Lignocellulosic ethanol production without enzymes–technoeconomic analysis of ionic liquid pretreatment followed by acidolysis. Oleskowicz-Popiel, P., Klein-Marcuschamer, D., Simmons, B. A., & Blanch, H. W. Bioresource Technology, 158:294–9, April, 2014. doi abstract bibtex Deconstruction of polysaccharides into fermentable sugars remains the key challenge in the production of inexpensive lignocellulosic biofuels. Typically, costly enzymatic saccharification of the pretreated biomass is used to depolymerize its cellulosic content into fermentable monomers. In this work, we examined the production of lignocellulosic recovery, a process that does not require the use of enzymes to produce fermentable sugars. In the base case, the minimum ethanol selling price (MESP) was \$8.05/gal, but with improved performance of the hydrolysis, extraction, and sugar recovery, the MESP can be lowered to \$4.00/gal. Additionally, two scenarios involving lignin recovery were considered. Although the results based on current assumptions indicate that this process is expensive compared to more established technologies, improvements in the hydrolysis yield, the sugar extraction efficiency, and the sugar recovery were shown to result in more competitive processes.
@article{oleskowicz-popiel_lignocellulosic_2014,
title = {Lignocellulosic ethanol production without enzymes--technoeconomic analysis of ionic liquid pretreatment followed by acidolysis},
volume = {158},
issn = {1873-2976 (Electronic) 0960-8524 (Linking)},
doi = {10.1016/j.biortech.2014.02.016},
abstract = {Deconstruction of polysaccharides into fermentable sugars remains the key challenge in the production of inexpensive lignocellulosic biofuels. Typically, costly enzymatic saccharification of the pretreated biomass is used to depolymerize its cellulosic content into fermentable monomers. In this work, we examined the production of lignocellulosic recovery, a process that does not require the use of enzymes to produce fermentable sugars. In the base case, the minimum ethanol selling price (MESP) was \$8.05/gal, but with improved performance of the hydrolysis, extraction, and sugar recovery, the MESP can be lowered to \$4.00/gal. Additionally, two scenarios involving lignin recovery were considered. Although the results based on current assumptions indicate that this process is expensive compared to more established technologies, improvements in the hydrolysis yield, the sugar extraction efficiency, and the sugar recovery were shown to result in more competitive processes.},
language = {eng},
journal = {Bioresource Technology},
author = {Oleskowicz-Popiel, P. and Klein-Marcuschamer, D. and Simmons, B. A. and Blanch, H. W.},
month = apr,
year = {2014},
pages = {294--9}
}
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