Process and apparatus to obtain tobacco flavor extracts
US-11044938-B2 · Jun 29, 2021 · US
US12593864B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12593864-B2 |
| Application number | US-201816614111-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 9, 2018 |
| Priority date | May 15, 2017 |
| Publication date | Apr 7, 2026 |
| Grant date | Apr 7, 2026 |
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Embodiments described herein provide a method of making a tobacco extract comprising; (a) contacting tobacco with an extraction solvent in a first chamber such that tobacco components are extracted from the tobacco into the extraction solvent, wherein the extraction solvent is a supercritical fluid in the first chamber; (b) passing the extraction solvent containing tobacco components along a line towards a second chamber, wherein a valve is present in the line and the conditions downstream of the valve are such that the extraction solvent is subcritical; and (c) pumping entrapment solvent into a flow downstream of the valve, wherein the tobacco components are released from the extraction solvent by transfer to subcritical conditions and are dissolved in the entrapment solvent, whereby the tobacco components dissolved in entrapment solvent are collected in the second chamber.
Opening claim text (preview).
The invention claimed is: 1 . A method of making a tobacco extract, the method comprising: (a) contacting tobacco with an extraction solvent in a first chamber such that tobacco components are extracted from the tobacco into the extraction solvent, wherein the extraction solvent is a supercritical fluid in the first chamber; (b) passing the extraction solvent containing tobacco components along a line towards a second chamber, wherein a valve is present in the line and the conditions downstream of the valve are such that the extraction solvent is subcritical; and (c) pumping entrapment solvent into a flow downstream of the valve and through the second chamber, wherein the tobacco components are released from the extraction solvent by transfer to subcritical conditions and are dissolved in the entrapment solvent, whereby the tobacco components dissolved in entrapment solvent are collected from the second chamber, and wherein entrapment solvent is pumped into the system at an approximately constant flow rate throughout the process, wherein the tobacco components include tobacco aromas and/or flavors. 2 . The method according to claim 1 , wherein the extraction solvent comprises carbon dioxide. 3 . The method according to claim 2 wherein at (a), the temperature is in the range of about 308-473K and the pressure is in the range of about 8-85 MPa. 4 . The method of claim 3 , wherein at (a), the temperature is in the range of about 328-350K. 5 . The method of claim 3 , wherein at (a), the pressure is in the range of about 20-30 MPa. 6 . The method according to claim 1 , wherein the entrapment solvent comprises an aerosol generating agent. 7 . The method according to claim 6 , wherein the entrapment solvent comprises a polyol. 8 . The method according to claim 7 , wherein the entrapment solvent comprises glycerol and/or propylene glycol. 9 . The method according to claim 1 , wherein the tobacco components include nicotine. 10 . The method of claim 1 , further comprising a step of providing the entrapment solvent containing dissolved tobacco components in a cartridge. 11 . The method of claim 10 , wherein the cartridge is configured for use in a smoking article. 12 . The method of claim 1 , wherein the tobacco extract has a viscosity of greater than 0.32 Pa s. 13 . The method of claim 1 , wherein the tobacco extract has a viscosity of at least 0.74 Pa s.
by aromatic compounds · CPC title
Use of organic solvents for extraction · CPC title
Nicotine · CPC title
in liquid or vaporisable form, e.g. liquid compositions for electronic cigarettes · CPC title
by extraction; Tobacco extracts · CPC title
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