Subscriber access provided by Yale University Library
Article
REDUCING BACTERIAL CONTAMINATION IN FUEL ETHANOL FERMENTATIONS BY OZONE TREATMENT OF UNCOOKED CORN MASH Mary L. Rasmussen, Jacek A. Koziel, Jay-lin Jane, and Anthony L Pometto J. Agric. Food Chem., Just Accepted Manuscript • DOI: 10.1021/acs.jafc.5b00563 • Publication Date (Web): 12 May 2015 Downloaded from http://pubs.acs.org on May 18, 2015
Just Accepted “Just Accepted” manuscripts have been peer-reviewed and accepted for publication. They are posted online prior to technical editing, formatting for publication and author proofing. The American Chemical Society provides “Just Accepted” as a free service to the research community to expedite the dissemination of scientific material as soon as possible after acceptance. “Just Accepted” manuscripts appear in full in PDF format accompanied by an HTML abstract. “Just Accepted” manuscripts have been fully peer reviewed, but should not be considered the official version of record. They are accessible to all readers and citable by the Digital Object Identifier (DOI®). “Just Accepted” is an optional service offered to authors. Therefore, the “Just Accepted” Web site may not include all articles that will be published in the journal. After a manuscript is technically edited and formatted, it will be removed from the “Just Accepted” Web site and published as an ASAP article. Note that technical editing may introduce minor changes to the manuscript text and/or graphics which could affect content, and all legal disclaimers and ethical guidelines that apply to the journal pertain. ACS cannot be held responsible for errors or consequences arising from the use of information contained in these “Just Accepted” manuscripts.
Journal of Agricultural and Food Chemistry is published by the American Chemical Society. 1155 Sixteenth Street N.W., Washington, DC 20036 Published by American Chemical Society. Copyright © American Chemical Society. However, no copyright claim is made to original U.S. Government works, or works produced by employees of any Commonwealth realm Crown government in the course of their duties.
Page 1 of 39
Journal of Agricultural and Food Chemistry
POET ground corn
POET corn slurry (pH 4.0) Urea (0.03% w/w)
Slurry (30 min, room temp.)
pH adjustment, if any (pH 4–5) Lactobacillus plantarum (ground corn only)
Ozonation/aeration Novozyme 50009 (0.11% v/w) Ethanol Red yeast (0.25% w/w)
SSF (stationary, 27°C, daily sampling)
Figure 1. Corn mash preparation, ozonation/aeration, and fermentation using POET ground corn and POET corn slurry.
ACS Paragon Plus Environment
Journal of Agricultural and Food Chemistry
1 2 3 4 5 6 7 8 9 10
REDUCING BACTERIAL CONTAMINATION IN FUEL ETHANOL FERMENTATIONS BY OZONE TREATMENT OF UNCOOKED CORN MASH
Mary L. Rasmussena,b, Jacek A. Kozielc,a,d, Jay-lin Janed, Anthony L. Pometto IIIe,f a
11
Department of Civil, Construction, and Environmental Engineering, Iowa State University, Ames, IA 50011
12
b
Biorenewable Resources and Technology Program, Iowa State University, Ames, IA 50011
13
c
Department of Agricultural and Biosystems Engineering, Iowa State University, Ames, IA 50011
14
(ORCID #0000-0002-2387-0354)
15
d
Department of Food Science and Human Nutrition, Iowa State University, Ames, IA 50011
16
e
Department of Food, Nutrition, and Packaging Sciences, Clemson University, Clemson, SC
17 18 19
29634 f
Corresponding author: Professor Anthony L. Pometto III, 223 Poole Agricultural Center, Clemson SC 29634-0316, Phone 864-656-4382; Fax 864-656-0331; E-mail
[email protected] 20
1 ACS Paragon Plus Environment
Page 2 of 39
Page 3 of 39
21
Journal of Agricultural and Food Chemistry
Abstract
22
Ozonation of uncooked corn mash from the POET BPXTM process was investigated as a
23
potential disinfection method for reducing bacterial contamination prior to ethanol fermentation.
24
Corn mash (200 g) was prepared using POET ground corn and POET corn slurry and was
25
ozonated in 250-mL polypropylene bottles. Lactic and acetic acid levels were monitored daily
26
during the fermentation of ozonated, aerated, and non-treated corn mash samples to evaluate
27
bacterial activity. Glycerol and ethanol contents of fermentation samples were checked daily to
28
assess yeast activity. No yeast supplementation, no addition of other antimicrobial agents (such
29
as antibiotics), and spiking with a common lactic acid bacterium found in corn ethanol plants,
30
Lactobacillus plantarum, amplified the treatment effects.
31
The laboratory-scale ozone dosages ranged from 26–188 mg/L, with very low estimated
32
costs of $0.0008 to $0.006 per gallon ($0.21 to $1.6 per m3) ethanol. Ozonation was found to
33
decrease the initial pH of ground corn mash samples, which could reduce the sulfuric acid
34
required to adjust the pH prior to ethanol fermentation. Lactic and acetic acid levels tended to be
35
lower for samples subjected to increasing ozone dosages, indicating less bacterial activity. The
36
lower ozone dosages in the range applied achieved higher ethanol yields. Preliminary
37
experiments on ozonating POET corn slurry at low ozone dosages were not as effective as using
38
POET ground corn, possibly because corn slurry samples contained recycled antimicrobials from
39
the backset. The data suggest additional dissolved and suspended organic materials from the
40
backset consumed the ozone or shielded the bacteria.
41
Keywords: ozonation; no-cook; BPXTM process; corn mash; fuel ethanol; bacteria; dry-grind
42
ethanol; lactic acid
2 ACS Paragon Plus Environment
Journal of Agricultural and Food Chemistry
43
Introduction
44
POET leads the fuel ethanol industry in streamlining corn dry milling to improve ethanol
45
production efficiency, as well as their feed coproduct, Dakota Gold BPXTM distiller grains. The
46
efficient BPXTM, or no-cook, process involves raw starch hydrolysis that, like the conventional
47
process, adds enzymes to convert starch to sugars and adds yeast to ferment sugars to ethanol,
48
but without the cooking step. 1 The BPXTM process is now used by 24 of the 27 POET
49
biorefineries. POET produces over 1.5×109 gal (5.7×106 m3) of ethanol annually in a network
50
spanning seven Midwestern states.
51
The POET BPXTM process for dry-grind corn ethanol production has important
52
advantages over the conventional process. The energy-intensive liquefaction and cooking steps
53
are omitted, thus reducing plant energy requirements by 8–15%. 1 The BPXTM process achieves
54
higher ethanol yields by improving starch accessibility, lowers volatile organic carbon (VOC)
55
emissions, cuts cooling water needs, and enhances the nutrient quality, flowability and anti-
56
caking properties of the distillers dried grains with solubles (DDGS) coproduct. Amino acid
57
digestibility in DDGS samples varies considerably among conventional ethanol facilities,
58
attributable to heat damage from corn mash cooking and DDGS drying. 2-5 Heat damage is
59
responsible for the lower amino acid digestibility in DDGS than in corn grain. 4, 6 Removing the
60
cooking step, therefore, improves the feed quality of Dakota Gold BPXTM DDGS over
61
conventional DDGS by reducing heat damage of the protein. 7
62
Unlike most beverage alcohols, fuel ethanol fermentations are not conducted under pure
63
culture conditions. 8 High-temperature jet cooking (90–165°C) in the conventional process not
64
only gelatinizes the corn starch, it helps reduce contamination and yield losses caused by
65
unwanted lactic acid bacteria (LAB). 9 Contamination in fuel ethanol fermentations originates
3 ACS Paragon Plus Environment
Page 4 of 39
Page 5 of 39
Journal of Agricultural and Food Chemistry
66
from bacteria present on the corn from the fields. 10 Bacteria compete with yeast for nutrients –
67
glucose, trace minerals, vitamins, and free amino nitrogen – and lower ethanol yields by
68
diverting glucose to lactic and acetic acids, which are inhibitory compounds to yeast. 11-13 In
69
addition to yield losses by chronic LAB contamination, acute infections arise unpredictably and
70
can result in plant shut-downs for cleaning – an expensive loss in productivity. 8, 13, 14
71
Gram-positive and gram-negative bacterial isolates from fuel ethanol production include
72
species of Pediococcus, Enterococcus, Acetobacter, Gluconobacter, Clostridium, and
73
Lactobacillus. 8, 15 Lactobacilli sp. are the most prevalent in the industry and are ubiquitous in
74
nature. In a study of two commercial dry grind ethanol plants by Skinner and Leathers, 8 the
75
genus Lactobacillus was isolated most frequently, representing 38 and 77% of total bacterial
76
isolates from the first and second plants, respectively. Gram-positive LAB are ethanol-tolerant,
77
grow faster than yeast, and produce organic acids which inhibit yeast.
78
During this research bacterial growth was controlled at POET biorefineries potentially by
79
dosing with antibiotic and antimicrobial agent and by operation at lower pH levels (pH~ 4.2).
80
Conventional ethanol plants, despite jet cooking, also add antibiotics to fight chronic or acute
81
bacterial infections. 8, 16-18 If no antibiotics are used, it is common for a facility to lose 1–5% of
82
its potential ethanol yield. 10 Rising concerns about the use of antibiotics and the emergence of
83
antibiotic-resistant bacteria is creating a demand for alternative methods of controlling bacteria.
84
Cleaning and sanitation are important microbial control measures in the corn ethanol
85
industry. Infections in process tanks and continuous yeast propagators, as well as resistant
86
biofilms within the process train, can continually reintroduce bacterial contaminants into the
87
fermentors. 8, 19 Large yeast inoculums (≥2% [v/v]) help control contamination during
4 ACS Paragon Plus Environment
Journal of Agricultural and Food Chemistry
88
fermentations; however, yeast growth and fermentation rates are still reduced by high lactobacilli
89
concentrations. 20
90
Penicillin and virginiamycin are the antibiotics available commercially for fuel ethanol
91
production. 15, 21 Virginiamycin, produced by Streptomyces virginiae, has had limited use in
92
human medicine but extensive use as a growth-promoting additive in animal feed. 22 The
93
recommended dose of virginiamycin in fuel ethanol fermentations is 0.25–2.0 ppm. 23 The use
94
of antibiotics has limitations. Commercial antibiotic applications are essentially selection
95
experiments for resistant microorganisms. Hynes et al. 23 observed reductions in the
96
effectiveness of virginiamycin after extended fermentations, possibly resulting from its
97
breakdown by lactobacilli. 24 Lactobacillus sp. with higher tolerance to virginiamycin have been
98
isolated from fuel ethanol plants that dose with virginiamycin. Moreover, bacterial isolates have
99
emerged with resistance to both virginiamycin and penicillin. 15, 25
100
Hop acids offer a natural alternative to antibiotics for fuel ethanol production. 10 Many
101
of the organic acids found in hops exhibit antimicrobial activities. Hop-compounds inhibit
102
growth by disrupting the trans-membrane pH gradient of microbes. 26, 27 Hops have long been
103
used in the brewing industry to contribute to the flavor of beer, by adding bitterness and aroma,
104
and to improve product shelf-life. IsoStabTM, a liquid hop extract, is a commercially-available
105
product for fuel ethanol applications. U.S. producers using IsoStabTM have obtained higher
106
ethanol yields with less fluctuation.
107
A variety of disinfectants have been investigated on lab scale for fuel ethanol
108
fermentations, including hydrogen peroxide, chlorine dioxide, potassium metabisulfite, 3,4,4’-
109
trichlorocarbanilide, and lactate with a lactate-tolerate yeast strain. 8, 28-33 Bacteria were
110
inhibited over yeast by these agents, but the effectiveness depended on the bacterial strain. 8
5 ACS Paragon Plus Environment
Page 6 of 39
Page 7 of 39
Journal of Agricultural and Food Chemistry
111
Chlorine dioxide and ozonation are common alternatives to chlorination for disinfection of
112
drinking water. Meneghin et al. 30 evaluated the effect of chlorine dioxide against bacteria
113
prevalent in ethanol fermentations (e.g., Lactobacillus plantarum and L. fermentum). The
114
minimum inhibitory concentrations (MIC) for chlorine dioxide on the bacteria and on the yeast
115
inoculum were determined using nutrient media; the effectiveness in nutrient media is likely
116
different from that in the high suspended-solids corn mash at fuel ethanol plants. The MICs
117
ranged from 10–125 ppm for the bacterial strains tested; L. plantarum had the highest MIC of
118
125 ppm. Yeast growth was also affected at chlorine dioxide concentrations over 50 ppm.
119
Ozone is a microbial inhibitor that is considered an alternative to chlorine and hydrogen
120
peroxide in food applications. 34 The rate of microbial inactivation is affected by the several
121
environmental factors (concentration of organic compounds, the physiological state of the
122
microorganism, pH of the medium, temperature). 35 Thus it has had mixed success in the food
123
industry. Garcia-Cubero et al., 36 illustrated the benefit of pretreatment of straw with ozone
124
resulted in a reduction in acid insoluble lignin (Klason Lignin) and improved enzymatic
125
hydrolysis of cellulose and hemicelluloses for biofuel production. Freitas-Silva et al., 37
126
demonstrated mycotoxin degradation by ozone use in corn on the cob, corn kernels, and corn and
127
rice powder. Miller et al., 38 reviewed the advantages and disadvantages of ozonation use for
128
fruits and vegetables preservation while Gerrity and Snyder 39 review its use in water reuse
129
applications. Thus, the application of ozone in dry grind corn ethanol production is needed.
130
Research Objectives
131
In this research ozone was used in place of antibiotics (e.g., Lactrol® and IsoStabTM) for
132
the control of bacterial contamination in ethanol (yeast) fermentations. Preliminary experiments
133
were subsequently performed using corn slurry to evaluate the effectiveness of ozonation for
6 ACS Paragon Plus Environment
Journal of Agricultural and Food Chemistry
134
reducing bacterial contamination under conditions more similar to plant operation, including the
135
contributions of recycled water sources.
7 ACS Paragon Plus Environment
Page 8 of 39
Page 9 of 39
Journal of Agricultural and Food Chemistry
136
Materials and Methods
137
Corn mash preparation
138
Ground corn and corn slurry were obtained from POET Biorefining in Jewell, IA in the
139
fall and spring of 2007 and 2008. The corn slurry obtained from POET contains the ground corn
140
in a slurry with recycled water streams, such as backset. Figure1 illustrates the corn mash
141
preparation, ozone treatment, and simultaneous saccharification and fermentation (SSF)
142
procedures. Corn mash was prepared in 250-mL polypropylene (PP) bottles with 35% (w/w)
143
ground corn (200 g mash per bottle) and deionized water or with 200 g corn slurry per bottle.
144
Urea was added (0.03% [w/w]) as a N source. The final corn mash volume was 186 mL per
145
bottle. Bottles were shaken for 30 min at 250 rpm and room temperature to slurry contents. The
146
pH was adjusted to 5.0 in select experiments. In preliminary work (pH 4.2), all controls with and
147
without Lactrol® and/or IsoStabTM added had similar values for lactic and acetic acids, glycerol,
148
and ethanol, which indicated minimal bacterial contamination even without ozonation (results
149
not shown). Therefore, no antibiotics or other antimicrobials (i.e., Lactrol® or IsoStabTM) were
150
added in these experiments to exemplify treatment effects of ozone. The POET corn slurry
151
experiments, however, potentially contained recycled antimicrobials contributed in the backset
152
from previous fermentations at the plant. Select samples were also LAB-spiked and/or not yeast-
153
supplemented to amplify the differences in treatment effects.
154
Microorganisms
155
Select corn mash samples were spiked with Lactobacillus plantarum, a lactic acid
156
bacterium, obtained from the American Type Culture Collection (ATCC 14917, Rockville, MD)
157
prior to ozone treatment. Stock cultures of L. plantarum were freeze-dried and stored previously
158
in sterile skim milk at 4 °C. Fermentis Ethanol Red (Lesaffre Yeast Corporation, Milwaukee,
8 ACS Paragon Plus Environment
Journal of Agricultural and Food Chemistry
159
WI), containing the yeast Saccharomyces cerevisiae, was added (0.5 g) after ozone treatment for
160
ethanol fermentation.
161
Ozonation
162
The laboratory-scale installation used to apply the ozone treatment is shown in Figure 2.
163
Ozone gas was generated from oxygen supplied by a compressed-air gas cylinder using a corona-
164
discharge ozone generator (TOG C2B, Trigon, Glasgow, Scotland). Moisture and hydrocarbon
165
traps (Restek, State College, PA) were placed between the ozone generator and compressed-air
166
cylinder to remove impurities in the feed gas. A mass flow controller (GLC17, Aalborg,
167
Orangeburg, NY) was used to control the gas flow rate.
168
Ozone gas was bubbled into the corn mash samples (200 g) in 250-mL PP bottles with a
169
flow rate of 500 mL/min. The ozone concentration in the gas phase was measured by the
170
potassium iodide titration method. 40 The ozone dose, or consumption, was calculated based on
171
ozone concentrations in the influent and effluent gas from the bottle over time. Corn mash
172
samples were ozonated and residual ozone in off-gas measured by titration after varying
173
ozonation times. This setup was used to determine the effects of different ozone dosages on
174
ethanol fermentation of corn mash samples prepared from ground corn or corn slurry. Aeration
175
treatment, as a control, was also performed using this equipment. The aeration and ozonation
176
procedures were the same (e.g., similar gas flow rate), but with the ozone generator turned off.
177 178
Ethanol fermentation
179
Following ozonation, raw starch hydrolyzing enzyme (Novozyme 50009, 0.11% [v/w])
180
and Ethanol Red (0.25% [w/w]) were added to ozonated, aerated, and non-treated corn mash
181
(Figure 1). Bottles were shaken for 2 min at 250 rpm to mix contents and incubated without
9 ACS Paragon Plus Environment
Page 10 of 39
Page 11 of 39
Journal of Agricultural and Food Chemistry
182
shaking at 27 °C (POET incubation temperature) until ethanol levels reached a plateau – up to
183
168 h. SSF samples were HPLC-analyzed on a daily basis.
184
Sample analyses
185
The ethanol, glycerol, lactic acid, and acetic acid contents of corn mash and SSF samples
186
were quantified using a Waters high pressure liquid chromatograph (HPLC) (Millipore
187
Corporation, Milford, MA). The HPLC system was equipped with a Waters Model 401
188
refractive index detector, column heater, automatic sampler, and computer controller. The
189
Aminex HPX-8711 column (300×7.8 mm, Bio-Rad Chemical Division, Richmond, CA)
190
separated sample constituents with a mobile phase of 0.012 N sulfuric acid, flow rate of 0.8
191
mL/min, injection volume of 20 µL, and column temperature of 65 °C. 41
192
Experiment sets
193
A pH experiment was conducted prior to fermentation. Aeration treatment was included
194
to confirm that ozonation, rather than aeration and mixing, lowered the initial corn mash pH
195
prior to fermentation (0 h).
196 197
The ethanol fermentation experiments reported in this publication are divided into three sets – two with POET ground corn and one with POET corn slurry – as outlined in Table 1.
198
POET ground corn (Experiment sets 1 & 2)
199
Two sets of fermentation experiments with ozone-treated corn mash prepared from
200
ground corn were performed. The first set included spiking with L. plantarum before ozone
201
treatment (0–188 mg/L) of corn mash; no yeast and no other antimicrobial agents were added to
202
select bottles to further amplify the treatment effects. The second set included ozonation and
203
aeration treatments of corn mash prior to ethanol fermentation. Select bottles were spiked with
204
L. plantarum. Fermentation experiments were conducted with aeration treatment as a control to
10 ACS Paragon Plus Environment
Journal of Agricultural and Food Chemistry
205
determine whether lower lactic acid contents in daily samples resulted from ozonation as a
206
disinfect/oxidant or from possible stimulatory effects of aeration on the yeast.
207
POET corn slurry (Experiment set 3)
208
A preliminary set of fermentation experiments was conducted with POET corn slurry to
209
assess the effectiveness of ozonation for reducing bacterial contamination under conditions more
210
similar to plant operation, including contributions of recycled water streams. The recycled
211
backset potentially contributed other antimicrobials in these experiments. Corn mash samples
212
were prepared with/without the addition of yeast, with the slurry initial pH of 4.0 and adjusted to
213
pH 5.0, and with/without ozone treatment, as shown in Table 1.
214 215 216 217
Statistical Analysis All treatments were performed in replicates of three. Statistical analysis was carried out
218
using the Statistical Analysis System package (SAS Computer Program Version 9.1.2, SAS
219
Institute Inc., Cary, NC). Student’s t-test analyses were performed on HPLC data sets to
220
determine statistical significance with a p value of 0.05.
11 ACS Paragon Plus Environment
Page 12 of 39
Page 13 of 39
Journal of Agricultural and Food Chemistry
221
Results and Discussion
222
Ozone dosages
223
The results of ozonating corn mash samples for various treatment times in order to
224
determine ozone consumption (i.e., ozone dosage) are illustrated in Figure 3. Ozone
225
consumption is the difference between the ozone applied to the corn mash, f(x), and the unused
226
ozone exiting the headspace of the treated corn mash over time (off-gas), g(x); it equals the green
227
area in Figure 3. The following fitted equations were used to calculate ozone
228
consumption/dosage:
229 230 231 232 233 234 235 236 237 238 239 240
Applied ozone (mg/min) Off-gas ozone (mg/min) Off-gas ozone (mg/min)
= f(x) = 0.996 = g(x) = 0.00319x+0.000538x2 = g(x) = 0.884
0 ≤ t ≤ 37.5 min 37.5 min ≤ t
(1) (2) (3)
௧
௧
= 0.996t-0.00159t2-0.000179t3
0 ≤ t ≤ 37.5 min
(4)
௧
௧
= 0.112*(t-37.5) + 25.7
37.5 min ≤ t
(5)
݂ሺݔሻ݀ ݔ− ݃ሺݔሻ݀ݔ ݂ሺݔሻ݀ ݔ− ݃ሺݔሻ݀ݔ
The ozone dosages computed for each treatment time are provided in Table 2. In our
241
preliminary work, the additional dosages of 26 and 75 mg O3/L were tested. The higher dosages
242
(127, 152, and 188 mg/L) were chosen for replicate experiments, as reported in this publication.
243
Ozone cost estimates
244
The ozone cost estimates include operating costs to purchase electricity for the ozone
245
generator and to prepare air for the ozonation. The costs of electricity and air are calculated as
246
follows:
247 248 249 250
Electricity consumption on typical ozone generators: 10 kWh/kg ozone Electricity: $0.07/kWh, 2009 average for industrial consumers 40 Electricity consumption for air feed drying: approximately 2 kWh/kg ozone Total electricity consumption and cost: 12 kWh/kg and $0.84/kg, respectively 12 ACS Paragon Plus Environment
(6) (7) (8) (9)
Journal of Agricultural and Food Chemistry
251
Capital costs: since the ozone dosage has not yet been optimized in relation to corn mash
252
formulations in industry, including recycled water sources, the required ozone generator size for
253
a typical plant cannot be determined. As a rough guide, the amortization costs will equal the
254
energy costs. The cost of ozone, therefore, can be expected to amount to roughly $1.68/kg. This
255
cost still needs to be determined to a greater degree of accuracy. Table 2 presents the estimated
256
ozonation costs based on the ozone dosages applied in experiments to date.
257
Initial pH experiment
258
The initial pH of corn mash prepared using ground corn, prior to fermentation (0 h), was
259
adjusted to 4.2 or 5.0. The pH of corn mash samples tended to decrease with increasing ozone
260
treatment times/dosages (Figure 4). The pH of ozonated samples (initial pH 5.0) started to
261
decrease after 15 min of ozonation (75 mg O3/L), reaching an average pH of 4.8 in 60 min (152
262
mg O3/L). With an initial pH of 4.2, the corn mash pH was also reduced by 0.2 pH units to 4.0
263
after 60 min of ozonation. Aeration using the same procedure, but no ozone generated, did not
264
affect the corn mash pH. This finding shows that the ozone or ozone byproducts, rather than
265
aeration and additional mixing, were responsible for the corn mash pH reductions observed in all
266
experiments using ground corn.
267
Corn mash samples were analyzed on the HPLC before and after treatment to detect any
268
changes in concentrations, in particular for organic acids. No consistent changes were observed
269
for ozonated and aerated samples. A slight increase in acetic acid of 0.35 g/L occurred in one
270
ozonated sample, but not in replicate samples. There were no changes in acetic acid in aerated
271
samples. No lactic acid was detected in any samples before or after ozonation/aeration.
272
Ground corn (Experiment sets 1 & 2)
273
Effects of ozonation on pH and lactic acid contents
13 ACS Paragon Plus Environment
Page 14 of 39
Page 15 of 39
274
Journal of Agricultural and Food Chemistry
Experiment set 1 (Figure 5): the daily pH values of ozonated and non-ozonated corn
275
mash samples decreased the first 24–48 h of fermentation only. The exceptions were samples
276
with higher ozone dosages (152 and 188 mg/L) and no yeast added; the pH of these samples
277
started decreasing after 24–48 h of fermentation and stabilizing by 96–120 h. All pH trends
278
corresponded with increases in lactic acid contents. Higher daily pH values, and less lactic acid,
279
were observed in samples subjected to higher ozone dosages.
280
Statistical analysis was conducted to compare the significance (p