loop water use. In this sequence the thickener handles volume and the press handles final drying; substituting one for the other makes the circuit either far too large or far too slow.

Which constraint forces which solution

Where land is plentiful and discharge permitting is flexible, the economical way to manage large water volumes starts with a high-rate thickener. Where discharge rules are strict, space is limited, or a settling pond will not be permitted at all, a filter press becomes unavoidable. The same holds where disposal cost is high: a dry, stackable product can be hauled or stored on site in a way that wet sludge cannot. The selection question is therefore not which is better but which constraint is binding.

Cake moisture and haulage cost

The return on dewatering shows up in two places. The first is water: every volume recovered is water that does not have to be sourced again, which reduces dependence on a well or a mains supply. The second is the cake itself. A stackable cake can be loaded onto a truck; wet sludge has to be either pumped or held in a pond. Because haulage is paid on the mass moved, including the water inside it, how dry the cake comes out feeds directly into disposal cost. That is why the first thing to examine in a press is not its capacity but whether the cake it produces can actually be handled.

The nature of the fines changes the choice

Whether the fines in the washed material are clay-bearing or dominated by rock flour governs settling behaviour. A clay-rich slurry settles slowly by nature and will not yield clear water without flocculant support; a settling pond alone falls short in that case, filling continuously and shortening the cleaning cycle. A slurry dominated by rock flour settles faster and asks for less chemistry. That distinction can be seen before the investment decision through a settling test; an arrangement chosen without one usually ends up either oversized or small enough to choke the circuit.

The question to ask before going wet

A dewatering investment makes sense where washing is genuinely necessary. Where the fines content and the specification can be met by dry screening, keeping water out of the circuit is the cheapest answer of all. That comparison is treated separately on the dry vs wet screening selection page and belongs before any dewatering discussion. Where washing is unavoidable, water and dust have to be planned together; the other subjects under environment and dust control keep both burdens inside one frame.

Frequently asked questions

Is a filter press still needed once a thickener is installed?

A thickener recovers the volume of water but does not make a dry cake. Where a pond exists to hold the underflow and disposal is not an issue, a press may not be required; without a pond, or where wet sludge has to be hauled, the press comes in.

Why are settling ponds still used?

Where land is broad, permitting is flexible and the fines load is low, a pond is the lowest-capital solution that works. Its limits are land and the cleaning cycle: as it fills, capacity falls and emptying becomes an operation in its own right.

Is flocculant use compulsory?

The material decides. In a clay-rich slurry gravity alone does not settle fast enough; where rock flour dominates the requirement drops noticeably.

Can press filtrate be reused for washing?

Filtrate from a filter press comes out clear enough to return to the circuit. That is the basis of near closed-loop operation, though the dissolved load building up in the circuit needs monitoring.

Definitions of technical terms: Glossary

Related Content

Baghouse jet pulse dust collector selection for crushing plants
ENVIRONMENT AND DUST CONTROL

Baghouse jet pulse dust collector selection for crushing plants

Dry dust extraction is decided by three numbers: the air volume to be drawn, the filter area it passes through, and the ratio betwe…

100 TPH, 200 TPH and 350 TPH Mobile Crusher Capacity Selection Guide
PROCUREMENT AND SUPPLY

100 TPH, 200 TPH and 350 TPH Mobile Crusher Capacity Selection Guide

100, 200 and 350 t/h are three different operating classes: feed opening, power unit, number of chassis and loading equipment all c…

Jaw Crusher Guide: Feed Openings, Hydraulic Adjustment and the Details Behind the Price
INVESTMENT AND COST

Jaw Crusher Guide: Feed Openings, Hydraulic Adjustment and the Details Behind the Price

Jaw crusher prices depend on feed opening size, primary or secondary type, mobile or stationary design and details such as flywheel…

Cone crusher hydraulic and lube system maintenance
MAINTENANCE AND WEAR

Cone crusher hydraulic and lube system maintenance

A cone crusher carries two independent fluid circuits, and treating them as one damages both. The lube circuit is governed by tempe…