System and method for an improved personal vapourization device
US-2018263283-A1 · Sep 20, 2018 · US
US12398113B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12398113-B2 |
| Application number | US-202117644690-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 16, 2021 |
| Priority date | Jun 11, 2019 |
| Publication date | Aug 26, 2025 |
| Grant date | Aug 26, 2025 |
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Disclosed herein are methods for converting cannabidiol, cannabidiolic acid and analogs thereof into Δ 8 -tetrahydrocannabinol, Δ 8 -tetrahydrocannabinolic acid and analogs thereof. In particular, there is provided a method for converting a compound of Formula (I) as defined herein into a compound of Formula (II) as defined herein, the method comprising heating the compound of Formula (I) and a Lewis acidic heterogeneous reagent in an aprotic-solvent system to provide a compound of Formula (II), wherein the Lewis-acidic heterogeneous reagent is acidic alumina.
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The invention claimed is: 1. A method for converting a compound of Formula (I) into a compound of Formula (II), the method comprising heating a compound of Formula (I) and a Lewis-acidic heterogeneous reagent in an aprotic-solvent system, to provide a compound of Formula (II) wherein the Lewis-acidic heterogeneous reagent is acidic alumina, and wherein: R 1 is hydrogen or COOH, and R 2 is hydrogen, C 1 -C 12 alkyl, C 2 -C 12 alkenyl, C 2 -C 12 alkynyl, (OCH 2 CH 2 ) 0-6 O(C 1 -C 8 alkyl), (C 0 -C 4 alkyl)-NR 2a R 2b , (C 0 -C 4 alkyl)-aryl, (C 0 -C 4 alkyl)-heteroaryl, (C 0 -C 4 alkyl)-cycloalkyl, or (C 0 -C 4 alkyl)-heterocycloalkyl, wherein R 2a and R 2b are each independently hydrogen or C 1 -C 6 alkyl. 2. The method of claim 1 , wherein the heating step occurs at a temperature in a range from about 80° C. to about 110° C. 3. The method of claim 1 , wherein the heating step occurs at a temperature in a range from about 80° C. to about 100° C. 4. The method of claim 1 , wherein the heating step occurs at a temperature in a range from about 80° C. to about 95° C. 5. The method of claim 1 , wherein the heating step occurs in an inert atmosphere. 6. The method of claim 1 , wherein the heating step is performed in a stirred tank reactor or a rotary bed reactor. 7. The method of claim 1 , wherein the Lewis-acidic heterogeneous reagent is in an amount of between about 0.1 to about 100 molar equivalents with respect to the compound of Formula (I). 8. The method of claim 1 , wherein the Lewis-acidic heterogeneous reagent is in an amount of between about 1 to about 50 molar equivalents with respect to the compound of Formula (I). 9. The method of claim 1 , wherein the Lewis-acidic heterogeneous reagent is in an amount of between about 1 to about 25 molar equivalents with respect to the compound of Formula (I). 10. The method of claim 1 , wherein the Lewis-acidic heterogeneous reagent is in an amount of between about 1 to about 10 molar equivalents with respect to the compound of Formula (I). 11. The method of claim 1 , wherein the Lewis-acidic heterogeneous reagent is in an amount of between about 1 to about 5 molar equivalents with respect to the compound of Formula (I). 12. The method of claim 1 , wherein the aprotic-solvent system comprises acetone, dimethyl sulfoxide, ethyl acetate, dichloromethane, chloroform, toluene, pentane, heptane, hexane, diethyl ether, tert-butyl methyl ether, tetrahydrofuran, dioxane, dimethylformamide, dimethylacetamide, N-methylpyrrolidone, anisole, butyl acetate, cumene, ethyl formate, isobutyl acetate, isopropyl acetate, methyl acetate, methylethylketone, methylisobutylketone, propyl acetate, cyclohexane, para-xylene, meta-xylene, ortho-xylene, or 1,2-dichloroethane, or any combination thereof. 13. The method of claim 1 , wherein the aprotic-solvent system is heptane. 14. The method of claim 1 , further comprising drying the acidic alumina before the heating step. 15. The method of claim 1 , wherein R 1 is hydrogen. 16. The method of claim 1 , wherein R 2 is C 3 H 7 , C 5 H 11 or C 7 H 15 . 17. The method of claim 1 , wherein the compound of Formula (I) is cannabidiol (CBD) and the compound of Formula (II) is Δ 8 -tetrahydrocannabinol (Δ 8 -THC). 18. A method for converting cannabidiol (CBD) into Δ 8 -tetrahydrocannabinol (Δ 8 -THC), the method comprising heating CBD and a Lewis-acidic heterogeneous reagent in an aprotic-solvent system at a temperature in a range from about 80° C. to about 110° C., and wherein the Lewis-acidic heterogeneous reagent is acidic alumina and is in an amount of between about 1 to about 100 molar equivalents with respect to CBD. 19. The method of claim 18 , wherein the aprotic-solvent system comprises acetone, dimethyl sulfoxide, ethyl acetate, dichloromethane, chloroform, toluene, pentane, heptane, hexane, diethyl ether, tert-butyl methyl ether, tetrahydrofuran, dioxane, dimethylformamide, dimethylacetamide, N-methylpyrrolidone, anisole, butyl acetate, cumene, ethyl formate, isobutyl acetate, isopropyl acetate, methyl acetate, methylethylketone, methylisobutylketone, propyl acetate, cyclohexane, para-xylene, meta-xylene, ortho-xylene, or 1,2-dichloroethane, or any combination thereof. 20. The method of claim 18 , wherein the aprotic-solvent system is heptane.
Dibenzopyrans; Hydrogenated dibenzopyrans · CPC title
of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11, as exemplified by patent documents US3702886, GB1334243 and US3709979, respectively · CPC title
Ring systems having three or more relevant rings · CPC title
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