METHODS FOR CONDITIONING PRETREATED BIOMASS
Methods for producing ethanol from cellulosic biomass and, in particular, methods for conditioning pretreated biomass are disclosed. In some embodiments, pretreated biomass is contacted with a cooling fluid in a flash vessel to cool the biomass. The amount of alkaline solution contacted with the biomass may be based on the pH of partially hydrolyzed pretreated biomass in a liquefaction bioreactor.
1 . A method for conditioning pretreated biomass, the method comprising:
discharging biomass from a pretreatment digester to a flash vessel to flash vapor from the biomass, the biomass forming a bed in the flash vessel; and
introducing a cooling fluid into the flash vessel to cool the biomass, the cooling fluid having a temperature less than about 25° C.
2 . The method as set forth in claim 1 wherein the cooling fluid is introduced into the flash vessel at a point opposite the bed.
3 . The method as set forth in claim 1 wherein the flash vessel comprises an agitator for mixing and distributing the biomass onto an extraction screw for removing biomass from the flash vessel, the cooling fluid being added to the flash vessel above the agitator.
4 . The method as set forth in claim 1 wherein the cooling fluid has a temperature less than about 20° C.
5 . The method as set forth in claim 1 wherein the cooling fluid has a temperature less than about 15° C.
6 . The method as set forth in claim 1 wherein the cooling fluid contains an alkali for increasing the pH of the biomass.
7 . The method as set forth in claim 6 wherein the concentration of alkali in the cooling fluid is adjusted based on at least one of (1) the rate of addition of biomass into the pretreatment digester and (2) a measured pH of biomass downstream of the flash vessel.
8 . The method as set forth in claim 1 wherein the rate of cooling fluid introduced into the flash vessel is adjusted based on at least one of (1) the rate of addition of biomass into the pretreatment digester and (2) a measured total solids of biomass downstream of the flash vessel.
9 . The method as set forth in claim 1 further comprising:
discharging the biomass from the flash vessel;
introducing the discharged biomass into a neutralization mixer; and
introducing an alkaline process stream into the neutralization mixer, the alkaline process stream having a temperature less than about 25° C.
10 . The method as set forth in claim 1 wherein the residence time of biomass above the entry point of the cooling fluid in the vessel is at least about 10 seconds.
11 . The method as set forth in claim 1 wherein the residence time of biomass above the entry point of the cooling fluid in the vessel is at least about 30 seconds.
12 . The method as set forth in claim 1 wherein the residence time of biomass above the entry point of the cooling fluid in the vessel is at least about 1 minute.
13 . The method as set forth in claim 1 further comprising:
contacting a biomass feedstock with an aqueous acid solution to prepare an acid-impregnated biomass stream, the aqueous acid solution having an acid concentration of less than about 5 wt %; and
introducing the acid-impregnated biomass stream into the pretreatment digester.
14 . The method as set forth in claim 1 comprising discharging pretreated biomass from the flash vessel, the temperature of the pretreated biomass being about 90° C. or less.
15 . The method as set forth in claim 1 comprising discharging pretreated biomass from the flash vessel, the temperature of the pretreated biomass being about 70° C. or less.
16 . A method for conditioning pretreated biomass, the method comprising:
discharging pretreated biomass from a pretreatment digester;
introducing the pretreated biomass discharged from the digester into a neutralization mixer;
introducing an alkaline solution into the neutralization mixer to adjust the pH of the biomass;
adding enzyme to the pH-adjusted pretreated biomass;
introducing the enzyme-containing pretreated biomass into a liquefaction bioreactor to partially hydrolyze the pretreated biomass;
measuring the pH of the partially hydrolyzed pretreated biomass in the liquefaction bioreactor; and
adjusting at least one of (1) the amount of alkaline solution introduced into the neutralization mixer and (2) the concentration of alkali in the alkaline solution based on the measured pH of the partially hydrolyzed pretreated biomass in the liquefaction bioreactor.
17 . The method as set forth in claim 16 wherein the concentration of alkali in the alkaline solution is adjusted based on the measured pH of the partially hydrolyzed pretreated biomass in the liquefaction bioreactor.
18 . The method as set forth in claim 16 wherein the amount of alkaline solution introduced into the neutralization mixer is adjusted based on the total solids content of the pH-adjusted pretreated biomass.
19 . The method as set forth in claim 16 wherein the pH of the partially hydrolyzed pretreated biomass is measured at the discharge of the liquefaction bioreactor.
20 . The method as set forth in claim 16 further comprising:
contacting a biomass feedstock with an aqueous acid solution to prepare an acid-impregnated biomass stream, the aqueous acid solution having an acid concentration of less than about 5 wt %; and
introducing the acid-impregnated biomass stream into the pretreatment digester.
21 . A method for conditioning pretreated biomass, the method comprising:
discharging pretreated biomass from a pretreatment digester into a flash vessel;
introducing an alkaline solution into the flash vessel to adjust the pH of the biomass;
adding enzyme to the pH-adjusted pretreated biomass;
introducing the enzyme-containing pretreated biomass into a liquefaction bioreactor to partially hydrolyze the pretreated biomass;
measuring the pH of the partially hydrolyzed pretreated biomass in the liquefaction bioreactor; and
adjusting at least one of (1) the amount of alkaline solution introduced into the flash vessel and (2) the concentration of alkali in the alkaline solution based on the measured pH of the partially hydrolyzed pretreated biomass in the liquefaction bioreactor.
22 . The method as set forth in claim 21 wherein the concentration of alkali in the alkaline solution is adjusted based on the measured pH of the partially hydrolyzed pretreated biomass in the liquefaction bioreactor.
23 . The method as set forth in claim 21 wherein the amount of alkaline solution introduced into the flash vessel is adjusted based on the total solids content of the pH-adjusted pretreated biomass.
24 . The method as set forth in claim 21 wherein the pH of the partially hydrolyzed pretreated biomass is measured at the discharge of the liquefaction bioreactor.
25 . The method as set forth in claim 21 further comprising:
contacting a biomass feedstock with an aqueous acid solution to prepare an acid-impregnated biomass stream, the aqueous acid solution having an acid concentration of less than about 5 wt %; and
introducing the acid-impregnated biomass stream into the pretreatment digester.