(617f) Secondary Hydrolysis of Pretreatment Liquor Obtained From Continuous High-Solids Dilute-Acid Pretreatment of Corn Stover | AIChE

(617f) Secondary Hydrolysis of Pretreatment Liquor Obtained From Continuous High-Solids Dilute-Acid Pretreatment of Corn Stover

Authors 

Shi, S. - Presenter, Auburn University
Lee, Y. Y. - Presenter, Auburn University
Elander, R. - Presenter, National Renewable Energy Laboratory
Nagle, N. - Presenter, National Renewable Energy Laboratory


Dilute-acid pretreatment is one of the most promising process options applicable for various lignocellulosic biomass feedstocks. NREL has developed an efficient continuous pretreatment reactor that can be operated with high-solid charge and with short residence time. Using this reactor, NREL has investigated extensively on pretreatment of corn stover. Because of these unique features, the pretreatment liquors produced from this reactor contain high level of hemicellulose sugars, the concentration surpassing 10 wt. %. On the other hand, the short residence time and low-acid condition limits the hydrolysis of hemicellulose. The pretreatment liquor obtained from this reactor thus contains relatively high amount of xylose oligomers, typically in the range of 10-40% of the total sugar. In order to fully utilize the sugars in the pretreatment liquor, oligomers need to be hydrolyzed to monomers. However, the secondary hydrolysis of this liquor was found to be much more difficult than hydrolysis of xylose oligomers in clean environment. This investigation was undertaken to verify the factors inhibiting the acid-catalyzed oligomer hydrolysis and to establish the comprehensive kinetics recognizing all reactions occurring under the heavily contaminated environment. For this purpose, the secondary hydrolysis was experimentally studied using rapid-heating small-scale batch reactors. The experiments were done for pretreatment liquor and for clean xylose oligomers. The comparison of the results indicated that the a significant fraction oligomers may be bound to lignin fragments, and some of it may also exist in branched form. The kinetic model was set up recognizing different forms of oligomers (linear, branched, and lignin-oligomer complex), and additional reactions of xylose including decomposition, and reversion to xylose dimmers. Model verification was performed using batch hydrolysis data, xylose decomposition data, the data obtained from reversion reaction. The results of the model verification are presented and how the model can be used to determine the optimum operating conditions are discussed.