Explore the Pros and Cons of CO2 Extraction Method vs Ethanol Extraction
What is the Best Extraction Technique: CO2 extraction method or ethanol extraction?
There are many different methods of extracting cannabidiol (CBD) or tetrahydrocannabinol (THC) and other cannabinoids from biomass. Each extraction method uses a different solvent to pull oils out of the biomass. While each method carries its pros and cons, supercritical CO2 extraction has emerged as the leader for demanding customers while driving high throughput and low operating costs, with the best quality, purity, and consistency oils produced. The following table compares the pros and cons of CO2 extraction method and ethanol extraction methods:
Table 1. Comparison of Solvent and CO2 Extraction Techniques
Parameter 245047_8de36d-90> |
Ethanol Extraction 245047_42675f-9d> |
Supercritical CO2 Extraction 245047_2948b3-ac> |
---|---|---|
Organic Oil 245047_0ef426-50> |
Organic ethanol required.1 245047_90f03c-d3> |
No special requirements, approved organic solvent.1 245047_461897-1b> |
Cannabinoid Recovery 245047_9649b9-1e> |
50-80% typical cannabinoid recovery including carbon scrubbing. Method may require carbon to remove chlorophyll. Carbon absorbs THC and CBD which lowers recovery. Carbon is a high cost consumable. 245047_a3793a-ad> |
85-95% typical cannabinoid recovery. No carbon required. 245047_1d53b0-5d> |
Solvent Recovery 245047_356119-d7> |
Ethanol is expensive and therefore needs to be recovered. Typically, 90-95% recovery of ethanol leads to high operating costs. Losses come from ethanol remaining in biomass and in the extract. 245047_3ef141-d6> |
No need to recover CO2 other than recycling within a run or batch due to low expense of CO2. 245047_29725a-dd> |
Reuse of Extracted Biomass 245047_91a391-2c> |
Biomass extracted with ethanol is hazardous waste until the ethanol is removed to negligible levels, may be flammable and/or toxic due to type of ethanol used. 2,3 Transportation is typically regulated. 245047_b2e03b-cf> |
Biomass extracted is clean and is a source of food grade essential amino acids. Transportation is not regulated. 245047_9dd885-18> |
Winterization 245047_8e04b2-d2> |
Winterization may be avoided if extraction is at < -20oC leading to high energy expense. Warm ethanol extractions need to be winterized. 245047_ccdf0d-38> |
Winterization may be avoided with subcritical extraction. However, extraction is much slower at low pressure. 245047_948f1e-31> |
Safety 245047_7c472a-c8> |
Significant fire hazard risk for indoor deployment.4 245047_3e2212-ab> |
Inert. No fire hazard risk.5, Static and asphyxiation risks are mitigated with proper install. 245047_7c700a-df> |
Infrastructure Cost & Requirements 245047_52e127-02> |
High cost for hazardous building occupancy and special room classifications and limitations.4,a 245047_92ba44-fd> |
Minimal requirements. May operate in industrial building (F2) classification.4 245047_0f2c45-e1> |
Equipment Cost 245047_a2ac55-a2> |
$2-3M USD for 1 ton per day 245047_102fd2-35> |
$3-4M USD for 1 ton per day 245047_f7389b-30> |
Operating Cost 245047_ef9cb5-4e> |
High variable costs and overhead due to ethanol cost, losses of ethanol, consumables, reduced recovery, high insurance premiums, hazardous waste disposal, and energy costs. 245047_3cf76a-51> |
Very low variable cost for CO2. No difficulty getting business insurance. 245047_fbd639-0a> |
Scalability 245047_587605-17> |
Scalable easily to 10 tons per day in less than 450 m2 with hazardous (H2,3) occupancy, with about ~7000 amps, 230V, 3 phase cooling capacity and C1D2 special rooms.6 245047_b84787-ba> |
Scalable easily to 10 tons per day in less than 450 m2 in F occupancy with ~2400 amps 230V 3 phase. 245047_6b5a5c-1e> |
Solvent Sourced Cross Contamination Risk 245047_709394-6a> |
Herbicide, pesticide, solvent contamination, extraction byproduct contamination and build up risk.b 245047_8b108a-91> |
CO2 is not generally used across lots. No risk of cross contamination. 245047_5679b4-bb> |
Solvent Sourced Cross Contamination Risk 245047_9f24bd-38> |
Herbicide, pesticide, solvent contamination, extraction byproduct contamination and build up risk.b 245047_2449e6-eb> |
CO2 is not generally used across lots. No risk of cross contamination. 245047_ecc24b-f0> |
Cost of Solvents 245047_bb718f-80> |
Food grade ethanol is safest and comes little to no chemical contamination risk but with higher cost. Specially denatured solvents are less expensive but carry a myriad of non-food grade contaminants.7 245047_ccb917-19> |
Low price per kg. 245047_d9f761-5d> |
Terpenes for full spectrum flavor and aroma 245047_d413e7-fc> |
Lost during processing. 245047_01d9b6-46> |
Harvested during processing. 245047_ad22e2-1c> |
Environment 245047_fb0a2b-68> |
High carbon footprint to produce ethanol, tons of cooling capacity needed to cool to <20oC, and dispose of hazardous biomass waste after processing. 245047_b7f3c6-5d> |
Byproduct of existing industrial processes, non toxic, non eco toxic, renewable, recaptured.8 Considered a green solvent by the American Chemical Society. 245047_1eb319-ec> |
- Limits on the amount and storage of flammable solvents in addition to specific alarm lights and deflagration alarms and detectors, emergency phones and alarm systems with 24-hour third party monitoring, alarm levers every 150 ft, setbacks from property lines or other adjacent occupants, automatic and special sprinkler systems, fire distance offsets, deratings on maximum solvent volume for multi-story, emergency power for vents, fail safe electrical systems, spark proof venting, certified equipment for hazardous locations, and explosion control plans.4,9The use of CO2 as an extraction solvent does not require any of this infrastructure since there is no limitation on the amount of CO2 a factory can have on site.4
- Most importantly, ethanol derived chemical contaminants10that remain in the extracted oil after removal of the ethanol, may increase the risk of safety and health for the consumer. For example, some of the residual contaminants listed in the specially denatured ethanol recipes have a higher boiling point compared to ethanol and are not removed from the oil during distillation. Furthermore, solvent analysis for contaminants are not always included in a typical certificate of analysis.
The table shows that in terms of every factor except capital equipment cost, CO2 extraction method has advantages over ethanol as the extraction method. Taken collectively, CO2 extraction as a method leads to DRASTICALLY lower operating costs.
It’s All About Operating Costs
The following table shows why CO2 is such an attractive business proposition compared to ethanol technology.
Table 2. Estimated Difference in Solvent Cost for a 1 ton per day Ethanol and CO2 system.
245047_3b415e-ee> |
Ethanol 245047_3fe3d6-67> |
CO2 245047_0c0a53-6a> |
---|---|---|
Approximate Equipment Cost 245047_eb1685-3b> |
$2,000,000 245047_467664-d1> |
$4,000,000 245047_2ffb70-e7> |
Required Solvent Start-Up Cost 245047_5f4b9b-f6> |
$7,000 245047_d085a9-a6> |
$500 245047_756ea1-86> |
Solvent Loss Cost per Day 245047_077482-65> |
$3,500 245047_225f55-1b> |
$115 245047_0e8c3b-c2> |
COMPARISON 245047_3a933c-73> | 245047_835a71-82> | 245047_928a50-ad> |
1 Year Solvent Loss Cost 245047_cd7033-8f> |
$1,260,000 245047_4fb203-8b> |
$42,048 245047_b14e1e-69> |
10 Year Solvent Loss Cost 245047_f720a9-18> |
$12,260,000 245047_f89f22-ca> |
$340,000 245047_84bd2f-9d> |
- Biomass throughput is 1 ton per day processing to distillate.
- All costs are approximate and in USD.
- Costs of infrastructure, biomass disposal, revalidation costs, and energy are neglected in the analysis.
- 5% ethanol lost per day at 1 gallon ethanol/lb of biomass extraction ratio. Assume no carbon or filters are used.
- Cost $35/gallon for food grade ethanol. Reduce figures to $12/gallon for denatured ethanol. Does not include shipping.
- Cost of CO2 in bulk delivered is about $0.04/lb.
With the highest cannabinoid recovery levels and low operating costs, CO2 extraction is usually the best choice for your manufacturing equipment foundation to serve multiple market segments.
Related Post:
- REFERENCES:
- Guidance & Instructions for Accredited Certifying Agents & Certified Operations | Agricultural Marketing Service https://www.ams.usda.gov/rules-regulations/organic/handbook (accessed Dec 8, 2019).
- eCFR — Code of Federal Regulations- EPA Hazardous Waste https://www.ecfr.gov/cgi-bin/retrieveECFR?gp=&SID=c94567294dff611654af7a3944a91d69&mc=true&r=PART&n=pt40.28.261#sp40.28.261.c (accessed Dec 15, 2019).
- Hazardous Waste from Cannabis Extraction – Extraction Magazine https://extractionmagazine.com/2019/08/14/hazardous-waste-from-cannabis-extraction/ (accessed Dec 15, 2019).
- Chapter 3: Use and Occupancy Classification, Building Code 2015 of Utah | UpCodes https://up.codes/viewer/utah/ibc-2015/chapter/3/use-and-occupancy-classification#3 (accessed Dec 8, 2019).
- CGA P-1-2015 – Standard for Safe Handling of Compressed Gases in Containers – 12th Edition https://webstore.ansi.org/standards/cga/cga2015-1531002?gclid=CjwKCAiA27LvBRB0EiwAPc8XWflJxH6MAC74YxV5upUoi5lt6OakcaPK5L_mu7CrSSu5CMXTjcG9mxoCrikQAvD_BwE (accessed Dec 8, 2019).
- 2006 International Building Code https://www.optasoft.com/applications/codes/2006IBC/HTMLHelp/414.htm (accessed Dec 8, 2019).
- eCFR — Code of Federal Regulations- TTB Alcohol and Rules for Specially Denatured Alcohol https://www.ecfr.gov/cgi-bin/text-idx?c=ecfr&sid=fc3be5d2e97afdd4aed5fb7b5c26309c&rgn=div5&view=text&node=27:1.0.1.1.17&idno=27#se27.1.21_1112 (accessed Dec 8, 2019).
- Brunner, G. Applications of Supercritical Fluids. Annu. Rev. Chem. Biomol. Eng. 2010, 1 (1), 321–342. https://doi.org/10.1146/annurev-chembioeng-073009-101311.
- Chapter 9: Fire Protection Systems, Building Code 2015 of Utah | UpCodes https://up.codes/viewer/utah/ibc-2015/chapter/9/fire-protection-systems#903 (accessed Dec 8, 2019).
- eCFR — Code of Federal Regulations https://www.ecfr.gov/cgi-bin/text-idx?c=ecfr&sid=3f34f4c22f9aa8e6d9864cc2683cea02&tpl=/ecfrbrowse/Title07/7cfr205_main_02.tpl (accessed Dec 8, 2019).