Methods and systems for processing a reaction product mixture of cellulosic biomass material
View Patent ↗Processing of a reaction product mixture containing at least one volatile organic compound as well as lignin, lignin derived compounds, and/or unextracted cellulose and hemicellulose using a recovery system comprising at least two flashers or at least one flasher and at least two reboilers. In a particular embodiment, the reaction product mixture comes from reactions involving deconstruction (or digestion) of biomass, particularly cellulosic biomass which contains various polysaccharides (e.g., carbohydrates) and lignin.
1. A system comprising:
a digestion unit adapted to digest a cellulosic biomass material to generate a digested product;
a separation zone adapted to separate the digested product into at least an overhead fraction and a bottom fraction; wherein the bottom fraction comprises (i) at least one compound having a separation point having a temperature in a range of about 100 to 600 degrees C. and a pressure of about atmospheric pressure, and (ii) one or more volatile organic compounds; and
a recovery unit comprising a first flasher coupled to the separation zone to receive at least a portion of the bottom fraction during operation of the first flasher;
and a second flasher coupled to the separation zone to receive at least a portion of the bottom fraction during operation of the second flasher;
wherein the recovery unit is configured to operate one of the first and second flashers to vaporize at least one volatile organic compound in the bottom fraction while the other flasher is in standby mode.
2. The system of claim 1 further comprising a further processing zone coupled to the separation zone, the further processing zone is configured to convert at least a portion of a plurality of hydrocarbon and oxygenated hydrocarbon molecules in the overhead fraction from the separation zone to a product stream comprising a higher hydrocarbon.
3. The system of claim 2 wherein an outlet of the recovery unit adapted to discharge at least a portion of the overhead product is coupled to an inlet of the processing zone.
4. The system of claim 1 further comprising a heating component adapted to heat at least a portion of the bottom fraction prior to the bottom fraction entering the flasher in operation.
5. The system of claim 1 wherein at least one flasher comprises a conduit adapted to circulate a heat exchange medium.
6. The system of claim 1 wherein the bottom fraction comprises a compound having a separation point having a temperature in a range of about 100 to 500 degrees C. and a pressure in a range of about 1 to 100 Torr.
7. The system of claim 1 wherein the flasher in operation is adapted to apply a temperature in a range of about 100 to 600 degrees C. and a pressure in a range of 0.01 to 250 psi to the bottom fraction.
8. The system of claim 1 wherein the bottom fraction comprises at least one of lignin, a lignin-derived compound, unextracted cellulose, unextracted hemicellulose, a caramelan, and any combination thereof.
9. The system of claim 1 further comprising a third flasher coupled to the separation zone to receive at least another portion of the bottom fraction.
10. The system of claim 1 wherein at least one of the first and second flashers comprises at least one packer element.
11. The system of claim 1 wherein each of the first and second flashers is adapted to combust a compound from the bottom fraction deposited on a surface in the flasher to generate thermal energy.
12. A method comprising:
providing a biomass feedstock containing cellulose and water;
digesting at least a portion of the biomass feedstock to generate a digested product;
separating the digested product into at least an overhead fraction and a bottom fraction, wherein the bottom fraction comprises (i) at least one compound having a separation point having a temperature in a range of about 100 to 600 degrees C. and a pressure of about atmospheric pressure selected, and (ii) one or more volatile organic compounds;
vaporizing at least one volatile organic compound from the bottom fraction in a first flasher to generate an overhead product;
depositing the at least one compound having a separation point having a temperature in a range of about 100 to 600 degrees C. and a pressure of about atmospheric pressure on a surface in the first flasher;
placing the first flasher in standby mode;
vaporizing at least one volatile organic compound from the bottom fraction in a second flasher to generate additional overhead product; and
combusting the deposited at least one compound in the first flasher.
13. The method of claim 12 further comprising converting at least a portion of a plurality of hydrocarbon and oxygenated hydrocarbon molecules in the overhead fraction from the separating step to a product stream comprising a higher hydrocarbon.
14. The method of claim 13 wherein the overhead product from at least one vaporization step comprises a plurality of oxygenated hydrocarbon molecules.
15. The method of claim 14 further comprising converting at least a portion of the oxygenated hydrocarbon molecules in the overhead product from at least one vaporization step to a product stream comprising a higher hydrocarbon.
16. The method of claim 12 wherein the vaporizing step comprises applying a temperature in a range of 100 to 600 degrees C. and a pressure in a range of 0.01 to 250 psi to the bottom fraction.
17. The method of claim 12 wherein said surface of the first flasher comprises a surface of a packer element disposed in the first flasher.
18. The method of claim 12 further comprising providing thermal energy from combustion of the deposited at least one compound in the first flasher to at least a portion of the bottom fraction prior to the bottom fraction entering the flasher in operation.