Process Design Report for Stover Feedstock: Lignocellulosic Biomass to Ethanol Process Design and Economics Utilizing Co-Current Dilute Acid Prehydrolysis and Enzymatic Hydrolysis for Corn Stover

By A. Aden, M. Ruth, K. Ibsen, J. Jechura, K. Neeves, J. Sheehan, B. Wallace, L. Montague, A. Slayton, J. Lukas. 2002

439 citations recorded by the source corpus.

Subfields: Biomedical Engineering, Molecular Biology

View Paper: https://www.semanticscholar.org/paper/cabe9466e2884abbc9a95876ca71cfa30380fc12

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Citations in the corpus

The economics of current and future biofuels (2009, methodology): “As documented (Wooley et al. 1999; Aden et al. 2002; Phillips et al. 2007), capital costs are developed for each piece of equipment using a number of sources, including vendor quotations (for more specialized equipments), costing software estimates (for simpler equipment such as pumps and tanks),…”
Commercial cellulosic ethanol: The role of plant-expressed enzymes (2009, methodology): “The challenge here is identifying microorganisms that can carry out this fermentation efficiently, such as the engineered Zymononas mobilis strain used by the US NREL in their techno-economic process analysis (Aden et al. 2002, Aden 2008).”
An economic and environmental comparison of a biochemical and a thermochemical lignocellulosic ethanol conversion processes (2009, methodology): “…not measured experimentally, but is used within the model to close material balance of the dry wt biomass to 100% Italicized values helps to separate the assumed moisture content of the feedstock from the rest of the dry weight composition adjusted for the weight of the ash (Aden et al. 2002).”
Lignocellulosic agriculture wastes as biomass feedstocks for second-generation bioethanol production: concepts and recent developments (2014, background): “For pretreatment of lignocellulosics, several physical, physicochemical and biological processes have been developed that improve lignocellulose digestibility in very different ways (Aden et al. 2002; Sun and Cheng 2002; Wyman et al. 2005a, b).”
The challenge of enzyme cost in the production of lignocellulosic biofuels. (2012, methodology): “Equipment and raw material costs (with the exception of poplar and glucose costs) were from (Aden et al., 2002; Kazi et al., 2010; Wooley et al., 1999), updated to 2007 dollars using the CEPCI and ICI indices, respectively for equipment and materials.”
Lignocellulosic Materials Into Biohydrogen and Biomethane: Impact of Structural Features and Pretreatment (2013, background): “Finally, pretreatment has to be as cost-effective as possible because several economic models show that pretreatment is an essential operation requiring a dedicated unit in a lignocellulosic biorefinery, accounting for 16–19% of total cost equipment (Aden et al., 2002).”
Renewable Fuel Standard: Potential Economic and Environmental Effects of U.S. Biofuel Policy (2012, methodology): “The conversion cost data used in the BioBreak analysis are based on laboratory or pilot-scale performance information and estimated investment and operating cost data for an optimized nth biorefinery that uses biochemical conversion of corn stover to ethanol (Aden et al., 2002).”
Economic Analysis of Cellulase Production Methods for Bio-Ethanol (2007, background): “According to Aden et al. (2002), the price variables for paper pulp and cellulose powder have an exponential distribution.”