IP Library › Granted Patent US 10,961,174
Granted Patent B2
US 10,961,174 · App. 16/538,487 · Granted Mar 30, 2021

Processes for solvent extraction of cannabinoids, terpenes and flavonoids from biomass

Inventors: Mark G. Tegen (Seattle, WA); Joon Cho (Tumwater, WA); William Rusty Sutterlin (Tuscaloosa, AL)
Assignee: SOCATI TECHNOLOGIES—OREGON, LLC
C07C37/685B01D11/0288C07C37/004C07C2601/14C07C2601/16
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Quick Facts
Patent No.
US 10,961,174
App. No.
16/538,487
Granted
Mar 30, 2021
Kind
B2
Abstract

In alternative embodiments, provided are industrial processes and methods for extracting or removing cannabinoids, flavonoids and terpenes from plant materials such as trichomes. In alternative embodiments, the cannabinoids, flavonoids and terpenes are extracted or removed from the plant materials using a non-polar, organic solvent, or a mixture of non-polar, organic solvent and polar, organic solvent.

Claims (32)

1. A method of producing a winterized, isolated cannabidiol consisting essentially of:

a) isolating a trichome from cannabis;

b) extracting the trichome of the cannabis using a first solvent selected from the group consisting of limonene, myrcene, pinene, humulene, geraniol, perillyl alcohol, terpineol, and mixtures thereof to produce a first extract of the trichome of the cannabis consisting essentially of cannabidiol,

wherein the limonene, myrcene, pinene, humulene, geraniol, perillyl alcohol and terpineol used for extraction are not derived from the trichome of the cannabis;

c) distilling the first extract of the trichome of the cannabis in (b) consisting essentially of the cannabidiol to produce a first isolate the cannabidiol,

d) extracting the first isolate of the cannabidiol using a second solvent selected from the group consisting of 1,4 dioxane, chloroform, dichloromethane, diethyl ether, acetone, benzene, toluene, xylene, ethyl acetate, propyl acetate, butyl acetate, tetrahydrofuran, tetrahydropyran, hexane, pentane, heptane, and mixtures thereof to produce a second isolate of the cannabidiol, and

e) winterizing the distilled, second isolate of the cannabidiol of (d) to produce a winterized, isolated cannabidiol.

2. The method of claim 1 , wherein the trichome of cannabis is from Cannabis sativa, Cannabis indica or Cannabis ruderalis.

3. The method of claim 1 , wherein the pinene is α-pinene.

4. The method of claim 1 , wherein the trichome of cannabis , other than harvesting or collecting, is unprocessed or has not been physically processed, or has not been exposed to a solvent solution, an aqueous solution, a heating process, a drying process, a dehydration process, a crushing process, a chopping process, a macerating process or a mincing process, since its harvest.

5. The method of claim 1 , wherein the trichome of cannabis is subjected to a heating process, a drying process, a dehydration process, a crushing process, a chopping process, a macerating process or a mincing process, since its harvest.

6. The method of claim 1 , wherein the extracting of the cannabinol from the isolated trichome from cannabis using the first solvent consists essentially of:

(a) feeding the trichome of cannabis into a vessel; and

(b) feeding the first solvent into the vessel to saturate or substantially saturate the trichome of cannabis in the vessel with the first solvent to create a mixture of the first solvent and the trichome of cannabis , thereby dissolving the trichome of cannabis into the first solvent.

7. The method of claim 6 , wherein the vessel is heated before and/or during the feeding and/or saturating or dissolving process for between about 5 min and 5 hrs.

8. The method of claim 6 , wherein the vessel is heated to or kept warm or hot between about 30° C. and 300° C.

9. The method of claim 8 , wherein the vessel is heated to or kept warm or hot between about 35° C. and 200° C.

10. The method of claim 9 , wherein the vessel is heated to or kept warm or hot between about 37° C. and 100° C.

11. The method of claim 1 , wherein the vessel is cooled and/or kept cool before and/or during the feeding and/or saturating or dissolving process.

12. The method of claim 6 , wherein the vessel is cooled or kept cool before and/or during the feeding and/or saturating or dissolving process, and the contact time is between about 1 hr and 48 hrs.

13. The method of claim 7 , wherein the vessel is cooled or kept cool before and/or during the feeding and/or saturating or dissolving process, and the contact time is between about 2 hrs and 36 hrs.

14. The method of claim 8 , wherein the vessel is cooled or kept cool before and/or during the feeding and/or saturating or dissolving process, and the contact time is between about 3 hrs and 24 hrs.

15. The method of claim 9 , wherein the vessel is cooled or kept cool to between about −20° C. and 37° C.

16. The method of claim 10 , wherein the vessel is cooled to between about −18° C. and 22° C.

17. The method of claim 6 , wherein the mixture is agitated during all or part of the saturating process.

18. The method of claim 1 , wherein the treating or exposing of the trichome of cannabis to the first solvent lasts for a period of between about 1 minute to about 48 hours.

19. The method of claim 18 , wherein the treating or exposing of the trichome of cannabis to the first solvent lasts for a period of between about 1 minute to 60 minutes.

20. The method of claim 1 , wherein the treating or exposing of the trichome of cannabis to the first solvent is immersion, spraying, washing, counter current liquid solid contacting or any combination thereof.

21. The method of claim 1 , wherein before the treating or exposing of the trichome of cannabis to the first solvent the cannabis is fed through a conveyor into an extraction unit and is sprayed or continuously sprayed with the first solvent.

22. The method of claim 1 , wherein the trichome of cannabis is not dried before the treating or exposing of the cannabis to the first solvent.

23. The method of claim 1 , wherein the trichome cannabis is substantially wet before the treating or exposing of the cannabis to the first solvent.

24. The method of claim 1 , wherein the distillation is batch distillation, continuous distillation or vacuum distillation.

Assignments (6)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 7, 2025
From: CLEEN TECHNOLOGY INC.
To: SALADINO, PETER
Reel/Frame 069771/0831 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 7, 2025
From: SALADINO, PETER
To: ATLAS INVESTMENTS SEATTLE LLC
Reel/Frame 069772/0349 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 7, 2025
From: ATLAS INVESTMENTS SEATTLE LLC
To: MOLO TECHNOLOGIES LLC
Reel/Frame 069774/0041 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 24, 2023
From: SOCATI TECHNOLOGIES - OREGON, LLC
To: CLEEN TECHNOLOGY INC.
Reel/Frame 064357/0006 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 13, 2020
From: SOCATI TECHNOLOGIES LLC
To: SOCATI TECHNOLOGIES - OREGON, LLC
Reel/Frame 052378/0852 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 9, 2020
From: TEGEN, MARK G.; CHO, JOON; SUTTERLIN, WILLIAM RUSTY
To: SOCATI TECHNOLOGIES LLC
Reel/Frame 052360/0599 →
Continuity (5)
Continuation 16447853 · Jun 20, 2019
Continuation In Part 16259616 · Jan 28, 2019
Provisional Application 62781958 · Dec 19, 2018
Provisional Application 62779862 · Dec 14, 2018
Related Publication 20200190002A1 · Jun 18, 2020