Processes for the removal of rubber from non-Hevea plants
US-9611334-B2 · Apr 4, 2017 · US
US10132563B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10132563-B2 |
| Application number | US-201715424224-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 3, 2017 |
| Priority date | Jun 18, 2012 |
| Publication date | Nov 20, 2018 |
| Grant date | Nov 20, 2018 |
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Provided herein are methods for the removal of organic solvents from wet bagasse. The use of the methods result in dried bagasse that contains no more than 1 weight percent organic solvents.
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What is claimed is: 1. A method for removing organic solvents from wet guayule guayule bagasse comprising: utilizing a quantity of wet guayule bagasse that contains up to 45 weight % combined organic solvents and water (based upon the total weight of the wet guayule bagasse) and no more than 0.1 weight % rubber; heating the wet guayule bagasse to a temperature of at least 100° C. utilizing a dryer apparatus containing multiple layers, circulating heated air through the layers, and passing the wet guayule bagasse from one layer to another whereby the organic solvents are evaporated; producing dried guayule bagasse that contains no more than 1 weight % organic solvents. 2. The method of claim 1 , wherein the heating occurs for no more than 10 minutes at a temperature of at least 110° C. 3. The method of claim 1 , wherein the heating occurs for no more than 8 minutes at a temperature of 125° C. 4. The method of claim 1 , wherein the heating occurs for no more than 7 minutes at a temperature of at least 125° C. 5. The method of claim 1 , wherein the dried guayule bagasse contains no more than 0.5 weight % organic solvents. 6. The method of claim 1 , wherein the wet guayule bagasse remains in the apparatus for 5-90 minutes. 7. The method of claim 1 , wherein the heating is achieved by heated steam. 8. The method of claim 1 , further comprising condensing the evaporated organic solvents and collecting them separately from the dried guayule bagasse. 9. The method of claim 1 , further comprising compressing the dried guayule bagasse into a briquette having a density that is at least 40% greater than the density of the non-compressed dried guayule bagasse. 10. The method of claim 1 , wherein the combined solvents are acetone and hexane. 11. The method of claim 9 , wherein the combined solvents are acetone and hexane. 12. The method of claim 1 , wherein the wet guayule bagasse is heated to a temperature of between 100 and 200° C. 13. A method for removing organic solvents from wet guayule bagasse comprising: utilizing a quantity of wet guayule bagasse that contains up to 45 weight % combined organic solvents and water (based upon the total weight of the wet guayule bagasse) and no more than 0.1 weight % rubber; heating the wet guayule bagasse to a temperature of at least 100° C. utilizing a dryer apparatus containing multiple paddles for mixing the wet guayule bagasse with heated air to evaporate the organic solvents; producing dried guayule bagasse that contains no more than 1 weight % organic solvents. 14. The method of claim 13 , wherein the heating occurs for no more than 10 minutes at a temperature of at least 110° C. 15. The method of claim 13 , wherein the wet guayule bagasse remains in the apparatus for 5-90 minutes. 16. The method of claim 13 , further comprising condensing the evaporated organic solvents and collecting them separately from the dried guayule bagasse. 17. The method of claim 13 , further comprising compressing the dried guayule bagasse into a briquette having a density that is at least 40% greater than the density of the non-compressed dried guayule bagasse. 18. The method of claim 13 , wherein the combined solvents are acetone and hexane. 19. The method of claim 17 , wherein the combined solvents are acetone and hexane. 20. A method for removing organic solvents from wet guayule bagasse comprising: utilizing a quantity of wet guayule bagasse that contains up to 45 weight % combined organic solvents and water (based upon the total weight of the wet guayule bagasse) and no more than 0.1 weight % rubber; heating the wet guayule bagasse to a temperature of at least 100° C. utilizing a desolventization screw extruder apparatus; producing dried guayule bagasse that contains no more than 1 weight % organic solvents. 21. The method of claim 20 , wherein the heating occurs for no more than 10 minutes at a temperature of at least 110° C. 22. The method of claim 20 , wherein the wet guayule bagasse remains in the apparatus for 5-90 minutes. 23. The method of claim 20 , further comprising condensing the evaporated organic solvents and collecting them separately from the dried guayule bagasse. 24. The method of claim 20 , further comprising compressing the dried guayule bagasse into a briquette having a density that is at least 40% greater than the density of the non-compressed dried guayule bagasse. 25. The method of claim 20 , wherein the combined solvents are acetone and hexane. 26. The method of claim 24 , wherein the combined solvents are acetone and hexane.
condensing vapours onto the surface of the materials to be dried · CPC title
the gas or vapour circulating over or surrounding the materials or objects to be dried (F26B3/14 takes precedence) · CPC title
Subject matter not provided for in other groups of this subclass {, e.g. flours, kernels} · CPC title
Treatment of rubber before vulcanisation, not provided for in groups C08C1/00 - C08C3/02 · CPC title
Materials not provided for elsewhere · CPC title
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