IP Library Granted Patent US 12,234,434
Granted Patent B2
US 12,234,434 · App. 18/095,209 · Granted Feb 25, 2025

Methods for modifying a hop flavor profile

Inventors: Thomas J. Martin, Jr. (Tustin, CA); Marcos A. Ojeda (Tustin, CA); Iain W. H. Oswald (Tustin, CA); Kevin A Koby (Tustin, CA)
Assignee: Abstrax Tech Inc.
C12C9/025C12C3/08C12C5/026
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Quick Facts
Patent No.
US 12,234,434
App. No.
18/095,209
Granted
Feb 25, 2025
Kind
B2
Abstract

A method of purifying a hop raw material includes subjecting the hop raw material to a first processing step to form a hop oil extract substantially free of lipids, waxes, flavonoids, and plant matter, collecting the hop oil extract, and optionally subjecting the hop oil extract to a second processing step to yield a purified hop oil product.

Claims (26)

1. A method of purifying a hop raw material, the method comprising:

subjecting the hop raw material to a first processing step to form a hop oil extract having less than 5 wt. % of lipids, waxes, flavonoids, and plant matter;

collecting the hop oil extract; and

subjecting the hop oil extract to a second processing step to yield a purified hop oil product,

wherein the first processing step comprises subjecting the hop raw material to a distillation selected from the group consisting of wiped film distillation, rolled film distillation, and falling film distillation;

wherein the distillation is conducted at a temperature of about 60° C. to about 120° C.

2. The method of claim 1 , wherein the second processing step comprises one or more of distillation, filtration, evaporation, extraction, centrifugation, and fractionation.

3. The method of claim 2 , wherein the second processing step comprises wiped film distillation.

4. The method of claim 3 , wherein the wiped film distillation is conducted at a temperature of about 35° C. to about 150° C.

5. The method of claim 1 , wherein the hop oil extract and/or the purified hop oil product has a higher purity of at least one terpene compared to the hop raw material.

6. The method of claim 1 , wherein the hop oil extract and/or the purified hop oil product has a lower content of at least one terpene compared to the hop raw material.

7. The method of claim 6 , wherein the at least one terpene comprises myrcene, humulene, or caryophyllene.

8. The method of claim 1 , wherein the hop oil extract and/or the purified hop oil product comprises a flavor component, an aroma component, or both a flavor and an aroma component.

9. The method of claim 1 further comprising blending the hop oil extract and/or the purified hop oil product with a terpene, a terpenoid, or both a terpene and a terpenoid.

10. The method of claim 9 , wherein the terpene or terpenoid comprises α-bisabolol, borneol, camphene, camphor, β-caryophyllene, γ-3-carene, caryophyllene oxide, α-cedrene, β-eudesmol, fenchol, geraniol, guaiol, α-humulene, isoborneol, limonene, linalool, menthol, myrcene, nerol, cis-ocimene, trans-ocimene, α-phellandrene, α-pinene, β-pinene, sabinene, α-terpinene, α-terpineol, terpinolene, α-guaiene, elemene, farnesene, germacrene, guaiol, pinanol, selina-3,7 (11)-diene, eudesm-7 (11)-en-4-ol, or valencene.

11. A method of modulating the content of one or more terpenes in a hop raw material, the method comprising:

subjecting the hop raw material to a first processing step to form a hop oil extract having less than 5 wt. % of lipids, waxes, flavonoids, and plant matter;

collecting the hop oil extract; and

subjecting the hop oil extract to a second processing step to yield a purified hop oil product;

wherein the first processing step comprises subjecting the hop raw material to a first distillation selected from the group consisting of wiped film distillation, rolled film distillation, or falling film distillation;

wherein the first distillation is conducted at a temperature of about 60° C. to about 120° C.; and

wherein the second processing step comprises subjecting the hop oil extract to wiped film distillation or rotary evaporation.

12. The method of claim 11 , wherein the one or more terpene comprises myrcene.

13. The method of claim 11 , wherein the wiped film distillation in the second processing step is conducted at a temperature of about 35° C. to about 150° C.

14. The method of claim 11 , further comprising mixing the raw hop material with a solvent prior to the first processing step.

15. The method of claim 14 , further comprising removing the solvent by rotary evaporation at a temperature of between about 30° C. to about 50° C. for a period of about 10 minutes to about 30 minutes.

Assignments (3)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 4, 2024
From: NOVO HOLDINGS, INC.
To: ABSTRAX TECH INC.
Reel/Frame 069122/0730 →
CORRECTIVE ASSIGNMENT TO CORRECT THE INCORRECT ATTACHMENT. CORRECTED ASSIGNMENT DOCUMENT ATTACHED ALONG WITH THE ORGINIAL ASSIGNMENT COVERSHEET PREVIOUSLY RECORDED AT REEL: 68681 FRAME: 280. ASSIGNOR(S) HEREBY CONFIRMS THE CHANGE OF NAME. Recorded Nov 4, 2024
From: ABX INVESTMENTS INC.
To: NOVO HOLDINGS, INC.
Reel/Frame 069293/0230 →
CHANGE OF NAME Recorded Sep 24, 2024
From: ABX INVESTMENTS, INC.
To: NOVO HOLDINGS, INC.
Reel/Frame 068681/0279 →
Continuity (2)
Provisional Application 63344934 · May 23, 2022
Related Publication 20240002758A1 · Jan 4, 2024
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