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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

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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.

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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.

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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

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Department of Civil, Construction, and Environmental Engineering, Iowa State University, Ames, IA 50011

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b

Biorenewable Resources and Technology Program, Iowa State University, Ames, IA 50011

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c

Department of Agricultural and Biosystems Engineering, Iowa State University, Ames, IA 50011

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(ORCID #0000-0002-2387-0354)

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d

Department of Food Science and Human Nutrition, Iowa State University, Ames, IA 50011

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e

Department of Food, Nutrition, and Packaging Sciences, Clemson University, Clemson, SC

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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]

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Abstract

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Ozonation of uncooked corn mash from the POET BPXTM process was investigated as a

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potential disinfection method for reducing bacterial contamination prior to ethanol fermentation.

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Corn mash (200 g) was prepared using POET ground corn and POET corn slurry and was

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ozonated in 250-mL polypropylene bottles. Lactic and acetic acid levels were monitored daily

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during the fermentation of ozonated, aerated, and non-treated corn mash samples to evaluate

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bacterial activity. Glycerol and ethanol contents of fermentation samples were checked daily to

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assess yeast activity. No yeast supplementation, no addition of other antimicrobial agents (such

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as antibiotics), and spiking with a common lactic acid bacterium found in corn ethanol plants,

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Lactobacillus plantarum, amplified the treatment effects.

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The laboratory-scale ozone dosages ranged from 26–188 mg/L, with very low estimated

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costs of $0.0008 to $0.006 per gallon ($0.21 to $1.6 per m3) ethanol. Ozonation was found to

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decrease the initial pH of ground corn mash samples, which could reduce the sulfuric acid

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required to adjust the pH prior to ethanol fermentation. Lactic and acetic acid levels tended to be

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lower for samples subjected to increasing ozone dosages, indicating less bacterial activity. The

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lower ozone dosages in the range applied achieved higher ethanol yields. Preliminary

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experiments on ozonating POET corn slurry at low ozone dosages were not as effective as using

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POET ground corn, possibly because corn slurry samples contained recycled antimicrobials from

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the backset. The data suggest additional dissolved and suspended organic materials from the

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backset consumed the ozone or shielded the bacteria.

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Keywords: ozonation; no-cook; BPXTM process; corn mash; fuel ethanol; bacteria; dry-grind

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ethanol; lactic acid

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Introduction

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POET leads the fuel ethanol industry in streamlining corn dry milling to improve ethanol

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production efficiency, as well as their feed coproduct, Dakota Gold BPXTM distiller grains. The

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efficient BPXTM, or no-cook, process involves raw starch hydrolysis that, like the conventional

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process, adds enzymes to convert starch to sugars and adds yeast to ferment sugars to ethanol,

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but without the cooking step. 1 The BPXTM process is now used by 24 of the 27 POET

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biorefineries. POET produces over 1.5×109 gal (5.7×106 m3) of ethanol annually in a network

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spanning seven Midwestern states.

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The POET BPXTM process for dry-grind corn ethanol production has important

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advantages over the conventional process. The energy-intensive liquefaction and cooking steps

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are omitted, thus reducing plant energy requirements by 8–15%. 1 The BPXTM process achieves

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higher ethanol yields by improving starch accessibility, lowers volatile organic carbon (VOC)

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emissions, cuts cooling water needs, and enhances the nutrient quality, flowability and anti-

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caking properties of the distillers dried grains with solubles (DDGS) coproduct. Amino acid

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digestibility in DDGS samples varies considerably among conventional ethanol facilities,

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attributable to heat damage from corn mash cooking and DDGS drying. 2-5 Heat damage is

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responsible for the lower amino acid digestibility in DDGS than in corn grain. 4, 6 Removing the

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cooking step, therefore, improves the feed quality of Dakota Gold BPXTM DDGS over

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conventional DDGS by reducing heat damage of the protein. 7

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Unlike most beverage alcohols, fuel ethanol fermentations are not conducted under pure

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culture conditions. 8 High-temperature jet cooking (90–165°C) in the conventional process not

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only gelatinizes the corn starch, it helps reduce contamination and yield losses caused by

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unwanted lactic acid bacteria (LAB). 9 Contamination in fuel ethanol fermentations originates

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from bacteria present on the corn from the fields. 10 Bacteria compete with yeast for nutrients –

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glucose, trace minerals, vitamins, and free amino nitrogen – and lower ethanol yields by

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diverting glucose to lactic and acetic acids, which are inhibitory compounds to yeast. 11-13 In

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addition to yield losses by chronic LAB contamination, acute infections arise unpredictably and

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can result in plant shut-downs for cleaning – an expensive loss in productivity. 8, 13, 14

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Gram-positive and gram-negative bacterial isolates from fuel ethanol production include

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species of Pediococcus, Enterococcus, Acetobacter, Gluconobacter, Clostridium, and

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Lactobacillus. 8, 15 Lactobacilli sp. are the most prevalent in the industry and are ubiquitous in

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nature. In a study of two commercial dry grind ethanol plants by Skinner and Leathers, 8 the

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genus Lactobacillus was isolated most frequently, representing 38 and 77% of total bacterial

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isolates from the first and second plants, respectively. Gram-positive LAB are ethanol-tolerant,

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grow faster than yeast, and produce organic acids which inhibit yeast.

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During this research bacterial growth was controlled at POET biorefineries potentially by

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dosing with antibiotic and antimicrobial agent and by operation at lower pH levels (pH~ 4.2).

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Conventional ethanol plants, despite jet cooking, also add antibiotics to fight chronic or acute

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bacterial infections. 8, 16-18 If no antibiotics are used, it is common for a facility to lose 1–5% of

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its potential ethanol yield. 10 Rising concerns about the use of antibiotics and the emergence of

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antibiotic-resistant bacteria is creating a demand for alternative methods of controlling bacteria.

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Cleaning and sanitation are important microbial control measures in the corn ethanol

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industry. Infections in process tanks and continuous yeast propagators, as well as resistant

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biofilms within the process train, can continually reintroduce bacterial contaminants into the

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fermentors. 8, 19 Large yeast inoculums (≥2% [v/v]) help control contamination during

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fermentations; however, yeast growth and fermentation rates are still reduced by high lactobacilli

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concentrations. 20

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Penicillin and virginiamycin are the antibiotics available commercially for fuel ethanol

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production. 15, 21 Virginiamycin, produced by Streptomyces virginiae, has had limited use in

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human medicine but extensive use as a growth-promoting additive in animal feed. 22 The

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recommended dose of virginiamycin in fuel ethanol fermentations is 0.25–2.0 ppm. 23 The use

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of antibiotics has limitations. Commercial antibiotic applications are essentially selection

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experiments for resistant microorganisms. Hynes et al. 23 observed reductions in the

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effectiveness of virginiamycin after extended fermentations, possibly resulting from its

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breakdown by lactobacilli. 24 Lactobacillus sp. with higher tolerance to virginiamycin have been

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isolated from fuel ethanol plants that dose with virginiamycin. Moreover, bacterial isolates have

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emerged with resistance to both virginiamycin and penicillin. 15, 25

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Hop acids offer a natural alternative to antibiotics for fuel ethanol production. 10 Many

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of the organic acids found in hops exhibit antimicrobial activities. Hop-compounds inhibit

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growth by disrupting the trans-membrane pH gradient of microbes. 26, 27 Hops have long been

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used in the brewing industry to contribute to the flavor of beer, by adding bitterness and aroma,

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and to improve product shelf-life. IsoStabTM, a liquid hop extract, is a commercially-available

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product for fuel ethanol applications. U.S. producers using IsoStabTM have obtained higher

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ethanol yields with less fluctuation.

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A variety of disinfectants have been investigated on lab scale for fuel ethanol

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fermentations, including hydrogen peroxide, chlorine dioxide, potassium metabisulfite, 3,4,4’-

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trichlorocarbanilide, and lactate with a lactate-tolerate yeast strain. 8, 28-33 Bacteria were

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inhibited over yeast by these agents, but the effectiveness depended on the bacterial strain. 8

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Chlorine dioxide and ozonation are common alternatives to chlorination for disinfection of

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drinking water. Meneghin et al. 30 evaluated the effect of chlorine dioxide against bacteria

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prevalent in ethanol fermentations (e.g., Lactobacillus plantarum and L. fermentum). The

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minimum inhibitory concentrations (MIC) for chlorine dioxide on the bacteria and on the yeast

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inoculum were determined using nutrient media; the effectiveness in nutrient media is likely

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different from that in the high suspended-solids corn mash at fuel ethanol plants. The MICs

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ranged from 10–125 ppm for the bacterial strains tested; L. plantarum had the highest MIC of

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125 ppm. Yeast growth was also affected at chlorine dioxide concentrations over 50 ppm.

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Ozone is a microbial inhibitor that is considered an alternative to chlorine and hydrogen

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peroxide in food applications. 34 The rate of microbial inactivation is affected by the several

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environmental factors (concentration of organic compounds, the physiological state of the

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microorganism, pH of the medium, temperature). 35 Thus it has had mixed success in the food

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industry. Garcia-Cubero et al., 36 illustrated the benefit of pretreatment of straw with ozone

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resulted in a reduction in acid insoluble lignin (Klason Lignin) and improved enzymatic

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hydrolysis of cellulose and hemicelluloses for biofuel production. Freitas-Silva et al., 37

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demonstrated mycotoxin degradation by ozone use in corn on the cob, corn kernels, and corn and

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rice powder. Miller et al., 38 reviewed the advantages and disadvantages of ozonation use for

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fruits and vegetables preservation while Gerrity and Snyder 39 review its use in water reuse

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applications. Thus, the application of ozone in dry grind corn ethanol production is needed.

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Research Objectives

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In this research ozone was used in place of antibiotics (e.g., Lactrol® and IsoStabTM) for

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the control of bacterial contamination in ethanol (yeast) fermentations. Preliminary experiments

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were subsequently performed using corn slurry to evaluate the effectiveness of ozonation for

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reducing bacterial contamination under conditions more similar to plant operation, including the

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contributions of recycled water sources.

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Materials and Methods

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Corn mash preparation

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Ground corn and corn slurry were obtained from POET Biorefining in Jewell, IA in the

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fall and spring of 2007 and 2008. The corn slurry obtained from POET contains the ground corn

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in a slurry with recycled water streams, such as backset. Figure1 illustrates the corn mash

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preparation, ozone treatment, and simultaneous saccharification and fermentation (SSF)

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procedures. Corn mash was prepared in 250-mL polypropylene (PP) bottles with 35% (w/w)

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ground corn (200 g mash per bottle) and deionized water or with 200 g corn slurry per bottle.

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Urea was added (0.03% [w/w]) as a N source. The final corn mash volume was 186 mL per

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bottle. Bottles were shaken for 30 min at 250 rpm and room temperature to slurry contents. The

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pH was adjusted to 5.0 in select experiments. In preliminary work (pH 4.2), all controls with and

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without Lactrol® and/or IsoStabTM added had similar values for lactic and acetic acids, glycerol,

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and ethanol, which indicated minimal bacterial contamination even without ozonation (results

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not shown). Therefore, no antibiotics or other antimicrobials (i.e., Lactrol® or IsoStabTM) were

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added in these experiments to exemplify treatment effects of ozone. The POET corn slurry

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experiments, however, potentially contained recycled antimicrobials contributed in the backset

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from previous fermentations at the plant. Select samples were also LAB-spiked and/or not yeast-

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supplemented to amplify the differences in treatment effects.

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Microorganisms

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Select corn mash samples were spiked with Lactobacillus plantarum, a lactic acid

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bacterium, obtained from the American Type Culture Collection (ATCC 14917, Rockville, MD)

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prior to ozone treatment. Stock cultures of L. plantarum were freeze-dried and stored previously

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in sterile skim milk at 4 °C. Fermentis Ethanol Red (Lesaffre Yeast Corporation, Milwaukee,

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WI), containing the yeast Saccharomyces cerevisiae, was added (0.5 g) after ozone treatment for

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ethanol fermentation.

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Ozonation

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The laboratory-scale installation used to apply the ozone treatment is shown in Figure 2.

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Ozone gas was generated from oxygen supplied by a compressed-air gas cylinder using a corona-

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discharge ozone generator (TOG C2B, Trigon, Glasgow, Scotland). Moisture and hydrocarbon

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traps (Restek, State College, PA) were placed between the ozone generator and compressed-air

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cylinder to remove impurities in the feed gas. A mass flow controller (GLC17, Aalborg,

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Orangeburg, NY) was used to control the gas flow rate.

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Ozone gas was bubbled into the corn mash samples (200 g) in 250-mL PP bottles with a

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flow rate of 500 mL/min. The ozone concentration in the gas phase was measured by the

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potassium iodide titration method. 40 The ozone dose, or consumption, was calculated based on

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ozone concentrations in the influent and effluent gas from the bottle over time. Corn mash

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samples were ozonated and residual ozone in off-gas measured by titration after varying

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ozonation times. This setup was used to determine the effects of different ozone dosages on

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ethanol fermentation of corn mash samples prepared from ground corn or corn slurry. Aeration

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treatment, as a control, was also performed using this equipment. The aeration and ozonation

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procedures were the same (e.g., similar gas flow rate), but with the ozone generator turned off.

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Ethanol fermentation

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Following ozonation, raw starch hydrolyzing enzyme (Novozyme 50009, 0.11% [v/w])

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and Ethanol Red (0.25% [w/w]) were added to ozonated, aerated, and non-treated corn mash

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(Figure 1). Bottles were shaken for 2 min at 250 rpm to mix contents and incubated without

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shaking at 27 °C (POET incubation temperature) until ethanol levels reached a plateau – up to

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168 h. SSF samples were HPLC-analyzed on a daily basis.

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Sample analyses

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The ethanol, glycerol, lactic acid, and acetic acid contents of corn mash and SSF samples

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were quantified using a Waters high pressure liquid chromatograph (HPLC) (Millipore

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Corporation, Milford, MA). The HPLC system was equipped with a Waters Model 401

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refractive index detector, column heater, automatic sampler, and computer controller. The

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Aminex HPX-8711 column (300×7.8 mm, Bio-Rad Chemical Division, Richmond, CA)

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separated sample constituents with a mobile phase of 0.012 N sulfuric acid, flow rate of 0.8

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mL/min, injection volume of 20 µL, and column temperature of 65 °C. 41

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Experiment sets

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A pH experiment was conducted prior to fermentation. Aeration treatment was included

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to confirm that ozonation, rather than aeration and mixing, lowered the initial corn mash pH

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prior to fermentation (0 h).

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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.

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POET ground corn (Experiment sets 1 & 2)

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Two sets of fermentation experiments with ozone-treated corn mash prepared from

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ground corn were performed. The first set included spiking with L. plantarum before ozone

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treatment (0–188 mg/L) of corn mash; no yeast and no other antimicrobial agents were added to

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select bottles to further amplify the treatment effects. The second set included ozonation and

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aeration treatments of corn mash prior to ethanol fermentation. Select bottles were spiked with

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L. plantarum. Fermentation experiments were conducted with aeration treatment as a control to

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determine whether lower lactic acid contents in daily samples resulted from ozonation as a

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disinfect/oxidant or from possible stimulatory effects of aeration on the yeast.

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POET corn slurry (Experiment set 3)

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A preliminary set of fermentation experiments was conducted with POET corn slurry to

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assess the effectiveness of ozonation for reducing bacterial contamination under conditions more

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similar to plant operation, including contributions of recycled water streams. The recycled

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backset potentially contributed other antimicrobials in these experiments. Corn mash samples

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were prepared with/without the addition of yeast, with the slurry initial pH of 4.0 and adjusted to

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pH 5.0, and with/without ozone treatment, as shown in Table 1.

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Statistical Analysis All treatments were performed in replicates of three. Statistical analysis was carried out

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using the Statistical Analysis System package (SAS Computer Program Version 9.1.2, SAS

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Institute Inc., Cary, NC). Student’s t-test analyses were performed on HPLC data sets to

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determine statistical significance with a p value of 0.05.

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Results and Discussion

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Ozone dosages

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The results of ozonating corn mash samples for various treatment times in order to

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determine ozone consumption (i.e., ozone dosage) are illustrated in Figure 3. Ozone

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consumption is the difference between the ozone applied to the corn mash, f(x), and the unused

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ozone exiting the headspace of the treated corn mash over time (off-gas), g(x); it equals the green

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area in Figure 3. The following fitted equations were used to calculate ozone

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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)





= 0.996t-0.00159t2-0.000179t3

0 ≤ t ≤ 37.5 min

(4)





= 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

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preliminary work, the additional dosages of 26 and 75 mg O3/L were tested. The higher dosages

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(127, 152, and 188 mg/L) were chosen for replicate experiments, as reported in this publication.

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Ozone cost estimates

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The ozone cost estimates include operating costs to purchase electricity for the ozone

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generator and to prepare air for the ozonation. The costs of electricity and air are calculated as

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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

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Capital costs: since the ozone dosage has not yet been optimized in relation to corn mash

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formulations in industry, including recycled water sources, the required ozone generator size for

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a typical plant cannot be determined. As a rough guide, the amortization costs will equal the

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energy costs. The cost of ozone, therefore, can be expected to amount to roughly $1.68/kg. This

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cost still needs to be determined to a greater degree of accuracy. Table 2 presents the estimated

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ozonation costs based on the ozone dosages applied in experiments to date.

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Initial pH experiment

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The initial pH of corn mash prepared using ground corn, prior to fermentation (0 h), was

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adjusted to 4.2 or 5.0. The pH of corn mash samples tended to decrease with increasing ozone

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treatment times/dosages (Figure 4). The pH of ozonated samples (initial pH 5.0) started to

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decrease after 15 min of ozonation (75 mg O3/L), reaching an average pH of 4.8 in 60 min (152

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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

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after 60 min of ozonation. Aeration using the same procedure, but no ozone generated, did not

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affect the corn mash pH. This finding shows that the ozone or ozone byproducts, rather than

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aeration and additional mixing, were responsible for the corn mash pH reductions observed in all

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experiments using ground corn.

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Corn mash samples were analyzed on the HPLC before and after treatment to detect any

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changes in concentrations, in particular for organic acids. No consistent changes were observed

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for ozonated and aerated samples. A slight increase in acetic acid of 0.35 g/L occurred in one

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ozonated sample, but not in replicate samples. There were no changes in acetic acid in aerated

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samples. No lactic acid was detected in any samples before or after ozonation/aeration.

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Ground corn (Experiment sets 1 & 2)

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Effects of ozonation on pH and lactic acid contents

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Experiment set 1 (Figure 5): the daily pH values of ozonated and non-ozonated corn

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mash samples decreased the first 24–48 h of fermentation only. The exceptions were samples

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with higher ozone dosages (152 and 188 mg/L) and no yeast added; the pH of these samples

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started decreasing after 24–48 h of fermentation and stabilizing by 96–120 h. All pH trends

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corresponded with increases in lactic acid contents. Higher daily pH values, and less lactic acid,

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were observed in samples subjected to higher ozone dosages.

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Statistical analysis was conducted to compare the significance (p