US2011271588A1PendingUtilityA1
Synthetic coal and methods of producing synthetic coal from fermentation residue
Est. expiryNov 6, 2029(~3.3 yrs left)· nominal 20-yr term from priority
Inventors:Frederick J. SchendelMarc Gregor Von KeitzKenneth J. ValentasLindsey R. JaderSteven M. Heilmann
Y02E50/30C10L 9/086Y02E50/10C10L 5/447
38
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Claims
Abstract
Synthetic coal, methods of producing synthetic coal, produced from fermentation residue, such as the residue from ethanol production, by subjecting the fermentation residue to hydrothermal carbonization in an aqueous solution at a temperature and a pressure sufficient to form a synthetic coal solid and a liquid component. The solid synthetic coal component has a low ash content and may be used as a carbon source for energy production, such as for combustive thermal energy generation, or for gassification for the production of synthesis gas.
Claims
exact text as granted — not AI-modified1 . A method of producing a synthetic coal from fermentation residues, the method comprising the steps of:
a) obtaining a fermentation residue; b) subjecting said fermentation residue to hydrothermal carbonization in an aqueous medium at a temperature and a pressure sufficient to form a synthetic coal solid.
2 . The method of claim 1 further comprising separating synthetic coal solid from the aqueous medium.
3 . The method of claim 1 wherein the temperature is between about 170° C. and about 225° C.
4 . The method of claim 1 wherein the pressure is between about 0.8 and about 2.41 MPa.
5 . The method of claim 1 further comprising combining the fermentation residue with an acidic buffer.
6 . The method of claim 1 wherein the fermentation residue is produced from corn based ethanol production.
7 . A method of producing a synthetic coal from fermentation residues, the method comprising the steps of:
a) obtaining an fermentation residue; b) subjecting said fermentation residue to hydrothermal carbonization in an aqueous solution at a temperature of between about 170° C. and about 225° C. and a pressure of between about 0.8 and about 2.41 MPa; and c) separating a synthetic coal solid from a liquid component. \
8 . The method of claim 7 further comprising combining the fermentation residue with an acidic buffer.
9 . The method of claim 1 wherein the fermentation residue is a byproduct of corn based ethanol production.
10 . The method of claim 7 further comprising employing the synthetic coal as a carbon source within a combustive thermal energy generation system.
11 . The method of claim 7 further comprising gasifying the synthetic coal.
12 . The method of claim 12 wherein gasifying the synthetic coal produces a synthesis gas.
13 . The method of claim 7 further comprising providing the synthetic coal as a source of coke for the manufacture of steel.
14 . A synthetic coal produced by the process comprising the steps of:
a) obtaining an fermentation residue; b) subjecting said fermentation residue to hydrothermal carbonization in an aqueous solution at a temperature and a pressure sufficient to form a synthetic coal solid and a liquid component.
15 . The synthetic coal of claim 14 wherein the process further comprises separating the synthetic coal solid from the liquid component.
16 . The synthetic coal of claim 14 wherein the temperature is between about 170° C. and about 225° C.
17 . The synthetic coal of claim 14 wherein the pressure is between about 0.8 and about 2.41 MPa.
18 . The synthetic coal of claim 14 wherein the process further comprises combining the fermentation residue with an acidic buffer.
19 . The synthetic coal of claim 14 wherein the fermentation residue is produced from corn based ethanol production.
20 . The synthetic coal of claim 14 wherein the synthetic coal has an ash content of <1% by weight.Join the waitlist — get patent alerts
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