PRODUCTION GUIDE, FOR BUYERS DECIDING WHAT TO BUILD
LAST UPDATED 09.14.2026

LIVE RESIN AT COMMERCIAL SCALE

Commercial live resin requires four things: fresh-frozen material kept at -80 C, a hydrocarbon system held at -60 to -70 C, a propane-forward solvent blend, and a C1D1 room. Our systems ship running on liquid CO2; a chiller can be specified at purchase or retrofitted later. Live resin is only taught from day three of operator training on.

01

THE PROCESS

01
FREEZE AT HARVEST
-80 C
The plant goes into the freezer wet, at the time of harvest. This is the step that makes it live resin. Nothing downstream can put back what a cure takes out.
02
COLD COLUMN LOAD
-60 to -70 C
Material goes into a column already at temperature, and stays there. Warm the column and you are running cured material with extra water in it.
03
BLEND AND SOAK
PROPANE FORWARD
A propane-forward blend pulls terpenes at low temperature where butane alone goes sluggish. Soak time is short, because selectivity is the goal, not yield.
04
RECOVER AND PURGE
LOW AND SLOW
Recovery and the purge schedule both run cooler and longer than a cured-material run. This is where most of the terpene loss happens if the operator rushes.

The whole point is temperature: cold enough, end to end, that the terpenes which boil off in a cured-material run never get the chance.

02

WHAT THE EQUIPMENT MUST DO

COLUMN TEMPERATURE
-60 to -70 C
Held through the whole run, not just at load. This is the number that separates live resin equipment from everything else.
COOLING METHOD
Midex chiller or liquid CO2
Systems ship on liquid CO2. A chiller is specified at purchase or retrofitted later.
MATERIAL STORAGE
-80 C
Fresh-frozen from harvest, kept frozen until it goes in the column.
ROOM
C1D1
Hydrocarbon extraction is a classified-space operation. No room, no run.
03

PICK YOUR BLEND

VAPOR PRESSURE @ 70F
SELECTIVITY
TERPENE PRESERVATION
CAUTION

Never exceed the system's MAWP by shifting the blend. Propane raises vapor pressure sharply with temperature. If you want to run a heavier propane fraction, call the shop first and we will confirm the rating.

04

ONE MACHINE, EVERY OUTPUT

SHATTER

Stable, glassy, cured on a lower-terpene fraction.

BADDER

Whipped, terpene forward, the common live resin presentation.

DIAMONDS

Slow crystallization in a sauce, highest terpene retention.

CRUDE

Feedstock for distillate, where terpene loss does not matter.

05

WHICH SYSTEM FITS

MOST COMMON
20 LB SYSTEM
~10 LB FRESH-FROZEN / RUN

ASME certified, runs live resin as built. The usual first system for an operator moving into fresh-frozen.

$160,000SPECS →
HIGHEST THROUGHPUT
40 LB DOUBLE BARREL
~20 LB FRESH-FROZEN / RUN

Two columns, so one loads while the other runs. This is the machine for a facility running fresh-frozen every day.

$350,000SPECS →

Fresh-frozen throughput runs about 50 percent of the dry rating, because water weight takes up column space. The ratings above are already corrected.

06

HYDROCARBON VS CO2, THE HONEST VERSION

If terpene-forward concentrate is the product, hydrocarbon wins on the axes below. If it is not, CO2 may be the right machine, and we will say so.

HYDROCARBON
CO2
Terpene preservation
High, the solvent works cold
Lower, heat and pressure strip volatiles
Run time
Under an hour
Most of a day
Solvent recovery
About 90 percent
Effectively closed, but slower
Room requirement
C1D1 classified space
No classified space required
Operator skill
Higher, more valves and sequence
Lower, more automated
Capital cost
Lower per pound of throughput
Higher per pound of throughput

Where CO2 is the better buy: if you cannot build or permit a C1D1 room, if flammable-solvent risk is a non-starter for your insurer, or if your product is distillate feedstock where terpene loss does not matter. CO2 is the more sensible machine in those cases, and it is not one we build. We would rather tell you that than sell you the wrong system.

Comparison reflects typical commercial hydrocarbon and supercritical CO2 practice. Exact figures vary by material, operator and configuration. Directional, not a benchmarked study.

07

QUESTIONS WE GET

Can I convert my existing system to run live resin?

Yes. Our systems ship running on liquid CO2. A chiller can be specified at purchase or retrofitted later. Most buyers start on CO2 because the chiller is a significant cost on top of the system.

So what actually makes it live resin?

The material, not the machine. The plant has to be frozen at the time of harvest. The equipment's job is holding minus 60 to minus 70 C through the run.

Do I need a different column?

No. The same column runs cured and fresh-frozen material. Throughput drops by about half on fresh-frozen because of water weight.

Is live resin training separate?

No, it is part of operator training and it runs on your material. It is only taught from day three on, so wanting live resin puts your minimum at three days. Training is billed separately from the system at $3,500 per day.

TRAINING, FROM DAY THREE

Live resin is taught from day three of operator training on: fresh-frozen handling, cold-column loading, blend selection and the purge schedule, run on your material. Training is three days minimum and five days recommended, and it is quoted separately from the system.

TRAINING PAGE →
WHAT IT COSTS TO RUN

Live resin trades throughput for price per gram. Fresh-frozen material takes up column space, so a run yields roughly half what the dry rating suggests, and the product sells for considerably more.

SEE THE SYSTEMS →