Process for production of essentially pure Δ8-tetrahydrocannabinol from cannabidiol extracted from hemp
AssigneeCct Sciences, LLC
InventorsKyle Olson, Mario Tremblay
Life of this patent
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Abstract
The present invention describes a process to isomerize industrial hemp derived Cannabidiol (CBD) to a pure Δ8-tetrahydrocannabinol (Δ8-THC) extract. This procedure will produce Δ8-tetrahydrocannabinol that is essentially free from any detectable levels of Δ9-tetrahydrocannabinol (Δ9-THC). Included in this filing are methods and processes to scale the reaction from the lab to process to large scale manufacturing. Additionally, the resulting extract from said methods and processes consists of higher purity than previously reported in the art and greater efficiency compared to prior art.
Claims16
A process, comprising:
- (i) refluxing a cannabidiol extract from industrial hemp having less than 0.3% Δ9-tetrahydrocannabinol in a mixture of toluene and p-toluenesulfonic acid monohydrate at 70° C.-100° C. for 120-1440 minutes to obtain a reaction mixture having less than 0.3% Δ9-tetrahydrocannabinol;
- (ii) adding aqueous sodium bicarbonate to neutralize the reaction mixture, adding water, and evaporating to obtain a crude Δ8-tetrahydrocannabinol oil having 73.59-99.73% Δ8-tetrahydrocannabinol by high performance liquid chromatography and less than 0.3% Δ9-tetrahydrocannabinol by high performance liquid chromatography.
A process of producing Δ8-tetrahydrocannabinol, comprising providing a source of cannabidiol extract, adding a catalyst and organic solvent to create a reaction mixture, wherein the catalyst is selected from Zinc Chloride, Hydrochloric acid, Sulfuric acid, Zinc Bromide, Boron Trifluoride, Boron Trifluoride Diethyl Etherate, p-toluenesulfonic acid monohydrate, and a combination thereof, refluxing the reaction mixture for a specified time under acidic conditions, neutralizing the reaction, recovering a solvent product, and distilling the solvent product to obtain a crude Δ8-tetrahydrocannabinol oil having >99% purity,
- wherein the refluxing is selected from the group consisting of a broad reflux performed for between 0.5 to 48 hours, a medium range reflux performed for between 60 to 180 min, and a specific reflux performed for approximately 120 min, and wherein the resulting crude Δ8-tetrahydrocannabinol oil is further purified using fractional, vacuum, short path, molecular, and/or wiped film distillation,
- wherein the dilution ratio of the cannabidiol extract to the organic solvent is 3 to 6 on a weight basis wherein the source cannabidiol extract is cannabidiol crude, cannabidiol isolate or cannabidiol distillate, wherein the organic solvent is toluene, wherein the catalyst is 2.6% of p-toluenesulfonic acid monohydrate, and wherein the refluxing is performed for between 60 to 180 minutes at a reaction temperature selected from the group consisting of a range between 50° C. to 100° C., a range between 60° C. to 80° C., and approximately 70° C.
A process, comprising:
- dissolving 5 kg to 500 kg of cannabidiol isolate with 25 to 250 liters of toluene to form a solution;
- loading the solution into a reaction vessel and heating;
- adding p-toluenesulfonic acid monohydrate (1 kg to 2 kg) to the reaction vessel and refluxing at 60° C.-80° C. for 100-150 minutes;
- quenching the mixture with aqueous 10% NaHCO3, and then adding purified water;
- evaporating the mixture to collect a crude oil having greater than 90% Δ8-tetrahydrocannabinol;
- loading the crude oil into a short path vacuum distillation system having Raschig rings in a condensing head and heating to remove residual solvent and terpenes and obtain a clear distillate;
- loading the clear distillate into a wiped film distillation unit and collecting a distilled oil having greater than 99% Δ8-tetrahydrocannabinol.
Dependencies are inferred from the claim text.