I am completely up for discussing any and all methods for extraction using pressure in any amount and solvents of any type. foaf, did you ever test dirty LPG through a wide-bore long tube preceding the extraction tube? Advantages of supercritical CO2 extraction of essential oils include the elimination of plant waxes from the oil, the elimination of solvent residue from the oil and use of physiologically inert solvent at that, the high percentage yield obtenable, and the ability to select extracted compounds based on their solubility and mass and exclude those undesired based on the same criteria.
butane is not metabolized, if you breath in some, you breath it out. and if you burn it, you get co2 and water anyway.physiologically inert solvent
so what would one exclude, and how and why? I dont get it. if you really wanted this it would be easier to do column chromatography on bho, almost certainly cheaper, safer, and easier.the ability to select extracted compounds based on their solubility and mass and exclude those undesired based on the same criteria
CO2 becomes super critical at under 1100psi and 100F. It doesn't have to be run at 300 bars to work on cannabis because you are not trying to leach it out of the pores, but primarily off the surface.
A 1500 psi system could be run in 300 series stainless schedule 160 pipe. End plugs like pistons with PTFE O-rings would seal the vessel while allowing quick access for cleaning and could be easily contained in a simple yoke under pressure.
I have designed a conceptual system that uses a Dewar of liquid C02 with a siphon tube. You pre-pressurize the chamber to 150 psi so that the liquid doesn't turn to dry ice when it is injected, and then use the remaining 100psi differential to force the liquid CO2 into the reaction chamber.
At that point, if you heat the reaction chamber, the C02 expands and gives you the 1500 psi needed, with a back pressure limiter venting everything above that.
Once the critical pressure and temperature are reached, the heat is turned off and the chamber vented through a stellite seated metering valve into an evaporation chamber, where the oil is deposited.
A 50 gallon Dewar of liquid C02 was $115 US last time I checked, making a cryopumped system damn cheap compareds to the pumps and refrigeration used in a typical C02 unit used to extract vegetable oil. The number of runs you would get would depend on your vessel size, but the 4" Diameter X 24" vessel that I had in mind would require less than a gallon per cycle.
I converted my simple minded AutoCad conceptual to PDF and a copy is attached:
Gray Wolf
i tink he's right, your wasting your time....
BHO has tested at 98-99% THC according to Cannabis Culture and PAul Hornby, so why not just fucx with that and leave the co2 for the plants to breathe