Ethanol extraction line
A cold ethanol line for hemp is a chilling problem first and an evaporation problem second. Ethanol is chilled to -40 F before it meets the biomass so it dissolves cannabinoids and leaves chlorophyll and waxes behind; the loaded solvent, the miscella, is filtered and evaporated; the ethanol vapor is condensed and returned; the crude is winterized, decarboxylated and distilled. Every step has an exchanger, and the ones sized wrong are the ones at -40 F.
This page is the ethanol side: the solvent chiller, the miscella and crude, the evaporator condenser and the glycol loop. Hydrocarbon and CO2 are on the Cannabis page.
Ethanol is easy to chill; the fluid chilling it is not. At -40 F ethanol is about 4.5 cP, while 60 percent propylene glycol at -50 F is over 100 cP and creeping. The plate exchanger that chills 20 gpm of ethanol from 70 F to -40 F, about 190,000 Btu/h, is sized almost entirely by the glycol film, and the fix is flow: 2 to 3 times the ethanol flow on the glycol side, a high-theta chevron plate to force turbulence, and a 10 F approach rather than the 3 F a water duty would get. A potassium formate or silicone fluid cuts the viscosity five to ten times and halves the plate count; HeatX quotes the exchanger both ways so the plant can see the difference.
After extraction the ethanol carries cannabinoids, some wax, fine biomass and water pulled from the plant. Kept cold on the way to the filter and the evaporator it stays clean; let it warm and the waxes redissolve into the crude. An in-line miscella cooler is a tube-in-tube, because the stream drops wax onto a cold wall and a plate channel plugs in a shift. The same applies to winterization, where crude in ethanol at 10 to 1 is chilled to -20 to -40 F for a day in a tube-in-tube or a jacketed tank. Wall temperature matters more than bulk: glycol at -60 F freezes wax onto the tube even with bulk ethanol at -20 F, so the glycol is tempered to a few degrees below target.
A falling-film or rising-film evaporator strips ethanol at 100 to 500 lb/h, under vacuum at 100 to 120 F or at atmospheric pressure at 173 F. The condenser is sized on that vapor rate, the pressure and the cooling fluid, with a sub-cooling section that brings the condensate 20 F below its boiling point so the receiver vent does not carry ethanol to the vacuum pump. Under vacuum the condensing temperature is close to summer tower water and the condenser needs chilled water or the evaporator rate falls every July. It is a vertical shell-and-tube with vapor on the shell, a vent at the top and a drain at the bottom, 316L on the ethanol side because the condensate meets product again. Recovery condensers for ethanol and other extraction solvents are covered in more depth on our solvent recovery condenser pages.
Buying a chiller by tonnage and the exchanger by area, separately, and finding at commissioning that the two do not meet. A 20 ton chiller at -50 F delivers perhaps 8 tons, and an exchanger with a 3 F approach on 100 cP glycol uses half of that. The line makes 60 percent of its rated batches and the operators blame the chiller. Glycol temperature, flow and fluid are chosen first, the exchanger is sized on them, and the chiller is bought to deliver that glycol with the real derating.
Send HeatX the ethanol flow, evaporator rating and chiller fluid and temperature, and the four exchangers are sized as a set. Call and talk it through with an engineer: 1-805-484-2992
Ethanol extraction runs cold and the rows show what the exchanger is sized for, including the area and the finish. Compare them with your extractor and send the solvent, flow and target temperature with the quote request.
| Condition | Detail |
| Product | Food-grade ethanol 190 to 200 proof; miscella; crude in ethanol for winterization |
| Flow range | Solvent chiller 5 to 60 gpm; evaporator condenser sized on 50 to 500 lb/h ethanol vapor |
| Temperatures in / out | Ethanol 70 F to -40 F; condenser 173 F vapor to 60 F liquid, or vacuum at 100 to 120 F |
| Hold | Biomass contact 5 to 20 minutes; winterization 24 to 48 hours |
| Utility | Glycol or low-temperature fluid at -50 F on the chiller; tower or chilled water on the condenser |
| Approach | 10 F on the chiller because the cold fluid is viscous; 15 to 20 F on the condenser |
| Construction | Gasketed plate on clean ethanol; tube-in-tube on miscella and crude; shell-and-tube condenser |
| Finish / class | 316L product side, 32 Ra or better; food-grade gaskets rated for ethanol at -40 F |
| Area | Class I Division 1 or 2 around extraction and evaporation; the skid carries the rated electricals |
| CIP | Ethanol rinse between strains; hot ethanol or caustic CIP on a schedule |
Below about -30 F chlorophyll and most waxes stay in the biomass; colder gains little and costs chiller capacity. Warmer than -20 F the extract is green and needs heavy winterization.
Plate for clean ethanol to the extraction vessel: highest coefficient, small holdup of cold flammable solvent. Tube-in-tube once the ethanol carries wax, solids or crude.
At atmospheric pressure ethanol condenses at 173 F and tower water does it easily. Under vacuum at 100 to 120 F chilled water is needed in summer.
316L at 32 Ra or better, drainable, food-grade gaskets. Pharmaceutical finish is not required on the extraction side.
Hydrocarbon, ethanol or CO2: the solvent decides the exchangers, the area classification decides the skid.
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Jacket water at 37 C, held to a tenth of a degree, by a heater and a cooler that never touch the culture.
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Below -20 F the fluid on the cold side is the design, and the exchanger is sized on it, not on the solvent.
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