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Your most expensive effluent is a fuel.

Spent wash is the largest single line on a distillery's environmental budget. It is also the densest organic feedstock in the sector — already liquid, already pumpable, already inside the fence line, with a known load that does not vary by ward or by weather.

01
The stream

Eight to fifteen litres for every litre of alcohol.

Spent wash leaves the distillation column hot, acidic, dark and carrying an organic load an order of magnitude above ordinary industrial effluent. Under zero liquid discharge it cannot be released, so it is concentrated, incinerated or composted — all of which consume energy the distillery buys. Biomethanation sits ahead of every one of those steps and removes most of the load before they run.

The load you are paying to destroy is the yield.

Chemical oxygen demand is the cost driver in the effluent plant and the energy content in the digester. They are the same number read from two sides of the ledger.

8–15 L
Spent wash per litre of alcohol
Varies with the molasses grade and the distillation configuration.
Very high
Organic load (COD)
An order of magnitude above ordinary industrial effluent — which is what makes the gas yield worth having.
Acidic
As-discharged pH
Corrected before the digester; the buffering regime is set during commissioning.
Year-round
Availability
Tracks the distillery's own run days, not a harvest window.
02
Where it fits

Ahead of the evaporator, not instead of it.

Fig. 1 · Effluent train
Biomethanation inserted at stage 02
01
Spent wash
Hot, acidic, high-COD stream leaving the distillation column.
02
Biomethanation
Anaerobic digestion strips the bulk of the organic load and releases biogas.
03
Concentration
Evaporation on a much lighter load than before — the main operating saving.
04
Incineration / composting
Residual handling under zero liquid discharge, correspondingly reduced.
05
Potash recovery
Ash and concentrate carry recoverable potassium back out as fertiliser value.

Biomethanation does not replace the zero liquid discharge train — it reduces what the train has to handle. Downstream evaporation and incineration run on a materially lighter load, which is where most of the operating saving sits.

03
Typical engagement

What a distillery-attached plant looks like.

Typical capacity Sized to daily spent wash volume and measured COD
Primary feed Spent wash, fed continuously from the distillation train
Co-feed options Press mud where a mill sits on the same premises
Operating days Matched to distillery run days; buffer storage covers shutdowns
Process High-rate anaerobic digestion with pH and buffering control
Purification Water scrubber to SATAT purity, two-stage H₂S removal
Gas destination Bottled BioCNG, or captive boiler fuel where offtake is unavailable
Residue value Potash-rich concentrate and ash recovered as fertiliser input
Commercial models Distillery-owned with EPC + O&M, or built and operated by us on a long-term effluent agreement

Indicative envelope for scoping only. Sizing is re-derived from your own spent wash volume, COD and run calendar in the DPR.

04
Why upgrade the gas

Most distillery biogas is burnt in the boiler. That is the cheapest possible use of it.

Raw biogas fired under a boiler displaces coal or bagasse at fuel value. The same gas, scrubbed to SATAT purity and bottled, sells as transport fuel into a mandated blending obligation. The digester is identical; the difference is the purification and bottling island bolted onto the end of it, and the difference in what the gas earns is not marginal.

01
From fuel value to fuel price

Boiler gas is worth the coal it displaces. Bottled BioCNG is worth what transport fuel is worth, under a contracted framework.

02
From cost centre to revenue line

The effluent plant stops being purely a compliance expense and starts carrying a saleable output alongside it.

03
From disposal to nutrient recovery

Potassium that would have gone up the incinerator stack or into a compost yard is recovered and priced as fertiliser.

Send us a spent wash analysis.

Daily volume, COD, pH and your run calendar. We will come back with a gas estimate and what it does to your effluent operating cost.

Talk to us DPR & feasibility