Processes for producing biomass pellets and sugars
US-9315750-B2 · Apr 19, 2016 · US
US10329505B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10329505-B2 |
| Application number | US-201414783091-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 8, 2014 |
| Priority date | Apr 8, 2013 |
| Publication date | Jun 25, 2019 |
| Grant date | Jun 25, 2019 |
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The present invention relates to a method for manufacturing a biofuel from a vegetable-based biomaterial by performing the manufacture in an integrated manner, in such a way that the biomaterial is made finer and dried with the aid of heat brought from a heat-releasing process, when the drying is finally performed after the finer making stage, optionally in such a way that drying is started already in connection with finer making. The invention also relates to a biofuel manufactured in this manner and the use of the fuel in question.
Opening claim text (preview).
The invention claimed is: 1. A method for manufacturing a biofuel from a vegetable-based biomaterial, comprising the integrated steps of making the biomaterial finer in at least one stage by defibration and drying the biomaterial with the aid of heat brought from a heat-releasing process wherein: the drying starts in the grinder and is finalized after the finer making stage, the defibration is done to sliver mass, the slivers having a diameter of 0.1 to 0.3 mm and length of 1 to 5 mm, and the heat-releasing process is one that is intended specifically and only for producing the heat required for drying the biomaterial by combusting the biofuel. 2. The method according to claim 1 , wherein the manufacturing is performed essentially as a continuous operation. 3. The method according to claim 1 , wherein the biomaterial is selected from the group of: timber material; peat; grass plants; organic waste, or some mixture of the aforementioned. 4. The method according to claim 1 , further comprising; chipping the biomaterial is to form chips that are substantially 20-40 mm long, wherein the chips are defibrated in a defibrator, removing the defibrated material from the defibrator, wherein the defibrated material is dried in a drier by leading a hot gas into the drier, and recovering the dried material. 5. The method according to claim 4 , wherein the biomaterial is timber material and wherein the biomaterial is chipped to form chips having a length of 20-40 mm, a width of 10-30 mm, and a thickness of less than 5 mm. 6. The method according to claim 5 , further comprising; screening the chips to separate impurities before the chips are led to defibration, and sending back excessively large wood pieces to be chipped. 7. The method according to claim 1 , wherein the heat-releasing process is a combustion process or a treatment process of a bio-refinery. 8. The method according to claim 1 , wherein the heat-releasing process is a combustion process, which is combined with production of high-pressure steam and electricity, or production of district heating. 9. The method according to claim 1 , wherein the biomaterial is dried with the aid of waste heat of a heat-releasing process. 10. The method according to claim 1 , wherein air having a temperature of 100-200° C. is used in the drying of the biomaterial. 11. The method according to claim 1 , wherein air is used in the drying of the biomaterial, and wherein the air is used as a carrying medium to transport the defibrated mass away from a defibrator to a drier. 12. The method according to claim 1 , wherein the drying includes flash drying in one or more stages. 13. The method according to claim 1 , wherein the biomaterial is dried to a dry-material content of 85-95%. 14. A biofuel, manufactured from a vegetable-based biomaterial, wherein the biofuel is manufactured in an integrated manner comprising the steps of; making the biomaterial finer in at least one stage of integrated defibration and drying with the aid of heat from a heat-releasing process wherein: the drying starts in the grinder and is finalized after the finer making stage, the defibration is done to sliver mass, the slivers having a diameter of 0.1 to 0.3 mm and length of 1 to 5 mm, and the heat-releasing process is one that is intended specifically and only for producing the heat required for drying the biomaterial by combusting the biofuel. 15. The biofuel according to claim 14 , refined into pellets or a liquid fuel. 16. The method of claim 1 , wherein the drying and defibration are integrated by leading a hot gas flow through a defibrator. 17. The method of claim 16 , wherein the biomaterial and hot gas flow are fed through the defibrator simultaneously. 18. A method for manufacturing a liquid biofuel from a vegetable-based biomaterial, comprising the integrated steps of making the biomaterial finer in at least one stage by defibration and drying the biomaterial with the aid of heat brought from a heat-releasing process wherein: the drying starts in the grinder and is finalized after the finer making stage, the defibration is done to sliver mass, the slivers having a diameter of 0.1 to 0.3 mm and length of 1 to 5 mm, the heat-releasing process is one that is intended specifically and only for producing the heat required for drying the biomaterial by combustion, and liquid biofuel is manufactured from the biomaterial that has been made finer and dried.
Fuel from waste, e.g. synthetic alcohol or diesel · CPC title
Biofuels, e.g. bio-diesel · CPC title
Disintegrating peat (obtaining fibres from peat D01B1/50) · CPC title
on vegetable substances · CPC title
Agricultural waste, e.g. corn crops, grass clippings, nut shells or oil pressing residues · CPC title
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