Phosphate Rock Filter Cloth for Horizontal Vacuum Belt Filters
This is the mine-side duty. Beneficiated phosphate rock concentrate and flotation tailings are dewatered in the beneficiation plant before the concentrate is shipped or fed forward and the tailings are stacked. Where that dewatering runs on a horizontal vacuum belt filter, the filter cloth is a consumable endless belt fabricated to the machine's dimensions.
What comes off a phosphate beneficiation plant
Phosphate rock as mined is not saleable. It is crushed and ground, the clay slimes are cycloned out, and the sized fraction goes to froth flotation, where apatite is separated from siliceous gangue — on many flowsheets in two stages, an anionic fatty-acid float of the phosphate followed by a reverse amine float of the silica. Two streams come out of that: a concentrate that carries the value, and a tailing that carries the sand and whatever clay survived desliming.
Both streams leave flotation far too dilute to move or to stack, so both are thickened and then filtered. That is the duty this page is about. The concentrate is filtered because moisture is freight you pay for and because the next step — shipping, drying, or feeding an acid plant — has a moisture ceiling. The tailing is filtered because a dewatered tailing can be stacked and the water goes back to the circuit instead of into a pond.
The cloth itself is a consumable. It is an endless belt fabricated to your machine's width and circumference, running on the grooved rubber transporter, and it is replaced on a cycle set by your duty rather than by a catalogue.
Same industry word, different plant. This page is the mine. Phosphogypsum is the by-product gypsum filtered inside the acid plant, in an acidic fluoride-bearing liquor, on a belt whose wash stage exists to recover soluble P2O5. Different slurry, different chemistry, different reason to wash.
Phosphogypsum filtration →The two phosphate duties, side by side
| Compared on | Phosphate rock (this page) | Phosphogypsum (acid plant) |
|---|---|---|
| Where it happens | Beneficiation plant at the mine | Wet-process phosphoric acid (WPPA) plant |
| What is on the belt | Apatite concentrate, or flotation tailings (siliceous sand plus clay slimes) | Calcium sulphate by-product gypsum |
| Liquor | Recycled process water carrying flotation reagent residue | Acidic, fluoride-bearing mother liquor |
| What the wash does | Displaces process water, where a wash stage is fitted at all | Recovers soluble P2O5 from the cake, counter-current |
| Why the cake matters | Moisture drives freight cost, or stackability on the tailings side | Wash efficiency drives acid yield |
A plant can own both duties — the mine site and the acid plant are sometimes the same company, occasionally the same fence line. They are still two cloth specifications. If you buy for both, say so on the RFQ and they will be quoted as two.
Process flow across the belt
- 01 Beneficiation Ground rock is deslimed and floated; apatite reports to concentrate, siliceous gangue and clay to tailings.
- 02 Thickening Both streams leave flotation dilute and are thickened before they are worth putting on a filter.
- 03 Slurry Feed Thickened underflow is distributed across the moving cloth at the feed end.
- 04 Filtration Vacuum pulls process water through the cloth; the cake builds on the surface.
- 05 Wash (where fitted) A wash stage on this duty displaces reagent-bearing process water. It is not recovering acid.
- 06 Dewatering & Discharge A dry-vacuum zone pulls residual moisture out; cake goes to stockpile, shipping or the stack.
Operating values for each stage — feed solids, particle size distribution, slimes fraction, liquor temperature, cake moisture target — are plant-specific and they differ between the two streams. We do not publish typical figures for them; they go on the confirmation list below instead.
What makes this duty hard on a belt
The chemistry here is not the problem the acid plant has. The liquor is recycled process water carrying flotation reagent residue rather than a hot acid. What is hard on this duty is the solids: clay fines that blind, sand that abrades, and reagent residue that changes how the cake lets go.
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Clay slimes blind the fabric
Phosphate ores carry clay. Whatever the desliming stage does not remove arrives at the filter as ultrafine solids that lodge in the fabric and close the free area.
Cloth implication: Weave geometry and surface finish decide how fast the fabric closes and how much of it washes back.
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The gangue is abrasive
The siliceous fraction that rides with a phosphate concentrate, and dominates a flotation tailing, is hard and angular. It abrades the cloth surface and works at the edges and the discharge roller.
Cloth implication: Abrasion resistance and edge treatment are specification items on this duty, not details left to the fabricator.
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Flotation reagents stay in the water
Anionic fatty-acid collectors, amine reagents on a reverse silica float, frother and fuel oil do not all report to the froth. What remains is a surface-active, partly oily residue in the liquor the cloth sits in.
Cloth implication: Reagent residue changes wetting and release behaviour, so a cloth chosen on particle size alone can still blind.
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Two streams are not one duty
Concentrate is a product stream judged on moisture and on not losing value to the filtrate. Tailings are a disposal stream judged on throughput and water recovery. Plants often run both on belts in the same building.
Cloth implication: One cloth specification covering both streams is a decision that has to be argued, not assumed.
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Tracking and wrinkling
The belt wanders on the grooved rubber transporter, touches the edge guides, and the vacuum seal starts leaking. Common to horizontal vacuum belt duty, not specific to phosphate.
Cloth implication: Fabricated length, seam squareness and edge treatment all feed into whether a belt tracks.
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Seam and joint leakage
A clipper or PAD joint opens up, vacuum drops as the joint passes the box, and the cake wets back. Also general to this machine family.
Cloth implication: Seam type is a specification to be decided, not a detail left to the fabricator.
The statements above are industry-level process knowledge about phosphate beneficiation and about horizontal vacuum belt duty. How severe each one is on your circuit depends on numbers we do not have yet — which is what the confirmation list is for.
The machines this duty runs on
Horizontal vacuum belt filters are one of the routes used for phosphate concentrate and tailings — not the only one. The families below are the ones observed in phosphate or mining service; the evidence level is stated as we found it, not upgraded.
| OEM family | Industries observed | Evidence level | Next step |
|---|---|---|---|
| ANDRITZ Delkor HVBF | Mining, fertilizer | OBSERVED | Send brand + model |
| TAKRAF DELKOR HBF | Phosphate, iron, coal | OBSERVED claims | Send brand + model |
| FLSmidth EIMCO Extractor | FGD, minerals | OBSERVED trade | Send brand + model |
| EKCP EIMCO-KCP | IN FGD + phosphate | OBSERVED | Send brand + model |
| GKD HVBF equipment | Mining, Li / PGM, fertilizer | OBSERVED | Send brand + model |
| Roytec VBF | Mining, spodumene mention | OBSERVED | Send brand + model |
| Metso Larox RB | Minerals | OBSERVED portfolio | Send brand + model |
| Toncin DU | CN FGD, mining, Li | Company-reported | Send brand + model |
| WesTech HBF | Minerals, FGD directories | PARTIAL | Send brand + model |
Phosphate concentrate is also dewatered on disc and drum vacuum filters, on pressure filters and on centrifuges, and a great deal of phosphate tailings is still sent to ponds rather than filtered at all. If your plant is on one of those routes, this belt page does not apply to you — tell us your machine and we will say honestly whether we can help.
OEM names above are used only to identify the machine a cloth has to fit.
How the cloth is specified for this duty
Selection runs backwards from the slurry. On the mine side the first questions are not chemical: what is the particle size distribution, how much of it is clay, how abrasive is the gangue, and is this the concentrate stream or the tailings stream. Those narrow the weave, the surface finish and the abrasion specification. The liquor — recycled process water, reagent residue, whatever the site's water balance has concentrated in it — then narrows the polymer. The machine narrows the fabricated dimensions, the seam and the edge treatment. The candidate polymers for horizontal vacuum belt duty are PET monofilament, PET mono/multifilament combinations, polypropylene, double- and multi-layer weave constructions, and hydrolysis- or alkali-resistant specialities.
We are not going to tell you on a web page which of those your belt should be. That decision belongs to your ore, your reagent regime and your machine — and getting it from a published table instead of from your data is how a plant ends up with a cloth that dewaters the concentrate well and blinds on the tailings line next door.
Specification status
Our factory specification package has not been confirmed in writing yet, so every parameter reads UNKNOWN. Each one is fixed against your machine and slurry during the engineering review, and it is stated in the quotation — not inferred from this page.
| Parameter | Value | Unit | How it is fixed |
|---|---|---|---|
| Polymer | UNKNOWN | — | Confirmed against liquor chemistry and reagent regime |
| Weave / construction | UNKNOWN | — | Confirmed against particle size distribution and duty |
| Air permeability | UNKNOWN | L/dm²/min | Test method and test pressure will be stated with the value, once the mill confirms them in writing |
| Fabric weight | UNKNOWN | g/m² | Reported with the value, once confirmed in writing |
| Abrasion resistance / surface finish | UNKNOWN | — | Confirmed against solids abrasiveness and discharge geometry |
| Seam type | UNKNOWN | — | Confirmed against machine and seam photo |
| Edge treatment | UNKNOWN | — | Confirmed against machine edge seal |
| Max fabricated width | UNKNOWN | mm | Confirmed against machine width during the engineering review |
| Continuous temperature limit | UNKNOWN | °C | Confirmed per polymer and finish |
Industry reference — not our specification
| Parameter | Industry reference | Unit | Source |
|---|---|---|---|
| Belt width commonly reached on this machine family | 4.5–4.8 m | — (value carries its own unit) | Equipment-family observation, third-party machines |
This row describes the machine population commonly used on this machine family, not what we can supply. Our own width limit is on the UNKNOWN list above until the factory confirms it. Dimensions are taken from your old belt — how to measure it →
What we can build for this duty
The parameter table above reads UNKNOWN because our own values are not confirmed in writing yet, and we will not fill that table with industry averages. This section is the other half of the answer: the options this cloth is actually built from, what each one changes, and which piece of your data decides it. Nothing below is a specification — it is the shape of the decision.
Cloth form An endless belt fabricated to your measured width and developed length, on a mine-side machine rather than an acid-plant one.
Recommended material direction
The distinguishing variable here is mechanical rather than chemical. The siliceous gangue is hard and angular and it works on the cloth surface, at the edges and at the discharge roller. The liquor is recycled process water carrying flotation reagent residue rather than acid from a reactor — but what its pH actually is depends on your reagent scheme and is not something this page knows. So abrasion resistance moves to the front of the polymer decision on the evidence available, and the chemistry has to come back and confirm it.
This narrows the field; it does not pick. Which polymer goes on your machine is settled against your measured numbers and not on a web page — the same position the selection section above takes. What follows is the reasoning behind that position, not a departure from it.
- Polyester (PET) PET
Continuous reference up to ~150 °C — a published property of the polymer, not a value of ours
- Acid Good
- Alkali Limited
- Hydrolysis Limited
- Abrasion Excellent
Excellent abrasion resistance and dimensional stability under tension, and nothing in a non-acidic reagent-bearing process water attacks it. This is the duty where the abrasion column of the polymer table earns its place.
- Polyamide (Nylon 6 / 6.6) PA
Continuous reference up to ~110 °C — a published property of the polymer, not a value of ours
- Acid Poor
- Alkali Good
- Hydrolysis Moderate
- Abrasion Excellent
The other polymer with excellent abrasion resistance — and here the usual objection to it, acid attack, does not apply. The remaining objection does: it absorbs moisture and changes dimension with it, which complicates a tensioned belt.
- Polypropylene PP
Continuous reference up to ~90 °C — a published property of the polymer, not a value of ours
- Acid Excellent
- Alkali Excellent
- Hydrolysis Excellent
- Abrasion Good
Chemically untroubled by this liquor, but its abrasion resistance is good rather than excellent, and that is the wrong column to compromise on a hard angular gangue.
- PTFE The best cake-release surface available and the worst mechanical fit for a tensioned endless belt: low tensile modulus, high creep, and a cost in a different bracket.
What actually decides it The measured pH of the recycled water — including after a reagent change, because the scheme is what sets it — and then a mineralogical breakdown or assay if the plant has one. Photographs of where the last belt actually wore settle the rest: edge wear and discharge-zone wear tell a different story from general surface wear, and they lead to different answers.
Everything in this block is reasoning from published polymer behaviour applied to the chemistry described further up this page. It is a direction, not a selection — and the selection is made against your measured numbers during the engineering review, then written into the quotation. The full polymer envelope is on the materials page.
Weave options
On an abrasive duty the structural back is doing mechanical work, not just carrying the filtering face.
- Double layer / multi-layer Two or more interlaced fabric layers woven as one. A fine filtering face carried on a coarse structural back — high strength with fine retention, and drainage channels inside the fabric. Watch: Thicker and heavier; more expensive to weave. The usual answer on heavy belt duties.
- Plain One over, one under. The most stable and the most rigid. Tight, uniform pores; lower permeability for a given yarn. Watch: Least forgiving of dimensional movement; can blind faster on fine solids.
- Twill The crossing point steps sideways each pick, giving a diagonal rib. More flexible and more permeable than plain at the same yarn count, with better cake release. Watch: Slightly less dimensionally stable than plain.
Strength and retention are chosen together as one requirement. A fabric specified only for its rating will meet the rating and lose the belt.
Yarn form. Monofilament gives the surface that releases and washes back; where the feed carries a wide particle distribution a mono-and-multi combination is the usual compromise between release and retention.
Yarn form, weave and surface finish are settled as one decision. The four yarn forms available are monofilament, multifilament, mono + multi combination and staple / spun.
Permeability considerations
Air permeability is the figure everyone compares and the easiest one to quote meaninglessly. It is measured per ISO 9237 at a stated pressure drop — often 200 Pa — or per ASTM D737 (Frazier). A value with no stated pressure and no stated unit is not comparable to anything, including ours. The same applies to a pore or retention rating: on a woven cloth that is a nominal figure and not an absolute cut-off, because woven media do not have a single pore size and the cake quickly becomes the real filter.
Permeability on this duty has to be read alongside the abrasion question: a very open structure discharges and washes well and offers the gangue less material to work on per unit of surface. Ask for the figure with its method and pressure; a number on its own settles nothing.
How each property is measured, and what to ask any supplier for alongside the number, is set out on the testing and inspection page. Naming the method is a fact about a public standard, not a claim about our laboratory.
Joint options
- Clipper (metal hook) Interlocking metal hooks crimped onto both cloth ends, joined by a pintle wire. Fitted and replaced on the machine without dismantling it. The fastest change-out. Watch: The joint is a discontinuity: it leaks vacuum as it passes the box, and it is where most belt failures start. Hook material has to suit the liquor.
- PAD / welded overlap The two ends are overlapped and thermally fused. A smoother, quieter joint that seals better than a clipper and carries load more evenly. Watch: Made off the machine or with a portable press; a change-out takes longer.
- Spiral Spiral coils on each end interlaced and pinned. Flexible, drains through the joint, distributes load along the full width. Watch: Adds an open line across the belt — not appropriate where the joint must seal.
The joint is where the belt carries its load and where it loses its vacuum seal. Match it to what the machine is already set up for, from a close-up photograph of both faces.
The four constructions drawn in cross-section: how joints fail and what each one costs you.
Edge treatment
- Cut and sealed The cut edge is thermally sealed against fraying. The baseline. Adequate where the machine edge seal is in good condition.
- Folded / hemmed The selvedge is folded back and secured. Adds thickness and stiffness at the edge where the seal rubs.
- Reinforced edge band A separate band is bonded along the selvedge. For machines that chew edges — the usual answer when a belt keeps failing at the edge while its body is sound.
- Coated / sealed band A polymer band is applied to the edge. Seals the edge against vacuum bypass as well as protecting it mechanically.
- Guide strip / tracking profile A profile bonded to the underside to run in the machine guide. Only where the machine is built for it. Fitting one to a machine that is not is a common and expensive mistake.
A reinforced edge band is the usual answer when a belt keeps failing at the edge while its body is still sound, and on a hard angular gangue the edge is exactly where the wear concentrates. A guide or tracking profile is a different matter: it goes on only where your machine is built to take one, because fitting one to a machine that is not causes the fault it was meant to prevent.
Relevant equipment
A filter belt is decided at the loom before it is decided anywhere else: what a weaving platform can hold — pick density, tension, width — sets what the finished cloth can be asked to do. Our weaving runs on DORNIER (Germany) and Sulzer (Switzerland) platforms, machines built for technical textiles rather than for apparel.
A mine-duty belt is wide, heavy and stiff, and holding a consistent pick density right across the web is a property of the weaving platform rather than of the finishing line. What width we can hold it across is the one number we have not confirmed in writing yet — send your measured width and we will answer it rather than assume it.
Model designations, working widths and installed quantities are being confirmed against the machine nameplates and are not published until they are. A weaving platform is easy to name and hard to fake, and we would rather you were able to check.
The full platform description, the eleven process stations from yarn to crate, and the nine laboratory checks: manufacturing.
Factory capability for this duty
The rows below are the part of our capability envelope that this duty touches. The last group is the one that makes the rest of it worth reading — a supplier who can do everything has told you nothing.
Machine families
- Rubber-belt horizontal vacuum belt filter Built to your spec
Core family. Endless belt with clipper, PAD or spiral joint and a finished edge.
What decides it Brand and model, measured width and developed length, a photograph of the joint.
Cloth construction
- Plain, twill, satin, double and multi-layer weave Built to your spec
Double layer is the usual answer on heavy belt duties — a fine face on a coarse structural back.
What decides it Strength and retention requirements together.
Fabrication
- Edge: cut and sealed, hemmed, reinforced band, coated band Built to your spec
The usual answer when a belt keeps failing at the edge while its body is still sound.
What decides it Photographs of both edges and of the machine edge seal.
- Guide / tracking profile Engineering review
Only where your machine is built to take one. Fitting one otherwise causes the fault it was meant to prevent.
What decides it A photograph of the belt underside and the guide rail.
What we do not do
- OEM spare parts Not offered
Replacement cloth fabricated to your machine dimensions. Not an OEM spare part.
The full envelope, including the machine families and services we decline: what we build to order and what we will not take on. Fifteen pages on how a specification like this is built and read: the filter cloth specification guide.
How phosphate rock belts come off the machine
A failed belt is usually three-way: something in the cloth, something in the machine, and something in the process. On this duty the process leg is unusually loud, because a change in the desliming circuit or the reagent dose reaches the filter before anyone writes it down.
Blinding by slimes and reagent residue
Process-side (desliming performance, reagent dosing, wash balance) interacting with weave choice.
Diagnose this →Abrasive wear and edge fray
Cloth-side and machine-side: fabric and finish against feed distribution, edge seal condition and discharge geometry.
Diagnose this →Belt tracking and wrinkling
Often machine-side (roller alignment, edge guides) before it is cloth-side.
Diagnose this →Seam / joint failure
Cloth-side and fabrication-side: seam type, squareness, and how the joint was closed on site.
Diagnose this →Cloth life on a horizontal vacuum belt filter is duty-specific, and on an abrasive mineral duty the spread is wider than on a chemical one. Published third-party cases run from weeks to months depending on slurry and machine condition, and we do not quote a life figure before seeing your duty. Anyone who promises you a number of months without asking what you filter is selling, not engineering.
Measuring the old belt and photographing where it failed is the first step in telling the three causes apart. How to measure your old belt →
What we need from you to quote
This list is the engineering RFQ in plain form — what you gather here is exactly what the form asks for. Nothing on it is optional because we like paperwork; each item removes a guess from the specification.
| What to confirm | How to get it |
|---|---|
| Which stream this belt runs | Concentrate or tailings. If the plant runs both, tell us both — they are quoted separately. |
| Machine brand and model | Copy it off the machine nameplate. “Unknown” is an acceptable answer. |
| Belt width | Measure the old cloth across the web, not the rubber transporter. |
| Belt length (circumference) | Measure the endless loop, or give us the machine centre distances. |
| Seam type in use now | Photograph the joint close up — clipper, PAD, or spiral. |
| Photos of the old cloth | Face and back, plus wherever it failed. This is the single most useful thing you can send. |
| What failed | Life, blinding, abrasion, tracking, seam leak, or cake release. Compare against the failure modes above. |
| Solids and particle size | Feed solids and a sizing from the plant laboratory, including the slimes fraction if you have it. |
| Reagent regime and process water | Collector type, whether a reverse silica float is run, and anything known about recycled water quality. |
Before you enquire
Can one cloth cover both the concentrate line and the tailings line?
Sometimes, and it is worth asking, because a single specification is cheaper to stock and cheaper to buy. But it has to be argued from the two particle size distributions and the two moisture targets, not assumed because both streams come out of the same flotation plant. Send the data for both lines and you will get a straight answer, including the answer that they need two different belts.
Get an engineering quote for phosphate rock duty
Three steps after you submit: an engineer checks what you sent against the machine, we come back for anything missing, and you get a quotation or a sample plan.
Every belt is fabricated to your machine dimensions — we quote per RFQ. No online checkout.
Samples available — freight terms confirmed per request.
Where to go next
Phosphogypsum Filtration
The other phosphate duty: the acid plant, not the mine. Separate slurry, separate wash.
HVBF Filter Cloth
The cloth family this duty uses: weave, polymer, seam, edge and width options.
HVBF Compatibility
OEM families, what we can fit, and what we need from each machine.
Measure Your Old Belt
Width, circumference and seam — how to take them so the replacement fits.