Technology Reference / Extraction & Separation / Cryogenic Ethanol Extraction
Extraction & Separation

Cryogenic Ethanol Extraction

Washing feedstock with deeply chilled ethanol so the cold itself does the sorting — dissolving the target compounds while waxes, fats, and pigments stay behind, and skipping the winterization a warm extraction would need.

One of several extraction routes — the family of extraction and separation unit operations, including the solvent and supercritical CO₂ routes.See the other extraction technologies The crude and its staged fractions refine and separate further downstream in the distillation and purification family.See the distillation & purification technologies Raw material is ground and sized to expose surface area before it’s loaded into the vessel — the particle-prep family upstream.See the size-reduction technologies
What it is

Let the cold do the separating.

Cryogenic ethanol extraction is a cold-solvent unit operation. Feedstock is washed with ethanol chilled to roughly −40°F to −80°F. At that temperature the ethanol selectively dissolves the target compounds while leaving most of the heavy, undesired material — pigments, waxes, fats, lipids — behind, so the extract comes off the line essentially pre-cleaned. The solvent is recovered and recycled in a closed loop.

It’s a general separation technique, not a single-material one: only the feed changes. The applications differ; the process does not.

The defining feature is temperature. The cold is what buys selectivity — and what skips the downstream winterization step a warm extraction would require to drop out the same waxes and fats. Hold the temperature and the extract stays clean; let it drift warm and you’ve quietly turned a cold extraction into a warm one that pulls everything.

Compound-rich solvent is separated from spent solids and filtered, then the ethanol is recovered on a rotary or falling-film evaporator and recycled. What leaves the step is a cleaned crude, ready for distillation, isolation, or formulation.

Process flow
1

Feedstock loaded into the extraction vessel; cryogenic ethanol introduced (soak or flow-through)

2

Compound-rich solvent separated from spent solids, then filtered

3

Solvent recovered (rotary or falling-film evaporator); ethanol recycled back into the loop

A cleaned crude extract, ready for distillation, isolation, or formulation

The leversTemperature above all — plus soak time, solvent-to-feed ratio, and how completely the ethanol is recovered.
Why it matters

The most regulatory ground converges at the cold step.

It sits at the front of the production chain, and an uncontrolled extraction step is one nothing downstream fully recovers from. Purity, residual-solvent compliance, yield, and final potency are all shaped here — the crude you make is the ceiling for everything after it.

It’s also where the most regulatory ground converges at once: process control, equipment design, calibration, solvent accountability, and electrical-area classification all meet at the cold step. Get it right and the rest of the line builds on a clean foundation; get it wrong and every later control spends its effort compensating. The discipline is a reconciling solvent mass balance, a calibrated and recorded temperature probe at the cold step, area classification designed in, and cleaning validation written for what congeals when cold.

21 CFR 111 · supplementFor a supplement extract, the extraction temperature window and the crude’s specs live in the master manufacturing record, and each batch is verified against the cold operating window it came from.
21 CFR 117 · foodFor a food-grade extract — flavor or color concentrates — cold-ethanol extraction runs under preventive-controls cGMP, with food-grade ethanol residue treated as a controlled hazard.
USP <467> · residual solventsEthanol is a Class 3 solvent under USP <467>; the residual burden originates at the crude, so the limit is proven there, not only on finished product.
NFPA 30/70 · flammableEthanol is a flammable liquid — NFPA 30 storage-and-handling and NFPA 70 electrical-area classification, with an OSHA 1910.106 anchor, designed in rather than retrofitted.

The governing rule follows the product class; residual-solvent limits and — for flammable ethanol — NFPA 30/70 area classification with OSHA 1910.106 anchor the rest.

How it compares

Why a maker runs cold ethanol — and what they trade.

Cryo ethanol trades a heavier safety profile for throughput and a pre-cleaned crude. What it was chosen over tells you what mattered.

vs.

Supercritical CO₂

CO₂ has no solvent-residue concern and a cleaner story.

The tradeIt carries far higher capital cost; cryo ethanol wins on cycle time and cost to scale.
vs.

Warm / ambient ethanol

Warm ethanol pulls everything — pigments, waxes, fats — and needs a separate winterization step.

The tradeCold skips winterization entirely; the selectivity is bought with refrigeration instead.
vs.

Hydrocarbon (butane/propane)

Hydrocarbons can pull certain fractions efficiently.

The tradeThey bring tighter residual-solvent limits and a heavier safety profile; cryo ethanol is the lower-risk solvent route.
Where it tends to go wrong

The gaps a reviewer looks for on a cold-ethanol extraction.

Every process fails first in a few predictable places. For cold ethanol extraction they’re well understood.

The solvent that quietly doesn’t balance — ethanol received, consumed, and recovered in a loop, and when those volumes stop reconciling, something is lost, vented, or carried into product.

The one instrument that governs the step — a single uncalibrated or unrecorded temperature probe at the cold step undermines every batch through it, however tidy the rest of the file.

Area classification added after the equipment — designed in, it’s routine; retrofitted after install, it’s almost always incomplete.

Cleaning that ignores what congeals when cold — residues that move freely at room temperature set up at cryogenic ones, and cleaning built for the former carries the latter forward.

Extraction temperature treated as a setpoint, not a record — the parameter the whole method rests on left unproven batch to batch.

Residual-solvent testing run only on finished product, not on the crude where the ethanol burden actually originates.

If this is your operation

Six things to check against your own records.

Most of this you can check yourself, with records you already have. Pull a recent batch and walk it.

01

Pull a solvent mass balance for your last three batches — receipt, consumption, recovery. Do they reconcile, and if not, can you say where the difference went?

02

Find the instrument that controls the cold step and its last calibration — is it traceable and current?

03

Check when your area classification was done — before or after the equipment went in, and whether it was ever completed.

04

Ask what congeals at your operating temperature, and whether cleaning addresses it.

05

Confirm extraction temperature is recorded per batch, not just set.

06

Check the residual-solvent method tests the crude, not only the finished product.

Applications

The same operation, across very different feedstocks.

Only the feed changes; the cold step doesn’t. What stays constant is the control problem: hold the temperature, balance the solvent, prove the residue.

Supplement

Botanical concentrates

Producing pre-cleaned botanical crudes where the cold drops waxes and fats out up front, simplifying the refining that follows.

Food & beverage

Flavor & color concentrates

Extracting flavor and color compounds into clean concentrates, with food-grade ethanol residue controlled to the finished use.

Pharma

Natural-source crudes

Front-end isolation of a drug substance from natural material under cGMP, where temperature control and solvent accountability set the foundation.

Specialty

High-value plant actives

Cleaning sensitive plant actives at low temperature so heat- and oxidation-prone compounds survive the extraction intact.