With Infinity Supercritical Process Up to 20 lbs (trim) to 40 lbs (bud) per day or 140-280 lbs per week Input: 10L CO2 System for Cannabis Oil and Hemp Oil Extraction Processing

Infinity is offering a 10L system which can process around up to 40 lbs per day of botanicals.

Infinity is also the first to offer a 10L system for $5,000 per month subscription.

Please visit our website for more information: Infinity 10L Subscription Special







With Infinity Supercritical Process Up to 200 lbs per day or 1,400 lbs per week Input: 100L CO2 System for Cannabis Oil and Hemp Oil Extraction Processing

Infinity is offering a 100L system (10 x 10L) at a special discount price which can process around 200 lbs per day of botanicals.

Infinity is also the first to offer a 10L system for $5,000 per month subscription.

Please visit our website for more information: Infinity 10L Subscription Special







Supercritical Carbon Dioxide Extraction of Cannabinoids from Cannabis Sativa

PDF Link to Review: 20170714-infinity-supercritical-sco2-science-review

SEATTLE, WA  July 2017 (Infinity Supercritical Staff Article Review)

Supercritical fluid extraction with CO2 is already used on a large scale for botanical extraction due to its low cost, generally safe nature, and well known properties.

Reference science pdf article: Rovetto, Laura J., and Niccolo V. Aieta. Supercritical carbon dioxide extraction of cannabinoids from Cannabis sativa L.  The Journal of Supercritical Fluids (2017)

Supercritical (SC) CO2 properties, like density, and thus solvent power, change with temperature and pressure allowing for selectivity via tuning.

One can also use more polar co-solvents, like ethanol, to expand the extraction range of the low-polarity CO2 to include more polar components.

Previous research has shown two different optimal extraction parameters with SFE for terpenes and cannabinoids.

This study did not find a significant difference in extraction rate from 313-333 Kelvin (104- 140 F).
During the extraction time (during the linear trend before exhaustion), a yield of 0.00243g of extract/g of CO2, 0.00455g of extract/g of CO2, and 0.00666g of extract/g of CO2 was found for 17 MPa, 24 MPa, and 34 MPa respectively at 328K. 16.63 percent THC plant potency.

At 34 MPa, 0.0066g of extract/g of CO2, 0.01361g of extract/g of CO2, 0.00431g of extract/g of feed, and 0.00186g of extract/g of feed for the potencies 16.63 percent, 14.03 percent, 10.11 percent and 6.05 percent THC cannabis respectively.

Comparing using SC CO2 at 328K between 17, 24, and 34 MPa, the higher the pressure, the higher the yield, but lower the THC potency of the final mixture. 7.4 percent, 17.2 percent, 18.5 percent extract yield in comparison to total start weight; 76.23 percent, 70.63 percent, 69.41 percent THC potency for over 2 hours. 16.63 percent THC potency starting material and S/F ratios of 50 for high pressures, 100 for low.

At these temperature and pressures, partial decarboxylation takes place on the THCA to THC.

Higher Pressure = Lower Potency

They used a multi-stage depressurization chillers to precipitate the extract. Most of theTHC (and highest extract amount) was found in the first stage at 13 MPa (1,885 psi) and 328K (130 F), but was waxy, pasty, and darker in color. In the second and third separator MPa (1,305 psi) and 328K (130 F) and MPa (870 psi) and 298K (77 F), more fluid yellow color extract appeared.

Compared different potency cannabis (A 16.63 percent, B 14.03 percent, C 10.11 percent, and D 6.05 percent), leading to potencies of extract of A 69.41 percent, B 61.21 percent, C 57.86 percent, and D 56.06 percent total THC. Thus the more originally potent, the more potent the extract.

Extraction efficiency (in relation to THC) rises slightly as potencies decreases (A 89.89 percent, B 89.17 percent, C 90.31 percent, D 92.23 percent).

Extraction efficiency increases as potency decreases.

They attempted to use ethanol as a co- solvents. This would cause more additional process steps, unless you want to use winterization, in which case it does not heavily modify your process line.

No major difference between using 5 percent and 10 percent ethanol by weight in extraction, but noticeable decrease dropping to 2.5 percent. Thus 5 percent is an efficient amount of co-solvents. (328K 131 F, 34 MPa 4,931 psi, S/F 20)

If ethanol is used, use 5 percent.

With the conditions in 12, the plant material was exhausted within 50 minutes of extraction.

Ethanol pulses versus constant flow was compared and pulses either performed better, or the same as constant flow. (2 hour extraction, 5 percent by weight ethanol divided into 3 pulses at 0 minutes, 50 minutes and 110 minutes.)

Since plant material was at exhaustion by the 50 minute mark, only the first pulse was needed to be applied, meaning minimal ethanol is necessary.

Ethanol drastically decreases the SF ratio necessary for lower potencies cannabis to be extracted (only 60 percent of the mass of extract gained using ethanol achieved at 2 hours, compared to the 100 percent gained in 50 minutes).

Something not mentioned in the article, the residual THC in the exhausted plant material is about the same for the lower potency cannabis, implying that the 2 hour extraction extracts all the THC and the extra mass accumulated with the ethanol comes from additional cannabinoids.


  1. Higher Pressure = Lower Potency

2. Extraction efficiency increases as potency decreases.

3. Ethanol cosolvent increases extraction, optimized at 5 percent ethanol added.

4. Pulsing performs better than constant flow.






Botanical Oil Extraction War of the Solvents

Which solvent is best ? Research and you decide.

BHO and Ethanol Solvent

 Hydrocarbons (such as Butane or BHO) and Ethanol are cheap solvents, that can degrade terpenes, nutraceuticals, and extract non-desirable components that require a great deal more post-processing. Both are highly flammable and explosive. So much, that specially designed blast rooms are required for code, and are outlawed in some areas. BHO specifically, can leave residues, which if are not properly removed during distillation, can result in nose-burn or heart aches (Google – butane in the bloodstream or dangers of butaneingestion for more info). If not properly processed, BHO only has a shelf-life of a few weeks. Reference: Human Toxicity of Butane

 CO2 Solvent

 CO2 is one of the preferred solvents for botanical extraction, which can better target oil (minimize wax and other undesirable extractions which need to be post-processed removed). It has a relatively unlimited shelf life if properly prepared. With proper extraction technique, CO2 can preserve both terpenes and nutraceuticals.

Organic Extraction Using Water

Using water as the botanical oil extraction method is the holy-grail of methods, since it does not require high-pressure gas containment, and uses one of the most abundant elements available, water.

 An additional benefit is that it is a organic process, can be continuous feed, and smaller footprint with less overall equipment costs in large processing operations. 

Currently there is only one manufacturer that builds the SDR (Spinning Disc Reactor) for this method of botanical oil extraction, Infinity Supercritical.


Infinity Supercritical Offers CO2 Extraction System Sales Distributorships For Cannabis and Hemp Equipment Sales

Distributorships Available For CO2 Extraction Systems for Cannabis and Hemp Industry

 If you are considering entering the equipment side of the botanicals cannabis or hemp industry, we are now making available a distributor opportunity. This allows you to license a territory for a prepaid distributor fee (on a yearly basis).

  • Any internet direct sales from Infinity Supercritical shipped to that state or territory automatically earn you 10 percent.  
  • Sales commissions are 10 percent from sales you bring in for your state or territory.  
  • As a distributor, you can also buy at a preset price, then set your own pricing. 

 Yearly State and Territory Distributor Fees Paid in Advance: 

  • California  $250,000 per year
  • Washington $25,000 per year
  • Colorado $50,000 per year
  • Oregon $25,000 per year
  • New Mexico $10,000 per year
  • Nevada $10,000 per year
  • Arizona $10,000 per year
  • Midwest $100,000 per year
  • East Coast $500,000 per year
  • South (all states which border Gulf of Mexico) $50,000 per year
  • Europe $500,000 per year
  • Asia $500,000 per year
  • Latin America (Caribbean, Central America, South America) $500,000 per year

 If you are interested in a distributorship, please visit Infinity Supercritical, or  email: greg@infinitysupercritical.com

Cannabis Oil Production For Profit

PDF Download: 20170302-infinity-supercritical-cannabis-oil-for-profit

Cannabis sweeps the nation

As the Cannabis revolution swings across America, states going legal are raking in huge tax revenue, and citizens are finally getting access to medical and recreational benefits of Cannabis production. The momentum is slowing moving towards oil (concentrates) which provide easier access to deliver the benefits via vape pens, edibles, and concentrates for medical purposes (CBD’s). With the political aspects aside, this review will list the aspects of producing Cannabis oil for profit.

Using a Infinity Supercritical 10L CO2 Extraction System is a good starting point for a oil refining business.


Supply versus demand

The mystique of the Cannabis industry has lots of people jumping into the mix, without knowledge of running a business, or the nuances of running a business to make money. A few are becoming millionaires, but most are breaking even, or losing money. Just look at the number of licenses issued in Colorado, and how supply has effected pricing. Business Insider reports that the price of wholesale marijuana has dropped by half in about a year.


Plan a startup strategy

What differentiates those making money, and those losing money ?

Those who make money set out with a plan, a budget, funding, and a team to deliver that plan. If you set out with detailed goals and a strategy, you’re already ahead of most of the groups in the industry. Failure to plan, is a plan for failure.

You need to have a startup plan, growth, and exit plan. If you plan and play your cards right, you’ll end up with a successful business.

Information is paramount to profit

In the planning stages, it’s critical to become informed. Read, research, inquire, and educate yourself about what you are getting into.

Read: Study online information.

Research: Online studies, scientific research papers, pricing models and consumer demand.

Inquire: Existing successful operations, and those that are not, and why they are not.

Educate: Sometimes the key to success is a very fine line, stack the deck in your favor.



Determine your business path to success

Select the part of the industry, that interests you the most, and makes the most money.

While this may be easier said than done, select a industry segment that you will enjoy working in, and develop it.

If you are vertically integrated, and have lots of funding, you can run an entire operation from cultivation to retail sales. The savvy types will focus on one targeted segment and make money with that segment, then grow by acquisition.


Start with oil extraction

Who makes the most money in the oil industry ? When compared to the hydrocarbon oil industry, it is the refiners.


In the Cannabis industry, the most value-added is extracting and refining the botanical oil.



Why is Cannabis oil extraction potentially the most profitable and least vulnerable to industry pitfalls ?

While supply and demand will ultimately determine overall industry income, as a Cannabis oil refinery lab (including post processing), you have the flexibility to determine downstream products. With a extraction system, you can make live resin, vape pens, concentrates, shatter, etc. And like other industries, you can tailor the output according to the market demand. Cultivators and retails do not have such flexibility. The ability to morph according to customer demand is an important factor to profitability.

What is the best method of cultivation of Cannabis to make a methodical profit ?

The best profit model would be a indoor grow, with staggered starting and harvest cycles, on a weekly basis. This will not only utilize your energy, personnel, and extraction lab more efficiently, but also allows you to tailor downstream product offerings to consumer demand, while providing a fresh product at all times. While outdoor grows are great, they are only once a year. The stress at harvest season is tremendous, and all that supply drives prices down, at that time of year.

FogPonics is the best kept secret in the Cannabis industry

Developed by a LA entrepreneur, the vertical grow tower system provides a weekly harvest, optimizing energy, personnel, and production specifically targeting oil production. On a five week grow out cycle, FogPonics is designed for oil production with fast growth varieties like Cinderella.


Oil extraction and post production

As oil is extracted from botanicals, the end product is a substance commonly referred to as crude oil. While this material can be used for dabs, it is more likely to go into post processing for refining downstream into concentrates or other products. It is typical for a extraction system to have a complimentary post processing lab, to refine and separate the oil for consumer products.


Strategy for success

Determining your actual business model will depend on your goals and the market in your area, but we recommend the following:

1. Start a extraction facility with post-processing lab.

2. If supply is an issue, vertically integrate with a FogPonics vertical grow facility.

3. Tailor your output products to demand.

4. Start or acquire your own vape pen brand, or develop products with your concentrates.

ROI App: http://www.infinitysupercritical.com/roi.html


Cannabis and Hemp Extractor Machines Build Your Own Brand Licensing

Infinity Supercritical is now offering the Build Your Own Brand licensing opportunity.

If you have a machine shop, or would like to brand your own Supercritical CO2 Fluid Extraction System for botanicals, Infinity is offering the following:

  • 10L Plans and Parts List
  • ASME Engineer Peer Reviewed and Proven System
  • Closed Loop and Certified in CA, AZ, NV, WA, OR, and CO
  • Machine Your Parts or Purchase Parts From Infinity and Assemble at your location
  • Enter into the Manufacturing Equipment side of Cannabis Industry
  • Typical Research and Development for this type of Equipment exceeds $1 Million
  • Typical Development and Testing Time for New Systems is about 2 years
  • Licensing Technology gives you Instant Access to Industry Sales
  • Optional Drop Ship from our Shop – You Sell and we Build and Ship
  • One Time Fee
  • Market with Infinity Supercritical Inside – Brand Recognition
  • With payment you can start building or selling immediately


With the Build Your Own Brand licensing opportunity, you can customize the frame design and colors. The Infinity frame is completely modular and bolt-together for rapid reconfiguration.


Modular Frame: Our Caster Beam frame allows you to configure your extraction equipment in many ways.


Machining Parts: We can provide you with all the parts, or custom make parts for your system with our Vertical Milling Machine or our Omax Waterjet. We’ve already made the huge investment in the machines, now you have the opportunity to use them for your business.



Quality Extracts: The Infinity Supercritical extraction system can provide extractions from any botanicals and provides a superior product.

Web Page Design and SEO Optimization: You can buy a page on our website, or build your own website to advertising your product. We also have a page optimizing SEO algorithm using Filemaker Database which can point tens of thousands of page links to your site.

Contact: greg@infinitysupercritical.com

Starting a Cannabis Business | Access for Women | Startup | Business Plan

Infinity Supercritical LLC

Email: greg@infinitysupercritical.com

Cannabis Search Engine Series Starting a Cannabis Business

PDF Publications Search Engine This real-time PDF document search/retrieve search engine forms dynamic search engine lists and results using Filemaker.  Search engine displays results with both text and a image field of the .pdf page.

Search Complete. Starting a Cannabis Business search was updated in real-time via Filemaker on:

November 16, 2016

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Sustainable Production of Cannabinoids with Supercritical Carbon Dioxide Technologies

PDF Review: 20170815-infinity-supercritical-co2-cannabinoids-review

Source: https://repository.tudelft. nl/islandora/object/uuid%3Ac1b4471f-ea42 -47cb-a230-5555d268fb4c
Title: Sustainable Production of Cannabinoids with Supercritical Carbon Dioxide Technologies

ISBN: 9789085707301

The goal of this thesis was to develop an alternative extraction method of natural compounds of interest from plant material. In specific, the goal was to avoid using organic solvents as much as possible due to residual solvents problems, low selectivity, high energy consumption, and environmental worries.

The alternative method consists of using supercritical fluid CO2 to extract compounds from plant material. There are numerous advantages to doing SFE with CO2, including CO2 being nonflammable, relatively inert, inexpensive, the ease of removal of the solvent, the plant material being non- hazardous afterwards, the different solubility of compounds depending on the temperature and pressure of the fluid, and low critical temperature allowing for extraction of heat- sensitive materials without damage.
The downsides to using CO2 include it not being a great solvent for larger polar molecules and requiring the stream to always be under high pressure which lead to higher initial investment costs. The higher initial investment costs can be outweighed though by how cheap CO2 is and the fewer steps needed for purification.  The focus of the thesis is on the separation of phytocannabinoids (or cannabinoids found in the cannabis plant) from the plant material. There are over 60 different phytocannabinoids with the most commons ones being (-)-D9- tetrahydrocannabinol (D9- THC), cannabidiol (CBD), cannabinol (CBN), cannabichromene CBC), cannabigerol (CBG) and tetrahydrocannabivarin (THCV). This study will focus on D9-THC, CBN, CBD, and CBG. Each of these compounds have their own medicinal effects, from pain relief and nausea relief with D9- THC, a sedative effect with CBN, convulsion, anxiety, and inflammation relief with CBD, and analgesic and anti-inflammatory effects with CBG.

The isolation of these compounds from the plant material is of high interest due to the drawbacks of smoking cannabis and different medicinal effects of each compound.

The production method proposed for cannabinoids with purities higher than 95% involves a pre- treatment step, where the acid forms of the cannabinoids are changed to the neutral ones due to better solubility, extraction using SFE with CO2, winterization of the extract to remove waxes, and then purification through centrifugal partition chromatography (CPC).

The cannabis plant strain used in this thesis is Bedrocan which contains around 18% D9- THC and less than 1% of other cannabinoids, thus the main focus will be on extraction of the D9-THC. CBN can be obtained through specific storage conditions to degrade the D9-THC into CBN. CBD and CBG can be obtained using the same process on different cannabis strains with higher concentrations of other cannabinoids.

CO2 becomes a supercritical fluid at temperatures higher than 31.1 degrees C and pressures higher than 1070 psi. This means that the CO2 can only be described as a fluid as it is indistinguishable between a gas or liquid. This is important because it allows for the tuning of the solvent. By changing the pressure or temperature supercritical CO2 can become more or less liquid-like with increasing or decreasing solvency power. CPC is similar to other chromatography techniques. It uses two immiscible liquid phases and uses a centrifugal field to force the mobile phase through the stationary phase.

Each compound has different interactions with these liquids and thus migrate through the phases at different speeds. Thus, they can be collected at the end of the column in relatively pure amounts. Decarboxylation of D -9-THC is necessary due to the acidic form found in the cannabis plant. Usually this occurs during combustion when smoking the plant, but when it comes to medicinal products it will likely need to be transformed without this step. The usual method for large scale decarboxylation involves organic solvents, basic aqueous solutions, and lots of energy, thus alternatives are preferred. One alternative is to pre-treat the cannabis plant before extraction.

When heating the plant material between 90 and 140 degrees C, the decarboxylation reaction from D9- THCA to its neutral form happens at near 100% selectivity. Since the process happens in a solid-state reaction, which leads to a catalytic process, the process could be estimated with a pseudo first order process. This reaction tends to happen at a lower activation energy than normally assumed possibly due to aliphatic and aromatic acids present as other plant constituents in cannabis. While adding strong acids seem to encourage this reaction and could decrease the activation energy, it causes toxic waste from the process which may be bad for other compounds of interest.

The solubility of D9-THC in supercritical CO2 was found for different temperatures and pressures. Below 1914 psi and 40 degrees C, the solubility could not accurately be recorded due to low solubility. In general, the solubility increases with pressure at all temperatures. At about 2175 psi, the solubility is found to decrease with increasing temperature, and above that pressure the solubility is found to increase with increasing temperature.

Some experimental values for D9-THC in supercritical CO2 from the data collected. At 42 degrees C, changing the pressure from 1914 psi to 3640 psi increased the solubility from by 4 times (0.20 to 0.83). At 54 degrees C, changing the pressure from 2030 psi to 3408 psi increased the solubility by around 6 times (0.33 to 1.99). At 61 degrees C, changing the pressure from 1987 psi to 3190 psi increased the solubility increased the solubility by about 7.3 times (0.32 to 2.33). At 72 degrees C, changing the pressure from 2117 psi to 3190 psi increased the solubility about 3 times (0.98 to 2.95).

At most of the temperatures and pressures evaluated in this study the constants created a good predictability for the solubility. The exception being at above 72 degrees C and low pressures.

The solubility of CBN in supercritical CO2 was found for different temperatures and pressures. In general, the solubility increases with pressure at all temperatures, but not as much as with D9-THC. Interestingly, the highest solubility was found at 53 degrees C.

The article concludes that CBN solubility in supercritical CO2 is different enough from D -9-THC that they could be extracted separately to isolate both compounds. This would include a two step extraction, there the plant material is first extracted at 53 degrees C and 1885 psi for CBN and then 2900 psi at the same temperature for D-9-THC.

The solubility of CBG in supercritical CO2 was found for different temperatures and pressures. In general, the solubility increases with pressure at all temperatures, but by a much less magnitude than the D9-THC. Also, the highest solubility was found at the highest temperature.

The article concludes that the solubility trends for CBG are similar to D9-THC, but the actual values are different enough between the two to extract them separately or through fractionation.

The solubility of CBD in supercritical CO2 was found for different temperatures and pressures. In general, the solubility increases with pressure at all temperatures. The difference in solubility between pressures is similar to CBN. Interestingly, the highest solubility occurs at 53 degrees C, like CBN.

The article concludes that CBD’s solubility trends are more similar to CBN and that they are different enough to D9-THC to be extracted separately.

When comparing all four cannabinoids, the difference in solubility can come from a couple things. This includes their melting point (with solid cannabinoids showing better solubility than liquid ones) and their chemical structures (due to CO2 having a higher affinity for non-polar compounds). Overall, CBN has the highest solubility in supercritical CO2. All of the solubility of the different cannabinoids in supercritical CO2 is on the order of 1-2g per kg of CO2 which place them at high enough for SFE.

An example is described to show how one could extract the majority of D-9-THC without other cannabinoids. In a cannabis plant containing 5% D9-THC and 6% CBD (Bediol strain), a first step extraction at ~1885 psi and 42 degrees C would extract 26 percentage of the THC and all of the CBD.

While the CBD would need to be purified, a large amount of the THC could be collected at very pure amounts using this step extraction method.

It was determined that particle size distribution of the plant material had little influence on extraction yields, and thus weren’t investigated.

The highest total yield (extract weight divided by starting weight) was 23.3 percentage and was found at the highest pressure and lowest temperature, 3335 psi and 40 degrees C respectively. This didn’t vary much from the differences in pressure, with 21 percentage being achieved as low as 2175 psi and is believed to be because the extraction was already being ran to completion. This was at flow rates of CO2 of 6 kg per hour for 3 hours. In terms of THC yield, the best yield was found at lower temperatures (40 degrees C).

In terms of time for extraction (at 2610 psi and 6 kg per hour of CO2), the maximum D9- THC yield was found at around 3.75 hours at 40 degrees C. This yield was 98 percentage. Compared to at 50 degrees C, where the maximum yield was reached at about 1.5 hours, however a maximum yield of 74 percentage is reached. During the extraction time, the D9-THC yield increases linearly in time at the same rate between the two temperatures. In comparison to hexane extraction, the D9-THC yields are about the same (85.3 percentage for CO2 and 85.9 percentage for hexane). The other cannabinoid yields were slightly higher with CO2.

The other cannabinoids were found to have the highest yields at 40 degrees C when varying temperature at 2610 psi. All three other cannabinoid yields decrease with increasing pressure at 40 degrees C, while D9-THC’s yield was stable over pressure ranges. This implies that the two step extraction method at 40 degrees C (first at 2175 psi and then at 2900 psi) could first extract the other cannabinoids and then extract the D9-THC, allowing for a more pure extract of D9-THC. This is consistent with what was stated before.

A winterization step could be avoided to remove waxes by having a two stage separator, where the CO2 to decompressed to a medium pressure to precipitate the waxes, followed by another decompression step to recover the cannabinoids. The exact temperatures and pressures would have to be tuned to the solubility of the cannabinoids in the CO2, but should be feasible. In this thesis, a winterization step was included with hexane. This involves dissolving the extract in hexane and freezing it to precipitate out the waxes.

The extraction curves found in this paper determined that the solvent to feed ratio required for extraction of D9-THC is about 0.7g of D9-THC extract per kg of CO2. This is the same for both 40 and 50 degrees C.

It was found that using CO2 as the stationary phase and a water/ethanol mixture as the mobile phase, that no adequate separation could be achieved. Same with CO2 as the stationary phase and a water/methanol mixture as the mobile phase. There are hopes to use supercritical CO2 as the stationary phase, but no commercial CPC machine can handle the pressures required for such a machine.

With the CO2 SFE process outlined, around 80 percentage of the organic solvents can be recycled and 96 percentage of the CO2 can be recycled. Also, the plant matrix after extraction is clean of organic solvent and can be disposed of much easier than with the hydrocarbon extraction. This favors the CO2 SFE process in relation to the environmental impact of the process.

In conclusion CO2 SFE can be used to extract cannabinoids from cannabis plant material. It is heavily favored economically, environmentally, and regulation wise compared to hydrocarbon extraction. The total amount of process steps is also lower than hydrocarbon extraction. It can produce 85 percentage D9-THC extract after a winterization step, which can be further purified. One method of this is CPC which can produce +99 percentage D9-THC. The cost can be largely reduced by having a lower initial cost of cannabis.

January 1, 2018. The California Weed Gold Rush Has Begun. Are you ready ? Strategy.

Read the PDF: 20170608-infinity-supercritical-california-cannabis

California Cannabis

The California recreational sales has begun. The current strategy is to put up cultivation, and then start extraction after harvest. While this may seem intuitively correct, it is the worst strategy for cash-flow.



Start-up Cultivation Means Delayed Cash-flow

If you start with cultivation, you’re looking at 9 -12 months to begin getting cash-flow (in the process from building the grow-house to mature harvest). The time might be a bit better for pure indoor grow, but still a long time regardless. This means you will need a large amount of initial capital outlay, to build facilities, and during the grow. This is valuable time that can be better utilized.


Start with Extraction of Oil for Cash-flow


The profit-makers out in the Cannabis industry have realized that while you can make money cultivating (which everybody is doing), faster access to cash-flow is from the value-added sector, of running extraction machines to produce live resin, shatter, crumb, concentrates for edibles, and vape- pen oil.


Extraction Revenue

Don’t have your own Cannabis product ? Then check with your state regulations and purchase trim or other products from producers who do not have extraction facilities, and then work the value-added space. $50 a pound trim has the potential to get you more than $200 of oil extract. That’s a minimum of four times the value of the trim, and great cash-flow. Of course you will still need to look into the extraction license and other regulations, but this gets you started faster, and with less capital outlay.

Equity Versus Cash-flow

This type strategy gets you faster cash-flow and the all-important sales. This builds equity faster, and requires less initial capital. Starting with just a licensed extraction facility can provide you with a springboard of capital which you can leverage into your own indoor grow, or expanding extraction machinery and capabilities.