Methods for extraction and isolation of isoprenoid and terpene compounds from biological extracts
10967018 ยท 2021-04-06
Assignee
Inventors
Cpc classification
A61K2236/35
HUMAN NECESSITIES
A61K2236/15
HUMAN NECESSITIES
A61K2236/37
HUMAN NECESSITIES
A61K31/352
HUMAN NECESSITIES
A61K2236/53
HUMAN NECESSITIES
A61K2236/39
HUMAN NECESSITIES
International classification
Abstract
A method for the extraction and isolation of the terpene and isoprenoid compounds from plant material, followed by a centrifugal force induced selective crystallization of isoprenoids resulting in a separation of terpene and isoprenoid fractions. This this method is suitable for the extraction of cannabinoids from Cannabis and the enrichment tetrahydrocannabinolic acid and reduction of tetrahydrocannabinol in an extract.
Claims
1. A method of extracting terpene and isoprenoid compounds from plant material and for selectively enriching the concentration of isoprenoid compounds in a fraction of this extract comprising the steps of: a. placing plant material into an extraction chamber, wherein the plant material comprises female flowers of Cannabis; b. degassing the extraction chamber; c. introducing chilled solvent into the extraction chamber such that extract-containing solvent forms; d. filtration of the extract-containing solvent; e. removal of the extract-containing solvent from the extraction chamber; f. placing extract-containing solvent on a surface prior to placing the extract-containing solvent into a centrifuge vessel, the surface being capable of being placed into a vacuum oven; g. placing the extract-containing solvent into a centrifuge vessel; h. centrifuging the centrifuge vessel to promote formation of crystals and to separate said crystals from supernatant solvent; and i. collecting the crystals.
2. The method of claim 1 wherein the crystals are over 90% pure THCA.
3. The method of claim 1 further comprising the step of: sorting and reducing the size of the plant material by destemming and grinding the plant material prior to placing the plant material in the extraction chamber.
4. The method of claim 1 further comprising the step of: chilling the plant material prior to placing plant material into the extraction chamber.
5. The method of claim 1 further comprising the step of: pre-chilling the extraction chamber prior to placing plant material into the extraction chamber.
6. The method of claim 1 further comprising the step of: placing said extract-containing solvent on a surface into a vacuum oven in order to accelerate crystal formation prior to placing the extract-containing solvent into a centrifuge vessel.
7. The method of claim 1 further comprising the step of: waiting for crystals to begin to form on the surface prior to placing the extract-containing solvent into a centrifuge vessel.
8. The method of claim 1 further comprising the steps of: waiting for crystals to begin to form on the surface; placing the surface and extract-containing solvent into a vacuum oven; closing the vacuum oven; purging the vacuum oven of air; incubating the extract in the vacuum oven until polymorphic crystals begin to form; and, removing the surface and extract-containing solvent from the vacuum oven.
9. The method of claim 1 further comprising the step of: placing the surface and the extract-containing solvent into a vacuum oven in order to accelerate crystal formation.
10. The method of claim 1 wherein the solvent is subcritical n-propane, butane, hexane, pentane, ether, ethyl acetate, heptane, toluene, naphtha, methanol, isopropanol, butanol, or combinations thereof.
11. The method of claim 1 wherein the solvent is supercritical carbon dioxide.
12. The method of claim 1 wherein various extracts of Cannabis are substituted for the plant material.
13. A method of extracting terpene and isoprenoid compounds from plant material and for selectively enriching the concentration of isoprenoid compounds in a fraction of this extract comprising the steps of: a. placing plant material into an extraction chamber, wherein the plant material comprises female flowers of Cannabis; b. degassing the extraction chamber; c. introducing chilled solvent into the extraction chamber such that extract-containing solvent forms; d. filtration of the extract-containing solvent; e. removal of the extract-containing solvent from the extraction chamber; f. addition of sugar, salt, or other precipitant to the extract-containing solvent, wherein the precipitant is chosen for selectively precipitating THCA; g. placing the extract-containing solvent into a centrifuge vessel; h. centrifuging the centrifuge vessel to promote formation of crystals and to separate said crystals from supernatant solvent; and i. collecting the crystals.
14. The method of claim 13 wherein the precipitant is chosen for selectively precipitating delta-9 THC.
15. The method of claim 13 wherein the precipitant is chosen for selectively precipitating CBD.
16. The method of claim 1 further comprising the step of: addition of acid, base, or buffering compounds to the solvent or solvent-containing extract so as to regulate the pH of the system and to promote differential crystallization.
17. A method of extracting terpene and isoprenoid compounds from plant material and for selectively enriching the concentration of isoprenoid compounds in a fraction of this extract comprising the steps of: a. placing plant material into an extraction chamber, wherein the plant material comprises female flowers of Cannabis; b. degassing the extraction chamber; c. introducing chilled solvent into the extraction chamber such that extract-containing solvent forms; e. removal of the extract-containing solvent from the extraction chamber; f. addition of precipitant, wherein the precipitant is chosen for selectively promoting the precipitation of delta-9 THC g. Buchner filtration of the solvent containing extract prior to centrifugation h. placing the extract-containing solvent into a centrifuge vessel; i. centrifuging the centrifuge vessel to promote formation of crystals and to separate said crystals from supernatant solvent; and j. collecting the crystals.
18. The method of claim 17 wherein the precipitant is chosen for selectively promoting the precipitation of CBD.
19. The method of claim 17 wherein the precipitant is chosen for selectively promoting the precipitation of gums, waxes, phospholipids, protein, lipoprotein, carbohydrates, sugars, nucleic acids, coenzymes, or metal ions.
20. The method of claim 1 further comprising the step of: collection of a terpene-rich fraction.
21. The method of claim 1 wherein the solvent is a non-polar liquid organic solvent chilled to between 0 C. and 100 C.
22. The method of claim 13 wherein the solvent is subcritical n-propane, butane, hexane, pentane, ether, ethyl acetate, heptane, toluene, naphtha, methanol, isopropanol, butanol, or combinations thereof.
23. The method of claim 17 wherein the solvent is subcritical n-propane, butane, hexane, pentane, ether, ethyl acetate, heptane, toluene, naphtha, methanol, isopropanol, butanol, or combinations thereof.
24. The method of claim 1, further comprising the steps of: sorting and reducing the size of the plant material by destemming and grinding the plant material prior to placing the plant material in the extraction chamber; chilling the plant material prior to placing plant material into the extraction chamber; pre-chilling the extraction chamber prior to placing plant material into the extraction chamber; placing the surface and extract-containing solvent into a vacuum oven; closing the vacuum oven; purging the vacuum oven of air; incubating the extract in the vacuum oven until polymorphic crystals begin to form; and, removing the surface and extract-containing solvent from the vacuum oven; wherein the solvent is subcritical n-propane, butane, hexane, pentane, ether, ethyl acetate, heptane, toluene, naphtha, methanol, isopropanol, butanol, or combinations thereof; and, wherein the crystals are over 90% pure THCA.
Description
BRIEF DESCRIPTION OF THE FIGURES
(1)
(2)
(3)
(4)
(5)
(6)
(7)
(8)
DETAILED DESCRIPTION OF THE INVENTION
(9) With reference to
(10) With reference to
(11) In some embodiments, the flowers are not dried. In one preferred embodiment, the flowers are reduced in size to 1-3 mm. In some embodiments, the flowers are not reduced in size. In one preferred embodiment, the flowers are chilled to between 0 C. and 100 C. prior to extraction. In one preferred embodiments the extraction chamber is pre-chilled to between 0 C. and 100 C. In one preferred embodiment, the n-propane is pre-chilled to between 0 C. and 100 C. before introduction into the extraction chamber. In some embodiments, there is a soak time upon introduction of the n-propane into the extraction chamber prior to separating the n-propane containing dissolved compounds from the plant material. In other embodiments there is no soak time, and separation of the n-propane containing dissolved compounds from the plant material is immediate. In some embodiments, the n-propane is recovered from the receiver vessel by use of differential pressure or temperature such that the n-propane becomes a gas and is readily removable, as is known in the art.
(12)
(13) In some embodiments the surface is a stainless steel sheet. In other embodiments, the surface is wax paper, a glass crystallization dish, foil sheeting, or other materials known in the art. In one preferred embodiment, the vacuum oven is at a temperature between 21 C. and 60 C., and at a pressure of less than one atmosphere. In some embodiments, the centrifuge (including but not limited to a continuous tubular centrifuge, scroll centrifuge or swing bucket centrifuge) is spun at a rate between 10 rpms to 50,000 rpms at a temperature range between 60 C. to 200 C. for a time which is sufficient to separate terpenes and isoprenoid compounds. In one preferred embodiment, the centrifuge is held at a temperature between 21 C. and 60 C., and activated so as to exert 500-2000 gravity upon the extract containing terpenes and isoprenoid compounds. In some embodiments, the centrifugally pelleted crystal fraction and liquid supernatant fraction are separated by filtration. In other embodiments the centrifugally pelleted crystal fraction and liquid supernatant fraction are separated by decanting.
(14) In some embodiments, the process may further comprise steps of filtering the condensate during centrifugation to collect water insoluble material and extracting the insoluble material. In some embodiments precipitants are added to the extract, in order to affect the precipitation of impurities, which will then be subsequently filtered out. In some embodiments precipitants are added to the extract in order to affect the selective precipitation of target isoprenoid compounds, with subsequent centrifugation or filtration being used to harvest these target compounds. In one preferred embodiment, sucrose crystals (sugar) can be used as a selective precipitant for THCA relative to other cannabinoids found in a non-polar solvent extract of cannabinoidswith this selectivity owing to the hydrophilic nature of sucrose and the relatively greater hydrophilic nature of THCA to other cannabinoids (resulting from the carboxylic acid moiety on THCA).
(15) As an example of the primary embodiment, consider the preparation of a highly pure THCA Cannabis extract meant for use in research into the potential treatment of a human disease state, such as prostate cancer or various inflammatory diseases (THCA has been indicated as potentially useful in treating these disease states, as in known in the art, with some examples being shown in
(16) In some embodiments, the starting material in the process, or condensates, may be derived from any Cannabis product containing the target compound(s), and most preferably from a stage in the processing in which higher molecular weight cannabinoids and/or terpenes are still intact.
(17) In some embodiments, the extract can also be provided in a variety of forms, including but not limited to oils and other concentrated liquid forms, or in dried forms such as but not limited to crystals, powders and the like.
(18) In some embodiments, the process may be operated continuously including but not limited to use of screen centrifuges or scroll centrifuges and as such is particularly suitable for use in large scale commercial production of extracts from crude Cannabis extracts or plant material.
(19) In some embodiments, Bchner filtration, or other types of differential pressure filtration, is used in order to speed the separation of liquids and solids contained in solvent extracts.
(20) In some embodiments other solvents are used for the initial extraction, including but not limited to supercritical carbon dioxide, hexane, or ether.
(21) In some embodiments the terpene containing fraction is used directly as a side-product.
(22) In some embodiments, the terpene or cannabanoid isolate is subject to further purification for purposes of isolating at least one target compound(s) from the extract by thermal fractionation (such as distillation, e.g. vacuum distillation, and related processes), chromatographic separation (such as normal and reverse phase or affinity purification), recrystallization or combinations thereof. In these and other embodiments it may also be preferable to adjust pH of the condensate to enhance precipitation of the at least one target compound(s).
(23) Although described with reference to preferred embodiments of the invention, it should be recognized that various changes and/or modifications of the invention can be made without departing from the spirit and scope of the invention. In any case, the invention is only intended to be limited by the scope of the following claims.