The requirement of pressurized vessel at hydrolysis temperature (~2.7 bar at 135°C), complex handling of high concentrations of sulfuric, and difficulty of handling water-insoluble solids associated with the use of some common neutralization agents (e.g. calcium hydroxide) could increase the overall cost of production of biofuel and biochemicals from biomass. Furthermore, a high sulfuric acid concentration could be detrimental to the downstream fermentation unit if it ends up as a neutralized salt surpassing the admissible toxicity level for the fermenting microorganisms to remain reactive for glucose conversion.
We have a developed a process for hydrolyzing pyrolytic bio-oil at relatively mild conditions, with temperatures as low as 95-105°C and sulfuric acid concentrations of only 50-150 mM. A response surface method was used to optimize the hydrolysis reaction conditions for levoglucosan. Overall, a 95% conversion of levoglucosan could be achieved and a high concentration of glucose (160.8 g/L) could be produced at 115°C using only 150 mM sulfuric acid at 3 h of reaction time. Modeling of bio-oil hydrolysis shows a good overall fit with first order conversion of levoglucosan to glucose with possibility of other C6 anhydrosugars conversion to excess glucose.