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dc.contributor.advisorHoltzapple, Mark T
dc.creatorZentay, Agustin Nicholas
dc.date.accessioned2015-01-09T20:27:21Z
dc.date.available2015-01-09T20:27:21Z
dc.date.created2014-05
dc.date.issued2014-05-05
dc.date.submittedMay 2014
dc.identifier.urihttp://hdl.handle.net/1969.1/152675
dc.description.abstractTransportation fuels are the major driver for fossil fuel production, a burden that many countries have tried to ease by blending fossil fuels with biofuel substitutes such as ethanol. Current U.S. ethanol production relies on fermentation of starchy biomass (e.g., corn), which competes with food. Using lignocellulose avoids competition with food; however, it is difficult to digest using traditional batch saccharification. This work investigates countercurrent saccharification as an alternative that reduces enzyme requirements. Compared to baseline yields for standard batch saccharification, countercurrent saccharification reduces enzyme requirements by 5 to 37 times. Initial studies identified Solka-Floc as an acceptable substrate to represent treated biomass; it is readily available and reliably consistent from sample to sample. To measure yields, batch saccharifications were performed at various enzyme loadings and reaction times. Two relatively low enzyme concentrations were selected for further study: 2 and 5 mg protein/g biomass, or 2.6 and 6.4 mg protein/g glucan, respectively. Both of the selected loadings are below levels suggested for commercial use. For each enzyme loading tested, a multi-stage, semi-continuous countercurrent train was constructed. The first experiments used trains consisting of eight 1-L bottles loaded with α-cellulose, using the same concentrations as the batch experiments. Liquid and solid phases were countercurrently contacted, with transfers of each phase occurring every second day for approximately 4‒6 weeks, until steady-state operation was maintained for at least 10 days. At 2 and 5 mg/g enzyme loadings, total sugar yields reached 55.9% and 85.3%, respectively. A follow up study using 16 bottles and 2 mg/g loading produced total sugar yields of 73.4%. In the interest of future scale-up, alternatives to the cycloheximide and tetracycline antibiotic cocktail were investigated. Preliminary results suggest that chloroform or a volatile essential plant oil may be effective. Future work is needed to confirm the antimicrobial strength of these compounds at low concentrations, which is needed to limit enzyme inhibition.
dc.format.mimetypeapplication/pdf
dc.language.isoen
dc.subjectcountercurrent
dc.subjectenzymes
dc.subjectenzymatic
dc.subjectsaccharification
dc.subjectsugar
dc.subjectbiofuels
dc.subjectethanol
dc.titleCountercurrent Enzymatic Saccharification of Lignocellulosic Biomass and Improvements Over Batch Operation
dc.typeThesis
thesis.degree.departmentChemical Engineering
thesis.degree.disciplineChemical Engineering
thesis.degree.grantorTexas A & M University
thesis.degree.nameMaster of Science
thesis.degree.levelMasters
dc.contributor.committeeMemberGlover, Charles J
dc.contributor.committeeMemberCapareda, Sergio
dc.type.materialtext
dc.date.updated2015-01-09T20:27:21Z
local.etdauthor.orcid0000-0002-1236-4894


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