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        <datestamp>2023-07-10</datestamp>
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        <thesis xmlns="http://www.ndltd.org/standards/metadata/etdms/1.1/" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" xmlns:dc="http://purl.org/dc/elements/1.1/" xsi:schemaLocation="http://www.ndltd.org/standards/metadata/etdms/1.1/ http://www.ndltd.org/standards/metadata/etdms/1.1/etdms11.xsd http://purl.org/dc/elements/1.1/ http://www.ndltd.org/standards/metadata/etdms/1.1/etdmsdc.xsd">
          <dc:contributor>Singh, Vijay</dc:contributor>
          <dc:creator>Kaur, Prabhjot</dc:creator>
          <dc:date>2011-01-14T22:51:25Z</dc:date>
          <dc:date>2011-01-14T22:51:25Z</dc:date>
          <dc:date>2011-01-14T22:51:25Z</dc:date>
          <dc:description>In conventional dry grind process, high glucose concentrations (&gt;15% w/w) and
liquefaction viscosities restrict slurry solids contents to 30 to 32% w/w. High slurry solids
fermentations (above 33%) are important in reducing energy costs; decreased water input results
in less evaporation, dehydration and distillation. There are numerous challenges associated with
high solids fermentations: high slurry viscosities, high glucose concentrations that exert osmotic
stress on yeast and high ethanol concentrations that result in loss of cell viability. The objective
was to determine an economical and process efficient enzyme combination to be employed during
simultaneous saccharification and fermentation (SSF) to reduce slurry viscosities and glucose
concentrations at high solids. We also evaluated effects of nitrogen source and dose on high solids
fermentation. The enzyme combination we considered for this study consisted of granular starch
hydrolyzing enzymes (GSHE), alpha-amylase component of GSHE (GSHE AA) and
glucoamylase (GA).
In this study, we showed that using low temperatures (55 C) and a combination of phytase
and alpha-amylase during liquefaction reduced slurry viscosities at 35% solids by 81% compared
to the conventional process. We compared eighteen SSF enzyme treatments to optimize each
GSHE, GSHE AA and GA. These SSF enzyme treatments included two enzyme combinations: 1)
GA and GSHE and 2) GA and GSHE AA, with different levels of enzyme concentrations. For all
treatments except control, liquefaction (55 C for 90 min) was conducted at 35% solids using a
formulation of alpha-amylase and phytase. SSF (32 C for 72 hr) was carried out using enzyme
treatments, urea and yeast. The treatment containing 0.5 L glucoamylase and 1.25 L GSHE per g
dry corn resulted in the highest fermentation efficiencies (92%) and ethanol yields (418 L/tonne).
The control treatment resulted in the lowest fermentation efficiencies (84%) and ethanol yields
(381 L/tonne). The above mentioned enzyme treatment also resulted in 34% lower peak glucose
ii
concentrations (9.87% w/v) compared to control treatment (13.49% w/v).
Nitrogen source and dose effects were determined at 35 and 40% solids using modified
process. Three nitrogen sources (urea, ammonium sulfate, glutamine) and protease were
compared for ethanol yields and other fermentation parameters. Urea and protease resulted in
similar ethanol yields. However, fermentation rates were higher for protease during initial 12 hr
of fermentation.
Effects of urea and protease levels were evaluated at 35 and 40% solids. At 35% solids,
2.16 mg urea and 0.71 mg protease resulted in highest fermentation efficiencies and ethanol
yields. However at 40% solids, 4.32 and 2.16 mg urea and 0.71 mg protease gave highest
fermentation efficiencies and ethanol yields. At 35 and 40% solids, increasing protease levels
from 0.71 to 1.42 mg reduced fnal ethanol concentrations, ethanol yields and fermentation
effciencies. Increasing solids content from 35 to 40% decreased fermentation effciencies and
simultaneously reduced ethanol yields across all urea and protease levels.</dc:description>
          <dc:description>Item withdrawn by Mark Zulauf (zulauf@illinois.edu) on 2010-12-08T17:58:30Z
Item was in collections:
University of Illinois Theses &amp; Dissertations (ID: 1)
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          <dc:identifier>http://hdl.handle.net/2142/18455</dc:identifier>
          <dc:language>en</dc:language>
          <dc:rights>c 2010 by Prabhjot Kaur. All rights reserved.</dc:rights>
          <dc:subject>Corn</dc:subject>
          <dc:subject>high solids</dc:subject>
          <dc:subject>fermentation</dc:subject>
          <dc:title>Enzymatic and process technologies to increase corn dry grind slurry solids</dc:title>
          <dc:date>2010-12</dc:date>
          <degree>
            <programCode>10KS5163MS</programCode>
            <program>MS: Agr &amp; Biol Engr -UIUC</program>
            <department>Engineering Administration</department>
            <departmentCode>1227</departmentCode>
            <discipline>Agricultural &amp; Biological Engr</discipline>
            <disciplineCode>5163</disciplineCode>
            <grantor>University of Illinois at Urbana-Champaign</grantor>
            <level>Thesis</level>
            <name>M.S.</name>
          </degree>
        </thesis>
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