DIY CO2 Extraction?

I don’t know about ya’ll, but I have been watching CO2 Super Critical Fluid (SFE) with interest and have wanted to sample some cannabis essential oils extracted by that method, but the cost of conventional SFE equipment, is outside the range of most of our finances.

For the rest of ya’ll just learning of the process, let’s quickly examine what SFE is, by looking at what Wikipedia has to say about it, followed by our kicking off our affordable DIY CO2 extractor design project:

Supercritical carbon dioxide

From Wikipedia, the free encyclopedia

SCFE CO2supercriticalpressure






Standard carbon dioxide pressure-temperature phase diagram  from Wiki, plus another showing the droopy nose normally not shown on CO@ SCFE charts, but which can be exploited.

Supercritical carbon dioxide is a fluid state of carbon dioxide where it is held at or above its critical temperature and critical pressure.

Carbon dioxide usually behaves as a gas in air at standard temperature and pressure (STP), or as a solid called dry ice when frozen. If the temperature and pressure are both increased from STP to be at or above the critical point for carbon dioxide, it can adopt properties midway between a gas and a liquid. More specifically, it behaves as a supercritical fluid above its critical temperature (31.1 °C) and critical pressure (72.9 atm/7.39 MPa), expanding to fill its container like a gas but with a density like that of a liquid.

Supercritical CO2 is becoming an important commercial and industrial solvent due to its role in chemical extraction in addition to its low toxicity and environmental impact. The relatively low temperature of the process and the stability of CO2 also allows most compounds to be extracted with little damage or denaturing. In addition, the solubility of many extracted compounds in CO2 vary with pressure,[1]permitting selective extractions.

Soooo, in us’n layman’s terms,  we use plain old CO2, that we have gotten hotter than 31.1C/87.98F, while under at least 1086 pounds per square inch pressure.

In that state, the CO2 becomes a super solvent, which has higher penetration power, and can be fine tuned to focus in on specific constitutes, by varying the pressure, temperature, and by the use of co-solvents like ethanol or hexane.

Fair enough, and easy enough to accomplish several ways!  Traditionally a high pressure intensifier pump is used to achieve the required pressures.

Cryo-pumping also works.  You start with liquid CO2 or dry ice and heat it in an enclosed space.

My first conceptual of a system that was semi affordable, was a simple minded system using liquid CO2 and heat to run it at about 1500 PSI.  That eliminated the pumps normally used and by using a liquid Dewar with a dip tube, with both a gas head and a liquid tap, the need for any liquid pumps is eliminated as well.

It is designed to use readily available Schedule 180 austenitic stainless pipe and its largest component is small enough to fit in my 7″ X 36″ lathe.  My original plan was to use an existing hydraulic cylinder for my vessel, but alas, carbon steel embrittles excessively at cryogenic temperatures.

My design calls for achieving pressure by simply heating the pipe with available pipe band heaters.

Pressure was controlled using a conventional, though expensive back pressure regulator.  Please note the attached conceptual, which reflects my thinking four to five years ago.  I put the project on the back burner after reading the SFE CO2 patents for extracting cannabis, and noting that CO2 isn’t a very aggressive solvent and the patented processes used significant fluid exchange rates, as well as relatively long spans of time.

To compound that, reports from those testing SFE CO2 extractions reported poor taste and effects, so I put CO2 extraction on the back burner to just watch for awhile.

Within the last couple of years several folks have done some interesting work starting with dry ice.  The first that I noted was able to maintain high enough pressure in a test tube to keep dry ice from sublimating as it warmed, so as to extract some Limonene from an orange peel.

That led me to question whether super critical pressures were required to extract the essential oils from cannabis that we typically extract with other solvents, and further experiments by others suggests that it is not.  Some even report better results at subcritical pressures, especially with the use of co-solvents.

Sub critical extraction presents an interesting twist from a simplicity standpoint, so of course my simple mind immediately envisioned replacing the test tube with a pressure vessel containing dry ice in the bottom, and a basket of material suspended above it.  Screw down lid and bring it up to temperature with a pipe clamp heater for pressure.

Flooding is achieved by simply turning it upside down to soak the material and right side up to drain.  That step could be repeated back and forth, to soak the material and keep the boundary layers diminished.  On setting it upright the final time, we could bleed off the liquid into an expansion chamber and then to atmosphere, leaving behind the oil.

I have decided to build a 2″ X 24″ prototype, and have acquired two resources on this project that emboldens me.  One is the offer from a dear old friend, to allow me the use of his aerospace pressure and vacuum equipment manufacturing facilities for giggles and old times sake.

The other is an agreement with another old friend, who owns a cryogenic equipment manufacturing plant back east and is familiar with SFE.

We have a mutual engineering support agreement in effect, in exchange for my support on one of their projects with a former aerospace customer of mine, who is now their customer as well.

For my support interfacing their equipment with equipment of my own design and manufacture before retirement, they will support me in developing a simple minded DIY SFE system, that hopefully more of us’ns can afford to build, or have built.

So here is my first simple minded conceptual using liquid:

Here is my simple minded conceptual starting with dry ice:
OOPs, solly, watch this space!

After working all day on the drawing, my 2002 32 bit Auto Cad program is not able to access my printer on my 64 bit processor, and I’m not smart enough to figure it out, so I have to find a computer hero or heroine first.

The way my conceptual works, is the bottom of the cylinder is filled with dry ice , on top of which sits a wire basket of plant material.  Clamp on band heaters turn the dry ice to liquid, which is circulated and soaked through the material by simply turning the cylinder upside down.

After flipping it about a few times, over an extended soak, the vessel is set upright and attached to the lower expansion chamber via a hydraulic quick disconnect.  The liquid is bled off, decompressed, and the oil collected from the decompression vessel via the bottom drain valve, as well as via the detachable bottom.

Lu lu lu lu lu lu lu lu lu lu lu lu lu lu lu!!!!!!!!!!!!!!!!!!!!!!!!  Progress!

Well thank the Great Spirit for ex-brother in laws, who can sort out computer problems, so that I can print from virtual mode.  Hee, hee, hee, kept him at tossed the sister……….

Here is my simple minded conceptual of how such a dry ice system might work.  More detail prints once I have exercised some resources.

After further discussion with another experimenter, I have decided to build the system to operate at 5000 psi and below.  Instead of using schedule 160 stainless pipe, I will gun grill a billet of stainless, but will keep the bore at one inch.

Hi ya’ll!

Been out talking to folks running commercial CO2 SFE units and would like to share some selected excerpts from their letters, to keep their identities confidential:

Hi Graywolf, here is some pics of the unit i have been running for 8+ years. Our whole thing with this unit was to have maximum fractionation capabilities. 

The extraction vessel is rated to 10,000psi,  and made of stainless!! 

We use a basket to hold the material and I’m having a natural cloth bag made that will go into the vessel and hopefully allow me to extract 2x current volume. 

There are some great graphs around the net that show the combinations of pressure and temps and the resulting density of co2. In general high pressure (we go up to 10,000psi) works well in combination with high temps (around 100c) and lower pressure around 5000 psi goes well with about 60c. 

I tried high pressure and while i need to try again to confirm, there seemed to be some degradation to the overall quality and definitely the fragrance. the yield was higher and its much more efficient requiring less co2. 

I already noticed on the bit of extract that i dissolved in ethanol and then winterized and filtered, the flavor is no where near what it was before going in the ethanol. I plan to try and get the waxes out with only co2. 

I cant see any advantage to using either hexane or ethanol or a mixture as a co solvent?? the compounds are easily soluble in co2 and usually those types of things will help to extract more polar compounds such as chlorophyll. It all depends on what your goals are? maybe he is using that mixture to help fractionate out the waxes?? 

I can do a small run next week using those co- solvents and report back if i see anything magic or some beautiful separation. maybe he is just some chemical engineer using a method that was used for another project and he is trying to apply it there? 

It seems really counterproductive to use co solvents and contaminate a great extract… maybe he can only do really low pressure and he requires the co solvent to help the efficiency?? 

I found material with a moisture content of around 10% to be fine. I don’t know what the implications of a slight amount of carbonic acid could mean? 

I have heard it can make oils rancid, but have run vegetable oils at 10+% moisture and had them test very low in peroxide values in respect to oxidation and rancidity. I do not see any problems with around 10% moisture, the water sometimes comes out with the extract and is sitting on top and the few mls there can be poured off.

And from yet another hero!

I. Extraction was performed by sub and supercritical CO2: 

        Subcritical (liquid): 10-12 ºC @ 65-70 bar for approximately 6 hrs. 

        Supercritical (liqid/gas): 40-45 ºC @ 230 bar for approximately 4 hrs. 

II. Separation of fats and sugars, by winterization, chromatography and high speed centrifugation. 

This part was very critical in the purification schema and required analysis of both the anaylate and precipitate. 

III. Purification, at this point one has two options, Flash Chromatography or Wiped Film Evaporation (Short-path) 

I performed both and in both techniques, one can obtain purities in the range of   95-99% total THC (∆9, ∆8 and ∆6) with the purity of  ∆9 ranging anywhere from  78-98% depending on the parameters set. 

One last comment, probably the most important….. absolutely no petroleum derived hydrocarbon solvent was used. Except for the small amounts used for LC/MS analysis.  This was my driving force to see if it could actually be pulled off.


We are moving this project from research to active experimentation in our FY 2013, now that the shack and Terpenators projects are a fait accompli.  What I did in FY 2012, was simply research and develop resources.

It was good that I did, as further research put things in better perspective.

While I determined that my simple minded CO2 SCFE system would work, it raises a the bigger germane question of why is this trip necessary, given how effective BHO and some of the other extraction methods are.  Why spend the money for this more expensive fish trap, if we already have the fish?

The answer lies in that what CO2 SFE extraction shines at, is selective extraction.  By fine tuning the pressure and temperature, as well as using co-solvents, specific components may be extracted, while leaving behind everything else.

That is of less value when discussing cannabis essential oil extraction, in that it has been determined that it is the entourage effects of all the terpenes present, including the diterpene cannabinoids, that are responsible for its medicinal properties.  That however doesn’t mean that we can’t specifically focus on that list of terpenes.

The other thing that my research made clear, and  that is using one vessel to process the material and raise the pressure in, would result in extractions along the entire temperature/pressure curve.  Woops, no selectivity there, but easily solved by bringing the liquid CO2 or dry ice up to a higher temperature and pressure in a separate vessel, and then equalizing it with the one containing the plant material!  Easy, but the system complexity grows.

One of the interesting things that my research turned up during tete a tetes with brothers owning and operating commercial CO2 SCFE’s, and bumblers like myself whomping up DYI ghetto extraction equipment, is the wide range of processes that different operators have achieved a modicum of success at.

One operator simply took the valve out of a CO2 bottle and filled it with plant material and dry ice, before replacing the valve and heating the tank to SCFE ranges.  He then inverted the tank and vented the CO2 into a catch container, where it left cannabis essential oils behind.

He claimed his best success using co-solvents at ~5500 psi and that his product was superior to all competing, but alas, I was never able to sample it and his spamming got him banned from the forums where we shared information.

Commercial SCFE operators report successful sub critical products as low as 350psi, and another at 850psi, but I haven’t been able to sample their successes, to confirm my own opinion of product quality.  There in lies the rub of course, as there is no common measurement and each creator loves his creation.

Fortune has ostensibly smiled on us however, in that two of the operators that I have been conversing with, have agreed to work more closely with us and to supply confirmation samples.  Hee, hee, hee……………………………

Even simpler DIY SCFE C02 6-2-13

Hee, hee, hee, you have to admire simplicity.  Here is the system by jyndustriez which I mentioned, that simply puts the plant material in an off the shelf CO2 tank, and floods it with liquid C02 from a second off the shelf tank, before heating to achieve super critical state.

More information on how he accomplishes that at, but here are some pictures he has shared:

DIY SCFE C02 extraction-1-2DIY SCFE extraction-1-1DIY SCFE CO2 extraction-1-3


Progress!  We got to play with a donated SCFE CO2 extraction sample and were able to heat it under vacuum and observe the effects.

As received, the sample was in a “wax” hydrate form, and was not aromatic.  The flavor was mild, and the effects were good.

As it was a small sample, I was unable to winterize it to remove the waxes, but I was able to heat it to 115F, under vacuum, and observe what happened.

The sample out gassed significant CO2, even though at 115F decarboxylation was minimal, and never quite turned clear, due to the high wax content, but that isn’t unique, as BHO extracts are improved by wax removal as well.

On the surface however, the wax content seemed high, compared to our typical BHO extraction, so I look forward to a large enough sample to winterize and determine just how much.

Here is a starting and ending photo, demonstrating the ending wax content.

C02 sample-1-1C02 sample-1-2

To add to our excitement, last week we got a guided tour of Eden Labs during our recent business trip to Seattle!  What fun!!!

Patrick, one of Eden Lab’s bright new sales consultants, attended one of our BHO classes and subsequently invited us for a tour, so how could we resist, hee, hee, hee, snicker, snark, snort………………?

Always a pleasure to see how the pros from Dover do things, and I do likes the way they detail a package.

We lucked out in finding the original creator available and got our guided tour from Fritz himself.  Besides his latest creation, we got to see not only his original test sled, but some of the R&D that may make great strides someday, when Fritz can find enough time to finish them, between current product demands……….

Their latest all stainless creation was in final assembly and testing, and was capable of extracting not only with subcritical and Super critical C02, but also with refrigerants like butane and propane.

It was appointed well, and used pneumatic intensifiers both for the hydrocarbon pump, as well as the SCFE CO2 pump.

It also sported a unique closure system, which simply spins close and that greatly simplifies loading, as compared to a 12 bolt flange with a torque wrench.

The vessel itself uses a Schedule 160 stainless core, but adds water jackets, so as to permit the use of a commercial heater/chiller for temperature control.

The unit that we looked at, had a $60K base price, plus the price of the hydrocarbon extraction capabilities.  Not cheap, and more complicated that most folks should attempt at home, but if you need a machine capable of a quality extract, in commercial quantities, you will need to step up to a system of this caliber, which includes pumps to cycle the C02, and C02 recycle to recover it afterwards.

Fritz did note that one of the things on his list of thangs he is juggling, is a smaller lab sized unit, which fills the market window for a smaller unit that doesn’t recycle.  Looking forward to see what comes up there!

From a process perspective, Fritz shared that the aromatic extractions are best done at low pressures and as the pressure goes up, so does the rate of chlorophyll extraction.  Based on his and other input, I will focus on the range from 800 psi to 3500 psi.  While I’ve heard operating parameters up to 9500 psi, the lower ranges sound more believable.

As unbelievable as it may sound, ah think sometimes operators shuck me, cause they are trying to protect process secrets and lead me astray.


Lu lu lu lu lu lu lu lu lu lu lu lu lu lu lu!!!!!!!!!!!!!!!!!!!!!!!1  The Great Spirit smiled and JYNdustriez loaned us a CO2 extraction setup and will show us how to use it, when he visits to watch Dr. Fischedick’s lecture on 11-2.

I’ve also located a local brother with an Eden Lab machine, who is amenable to experimentation, so things are heating up in the area of CO2 extraction at Skunk Pharm Research.  We will have machines from both ends of the price scale to experiment with.

Sound CO2 has also extended us an invitation to visit, and they run Apeks equipment, soooo even though our CO2 project was slow getting in motion this year, it looks like it is finishing with a bang.


Hee, hee, hee, check out JYN’s latest link on DIY SCFE CO2

381 responses to this post.

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  4. Posted by AJ on June 19, 2015 at 10:55 PM

    We have an Apeks Fully Automated 20L 1500 PSI system for sale if anyone is intersted. System has less than 1000 hours on it. We bought it to lease to a company, and due to certain legal circumstances with the lessors it didn’t work out. contact if interested.


  5. I like your research and you’ve surrounded yourself with several experts. I’d be a fool not to follow through, so I was a bit surprised to see no more information about this Co2 project. Given your progress last year and of course baring any illness, I’m guessing it was ready to sell in September 2014. My question is are you now willing to sell the finished product and at what cost? Please let me know at your earliest convenience. Thank you.


    • Good point Jordon! We got buried, but are in the process of cleaning up the site and I will finish off the SCFE CO2 page.

      We don’t sell any equipment or concentrates, just do research and share the results.

      If you are looking for equipment immediately, I suggest considering Eden Labs and APEKs.


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  10. We would be interested in collaborating on several of your projects the top projects are DIY Co2 extraction and tissue culturing. We are organizing our summer interns and we usually get a lot of them.


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  12. Posted by Jordan on April 10, 2015 at 10:33 AM has a very interesting report on, Solubility in Supercritical Carbon Dioxide. Definitely worth a read.


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  14. Ive made some pretty simple C02 chambers for euthanasia in feeder rodents for our reptiles out of Co2 cartridges and a cracker with a valve attached to release into the chamber as well as some Co2 reactors for advanced planted aquariums. I’m gunna start brain storming tonight to see if any methods could apply.


  15. Posted by andrew on March 25, 2015 at 12:18 PM

    I have one of jy systems. I’m no longer using it so I would be willing to unload it. Shoot me an email.


  16. Posted by Doug on March 25, 2015 at 11:30 AM

    Do u know where can get a unit.
    Jyndustriez sites no longer good


  17. Posted by sam on March 21, 2015 at 8:15 AM

    Looking for closed loop co2 extractor in cali 4088051628


    • Posted by AJ on June 19, 2015 at 10:56 PM

      We have an Apeks Fully Automated 20L 1500 PSI system for sale if anyone is intersted. System has less than 1000 hours on it. We bought it to lease to a company, and due to certain legal circumstances with the lessors it didn’t work out. contact if interested.


  18. Posted by Ken wood on March 15, 2015 at 7:58 AM

    Love to see more


  19. Posted by Ken wood on March 14, 2015 at 4:21 PM

    We are looking for a co2 oil extractor for home use
    Smaller tube
    Could you help us with that
    Thank you so much for your help


  20. Posted by Scotty Rotten on March 3, 2015 at 5:20 PM

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  23. Does anyone have any experience with Oco Labs’ Super C Extractor? I am considering purchasing one for personal use, so any info is appreciated!


    • Love mine! Need a centurfuge to separate water. Very easy to use and extract with :-)! I’m working on increasing potency anyone following this forum I would greatly appreciate any input on CO2 extraction. Our local testing facility tested oil out at 39% in raw form.


  24. Posted by eric on February 14, 2015 at 6:12 AM

    JYNdustriez LLC, are you still making your stainless steel system for retail?


  25. Posted by pd partners on January 26, 2015 at 4:47 PM

    our company is looking into making a system using carefully chosen components.. i think we can use a 3000 psi vessel and heating control to 150 F. We will be purchasing a new CO2 pump as well. We are trying for 1 liter or so of dried plant material (in a ss basket) ..So with @20% air space for the vessel it would need to be a bit larger or we would use less size in basket? We are NOT going automatic yet…so manual valve adjustment will be the art and science of our lab. We also do not need to stir, but need the super critical CO2 to permeate the plant material. 2 liters would be better but i worry about the saturation? any advice you can give me would be appreciated also any suggestions as to flow rate
    Thank You,


  26. Posted by Retired CO2 Guy on January 16, 2015 at 7:50 AM

    Anybody who knows anything about this knows that pumping is measured in grams/minute (mass flow). If somebody is trying to sell you a system or pump with a liter/minute number – be wary that they don’t know much…I was in SC CO2 for over a decade in the 90’s & 2000’s. Not currently in the business but gurus like Profs. Taylor and King at VTU and Arkansas plus Dr. Chordia at THAR in Pittsburgh have 30+ years at this from analytical to scale-up. The higher the pressure equipment, the more options you have for more products as this moves up to food chain into a regulated environment.


    • Posted by PSI on January 16, 2015 at 8:29 AM

      Gram/minute can easily be converted into Liter/minute. It is a simple equation to change mass flow rate to volumetric flow, Liters/min or even gallons/min are easier for people to understand not only that but it is implied that in a system Volumetric flow is not concerved, and therefor deems appropriate for variable systems in which temperature and velocities change. Volumetric flow rate it NOT an incorrect way to describe flow rate. King specifically described flow rate in volumetric terms in his paper entitles Liters/min in his published paper “Supercritical CO2 Extraction of Carotene and Lutein from leaf protein concentrate” Here is some information on how the two relate, and how to do conversions of the two


  27. Posted by pam tano on January 11, 2015 at 2:22 PM

    how do you feel about using an aluminum extraction vessel for bech top CO2 extraction @ 1500 psi? and any o rings which come in contact with SCF?


    • Posted by Wayne on January 11, 2015 at 4:28 PM

      I purchased a stainless steel tube for a CO2 extractor and steel for end plugs and pins:

      Order Number: 1005903
      Amount: $450.29
      Shipping: UPS Ground
      1 piece @ $319.67/piece
      Stainless T-316/316L
      Seamless Tube
      3″ x 0.25″ x 2.5″
      Cut to: 36″
      Ships from the Toledo warehouse
      1 piece @ $95.96/piece
      Stainless T-316/316L
      Cold Finish Round
      Cut to: 10-12″ random length
      Ships from the Toledo warehouse
      1 piece @ $10.17/piece
      Stainless T-316/316L
      Cold Finish Round
      Cut to: 10-12″ random length
      Ships from the Toledo warehouse

      I will sell it all for $300.00 you pay the shipping. I am in Michigan.

      If anyone is interested email me at


  28. Posted by reidh Beallagh on January 8, 2015 at 5:44 PM

    This cool, please send me further postings on this matter.


  29. Posted by Lynn on December 23, 2014 at 10:14 PM

    We’ve experimented with Freon 123 and 134a, potential in it. Don’t know about Nitrious Oxide


  30. Posted by cplamb on December 22, 2014 at 7:55 PM

    I know extraction using Butane has been mentioned here. Has anyone tried extraction using Nitrous Oxide? I know this is done for food and would require lower pressure than CO2.


  31. Posted by Lynn on December 22, 2014 at 6:13 PM

    I’m about to purchase an Apeks Co2 extractor and have been debating wether to get the 1500PSI 5L or the higher pressure 5000PSI 5L. I’m leaning towards the higher pressure 5000PSI 5 L. I’d like any opinions on which pressure machine would be a better choice. Thanks


    • Posted by PSI on January 11, 2015 at 9:32 PM

      Did you ever buy the Apeks? I am wanting to know what your run time and yields were if you had.


    • Posted by Eric Catuccio on May 5, 2015 at 4:06 PM

      Definitely the 5000. You’ll be able to do some cannabinoids fractionation with the 5k psi.


    • Posted by AJ on June 19, 2015 at 11:00 PM

      We have an Apeks Fully Automated 20L 1500 PSI system for sale if anyone is intersted. System has less than 1000 hours on it. We bought it to lease to a company, and due to certain legal circumstances with the lessors it didn’t work out. contact if interested.


  32. Posted by MOME on December 20, 2014 at 10:18 PM

    Just wondering if those shucksters didn’t hold you down from discovering process secrets…Funny how we were just talking alcohol and low extraction temps and have merged into this area in just 72 hours ;) I guess I never considered co2 as an option due to limited funds. But in light of a strong support group now, I am exploring my options. Have you folks made any headway on these processes? I am specifically looking for methodolgy on a full plant extract to promote medicinal “entourage/synergy” properties along with de-waxing and removing water all in one fell swoop. In other words…”Would there be a possibility of a class on co2 extractions in the foreseeable future?”

    As always, thank ya


    • Sub critical and SCFE CO2 extraction have made significant inroads in the last couple of years, and we’ve done enough of our own research to appreciate the depth of the rabbit hole, but are not the experts.

      Our experiments lead us to believe that optimizing C02 extraction, requires a high C02 exchange rate, because it is a small molecule and not capable of carrying much solute individually, so it requires a lot of them.

      They also lead us to believe that achieving pressure by loading the column with room temperature liquid CO2, and adding heat, is an interesting experiment, capable of SCFE extraction, but not the fine nuances of exposing the material to specific temperature and pressure, rather than the full curve.

      Sub critical around 850 psi had a higher monoterpene yield, but the total yield sucked. We experimented using a passive system, so weren’t able to achieve super critical state cooler than ambient temperatures, which I’ve been led to believe works even better.

      As the different components in the raw oleoresin have different molecular weights and boiling points, the optimum temperature and pressure for extracting them is different, sooo in comes fractionating, arguably our ray of sunshine.

      Experiments by brothers like Patrick at Eden Labs, fractionating off the monoterpenes on one end and the pigments, chlorophyll, and plant waxes on the other, before blending back some of the monoterpenes into the concentrated diterpene cannabinoids, were eye opening.

      Not for any pristine museum quality visual appeal, but the aroma was impressive, the taste followed suite, and effects were outstanding.

      As far as post extraction processing, the raw extract has water, CO2, and plant waxes, if they weren’t fractionated off, which we didn’t.

      We had no problem removing the water and CO2 at around 115F and -29.5″ Hg vacuum. We de-waxed using conventional winterizing techniques with ethanol.


  33. I’m interested in building my own system but first want to work with a couple different setups by offering some assistance. I’m an easy going guy who’s eager to learn and develop some good connections with focused people in this business.


  34. Posted by Paradigm on November 13, 2014 at 6:27 PM
    I am opening up to the market a Dual Chamber Supercritical CO2 machine. Each chamber is 2.5 liters and it has a max pressure of 3000 psi. This is a one of a kind and pumps a whopping 7.8 L/m For more information email me.


  35. Posted by gabe on November 10, 2014 at 11:23 PM

    I am looking at a small machine a table top with a top rating of 4500psi …. I am wondering what temp and pressure will get me the most terps and cannabinoids any help is appreciated


  36. Posted by Miles Smart on October 25, 2014 at 8:33 AM

    Hello, I have a used Apeks 5L, 1500 PSI system for sale. Its been used less than 1 yr and comes with Chiller, Compressor and everything needed to begin. Please feel free to email me for details.
    As always, great site Skunk Pharm! Thanks


  37. Posted by cplamb on October 11, 2014 at 5:18 PM

    Has anyone experiment with agitation? If so, what were the results?


  38. Posted by Tom on October 7, 2014 at 2:41 PM

    Look for CO2 machine parts. Can anyone help me?


  39. Posted by drew on October 7, 2014 at 11:59 AM

    It depends on how good your material is and the amount your putting in the tank. I would run approximately 1 1/2 lbs of material about 10 times with an average of 8 grams per run.


  40. Posted by drew on October 7, 2014 at 9:46 AM

    It was about 6 lbs per soak. I would generally do a 3hr soak although I have soaked overnight. I would run different pressures and keep them separate. If I ran a lower pressure first I would get more of the terpenes. I would slowly raise the pressure with each run ending up at about 4500 psi. Then I would mix in the the with the final product. The secret to the yield was doing a slow final transfer and purging of the co2.


    • wow yeah that seems like alot of manual work and waiting for one run plus the abuse on the co2 storage tank from the transferring can’t be to good.seems dave is right w/ the liquid pumps needed to achieve the proper pressures. what where your yields like and how many soaks total with the jyn? i really had high hopes for it


    • Posted by Wayne on October 7, 2014 at 11:47 AM

      did you change your mind about selling?


  41. Build your own system it is very easy. I currently have my own 5l and 10l. Do not replicate the Jyn system it dose not work well. You need to have a liquid pump and play with different pressures. Higher pressure increases yield but lowers quality of oil by adding excess waxes. All you need to do is research pressure vessel dimensions and specs then plumb it to match the flow diagram of many other c02 systems available online. There are many flow diagrams available online that are all similar.


    • yea i was leaning more and more towards doing a diy as i can not afford a $80k eden labs which are so nice. how much did your design w/liquid co2 pumps run you? do you reclaim you co2?


    • Posted by Wayne on October 7, 2014 at 9:59 AM

      Hi Dave, can you give more info on your unit please? flow diagrams are not my strong point ;-P


    • Posted by Matthias on October 7, 2014 at 12:04 PM

      I think this is careless advice. People should not just go about trying build these unless they have technical skills. The reality is that there are risks that need to be considered when designing a pressurized system. Please if you don’t know how to read schematics and flow diagrams, or don’t have the capacity to learn,then don’t undertake the task.


      • Posted by Wayne on October 7, 2014 at 12:14 PM

        The designing of the pressurized part is not where I am concerned, I am more interested in the pumping, pressures used to get the best results, the tech details. I have a small machine shop and friends that make high pressure vessels for a living, but I know no one making Super Critical CO2 extractors ;-P


        • Posted by Paradigm on October 12, 2014 at 8:31 AM

          The problem is not finding a pressure vessel, I am speaking specifically about the whole system, you need a some back ground in order to safely design a CO2 machine at the pressures and temperatures required. Again I am not saying it can’t be done, I am saying not everyone should, it can be dangerous and if you do not understand fluid dynamics and thermodynamics then don’t take this one, unless you have some serious help.


          • Posted by Paradigm on November 11, 2014 at 10:38 PM

            I wanted to amend my last comment, and note that I was speaking of a closed loop system. It is not difficult to build an open system for CO2 extractions. However the closed loop system requires much more technical knowledge and should be done with great care.

  42. Posted by drew on October 7, 2014 at 5:10 AM

    I bought one of jy ind. Systems. It works OK but you have to run your material many times to get the full extraction. I am unable to work it anymore so I am going to sell it for half price. $1000 plus shipping. I paid a little over $2000 And upgraded to quick connects and the 5000 psi system.


  43. You have made some decent points there. I looked on the
    web for more info about thhe issue and found most people will go along with your
    views on this site.


  44. […] DIY CO2 Extraction? | Skunk Pharm Research LLC […]


  45. Posted by Matthias on September 21, 2014 at 11:13 AM

    Email me.. I may have something to offer you.


  46. Posted by brandon nelson on September 20, 2014 at 9:03 PM

    Bought the jz industries set up, could never get anything but oil. After a month j told me I needed to go above 5000 psi to get wax. Worked with it for about 6 months oil was decent for edibles but not much else. went back to bho.


    • Posted by Wayne on September 22, 2014 at 1:23 PM

      considered buying a jz industries then web site went down. started building one, what advice can you give? consider selling yours?


      • Posted by ron on October 7, 2014 at 12:26 AM

        haha same here. so i am gonna build one also. anyone still have his diy instructions?


        • Posted by Wayne on October 7, 2014 at 4:06 AM

          I have put together plans by research on the web, I have never seen a real DIY set of plans. I am concerned about Brandon’s comments. jz ind. seems to have vanished from the net, did he blow himself up? did he get sued by someone that blew them selves up? or did his system not work very well? all of his youtube video’s and you will have a good idea of what to do to male a copy of his system. the real question is how well will this system work.


          • Posted by ron on October 7, 2014 at 8:18 AM

            haha yea i was very concerned as well about his site dissaperance he’s not even answering emails any more. did u run it with heat silicon heat mats? seemed like the heat and 4000psi was the key with a 40 min soake. also how much co2 did you use per soak? think the videos said 100lbs per 8 oz material. not sure really wanted to try one out so bad as i am over butane and all the laws in CO we have with it. ran open tubes fro 1999 to 2014 w/ out any explosions or flame ups. some people just ruin all the fun

  47. Thanks for finally writing about >DIY CO2 Extraction? | Skunk Pharm Research LLC <Loved it!


  48. Love the info here. looking how this could be used in small scale hop oil production as well as other non-MJ applications. I am wondering if a Eden Lab 20L rig or larger could be used on a mobile trailer or even a box truck for mobile extraction? What would be the main concerns as far as equipment durability and operation?


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