DATASHEET / GLASS
Cullet and glass batch: abrasive, precise, dusty
A datasheet for glass batch and cullet handling: how sand, soda ash, limestone and cullet behave, the batch house steps from reception to charging, what wears and segregates, and what to check on an existing line.
Part of the guide: Transfer point design: dust, spillage and chutes
A glass furnace is fed by a recipe, not by a material. The batch house weighs several raw materials to tight tolerances, mixes them, wets them and delivers them to the furnace in a state that has to be the same every hour. Most are abrasive; one of them cakes in humid air; the sand carries a respirable dust hazard; and the recycled glass that makes up a growing share of the charge arrives sharp, variable and contaminated. What follows is how each component handles, where the batch house wears and segregates, and what a cullet line has to do.
What goes into the batch, and how does each part handle?
| Component | Role in the glass | How it behaves | Handling watch-outs |
|---|---|---|---|
| Silica sand | The glass former; the largest fraction | Hard, abrasive, free-flowing when dry; dusty | Respirable crystalline silica — enclosed transfers and extraction; liners everywhere; damp sand sticks to belts |
| Soda ash | Flux; lowers the melting temperature | Fine, dusty, hygroscopic; cakes and sets in humid air | Dry, closed storage; outlet and feeder drawn for a cohesive powder; residues corrode |
| Limestone and dolomite | Stabilisers | Granular, abrasive, dusty | Liner wear; dust at transfers |
| Feldspar or nepheline syenite | Alumina source | Fine to granular, abrasive | Liner wear; dust |
| Sulphate and minor additives | Fining, colour, decolourising | Small quantities; some hazardous | Precision weighing; closed handling; segregation in the mix |
| Cullet | Recycled glass; a large part of the charge | Sharp, abrasive, variable in size and moisture; contaminated | Metals, ceramics and stones must come out; shards cut belts and wedge in screws; wet fines stick |
The behaviours in the table are directions, not design values. Bulk density, moisture, particle size and flow behaviour vary between sources and grades, and a batch house is sized on the materials it actually receives, measured, rather than on the ones the recipe names.
How does a batch house work?
- Reception
- Bulk road or rail delivery, unloaded pneumatically or mechanically into silos; sand may arrive damp and need drying before it will weigh and flow consistently.
- Storage
- One silo or bin per component. Sand and limestone flow; soda ash and fine additives need hoppers drawn for cohesive powders — see the pillar note on bridging and ratholing.
- Weighing
- Each component is fed into a weigh hopper on load cells — one cumulative hopper or a scale per material — to a tolerance the glass chemistry sets. Feeder cut-off, tare drift and residue in the hopper are the accuracy questions.
- Mixing
- A batch mixer homogenises the weighed components; too short leaves streaks in the glass, too long segregates and makes dust.
- Wetting
- A small percentage of water is added to bind the fines, limit dust and reduce segregation between the mixer and the furnace.
- Charging
- The wet batch, with cullet mixed in or added alongside, travels by belt or elevator to the furnace hoppers and is fed by a batch charger at the doghouse.
What wears, what segregates, what dusts?
Three questions decide most of the equipment. Wear: sand and cullet cut steel, so every chute, hopper cone, screw and elevator boot is lined and belt covers are chosen for abrasion; a liner is a wear part with a replacement route, not a finish. Segregation: the batch is a blend of materials with different sizes and densities, and every drop, every pile and every centrifugal elevator head separates them a little — which is why continuous-discharge elevators are the usual choice for mixed batch (the note on discharge types explains why), why drop heights are kept low, and why the pillar note on transfer point design applies with unusual force. Dust: silica dust is a health matter, soda ash dust a corrosion and housekeeping matter, and both are made at open transfers.
- Belt covers and cleaners — damp sand builds a layer on the belt that ordinary cleaners smear; the note on carry-back and belt cleaners sets out the choice.
- Enclosed transfers with extraction — for any sand or soda ash transfer, with the hood where the dust is made rather than where it is convenient.
- Wetted batch — the water is the dust control between mixer and furnace; a wet batch dropped from height still segregates, but it does not dust.
What is different about a cullet line?
Cullet is glass, but it is not batch: it arrives as a mixed, dirty, sharp solid, and the line's job is to turn it into a clean, sized, dry material before it meets the batch. Internal cullet from the plant's own rejects is predictable; external, post-consumer cullet is not.
- Crushing to a size the charger and the furnace accept, in a machine that tolerates the contaminants not yet removed.
- Contaminant removal — magnets for ferrous metal, eddy-current separation for non-ferrous, and optical or mechanical sorting for ceramics, stones and porcelain, which do not melt and end up as defects in the glass.
- Screening to remove fines and organic debris, which carry moisture and burn in the furnace.
- Storage and reclaim in bunkers or silos that tolerate a sharp, abrasive material of variable moisture; dry cullet flows, wet cullet with fines does not.
- Conveying by belt or vibrating feeder rather than screw wherever possible; shards wedge between flight and trough.
What to check on an existing batch house
- Scale calibration and tare drift on every weigh hopper, and residue on the hopper walls after discharge.
- Feeder cut-off — how much material is in flight when the feeder stops, and whether the control allows for it.
- Soda ash silo — bridging record, moisture ingress, condition of the cone and feeder; whether the vent filter keeps the silo dry.
- Mixer — liner and paddle wear, residue build-up, mixing time against what the glass quality data shows.
- Batch water — metering and distribution; dry streaks in the batch mean dust downstream.
- Liners — thickness at the impact points of chutes and hopper cones; belt cover wear pattern and cleaner condition.
- Silica dust controls — hood positions, extraction, enclosure integrity and housekeeping, against the plant's exposure assessment.
- Cullet contaminants — what reaches the furnace hoppers; magnet cleaning routine; screen condition; wear in the crusher.
Much of a batch house is standard handling equipment working to unusual tolerances, and the difference lies in the specification of liners, feeders, sealing and access. Our equipment, components and spares work covers the wear parts, feeders and transfers a batch house consumes; the glass duties in the Flow Finder list the equipment types involved.
QUESTIONS WE HEAR
Why is glass batch wetted before it goes to the furnace?
A small addition of water binds the fine components to the coarser ones, so the batch dusts less at transfers and in the furnace and segregates less on the way. It also helps the batch melt more evenly. The amount is set by the plant: too little and the batch dusts, too much and it sticks, and freezes in winter.
Which conveyor is best for cullet?
A belt conveyor with an abrasion-resistant cover, low drop heights and lined chutes, or a vibrating feeder for short transfers. Screw conveyors are a poor choice: shards wedge between flight and trough and the flights wear quickly. Bucket elevators work with heavy-duty buckets and a lined boot.
Why does soda ash bridge in the silo?
Soda ash is hygroscopic and cakes when it takes up moisture from humid air or from damp aeration air. Caked material has real cohesive strength and arches over an outlet sized for a free-flowing powder. Dry, closed storage, a hopper and feeder designed for a cohesive powder and a vent that keeps moist air out are the usual answers.
How do you stop batch segregating between the mixer and the furnace?
Wet the batch, keep drop heights low, use continuous-discharge rather than centrifugal elevators, avoid intermediate stockpiles and long belts with many transfers, and add cullet as late and as gently as the layout allows. Segregation cannot be reversed downstream; it can only be avoided.