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<article article-type="research-article" xmlns:xlink="http://www.w3.org/1999/xlink" xmlns:mml="http://www.w3.org/1998/Math/MathML" xml:lang="en">
<front>
<journal-meta>
<journal-id journal-id-type="publisher-id">IJFS</journal-id>
<journal-title-group>
<journal-title>Italian Journal of Food Science</journal-title>
<abbrev-journal-title>IJFS</abbrev-journal-title>
</journal-title-group>
<issn pub-type="epub">1120-1770</issn>
<publisher>
<publisher-name>Codon Publications</publisher-name>
</publisher>
</journal-meta>
<article-meta>
<article-id pub-id-type="publisher-id">IJFS-38-240</article-id>
<article-id pub-id-type="doi">10.15586/ijfs.v38i1.3299</article-id>
<article-categories>
<subj-group subj-group-type="heading">
<subject>ORIGINAL ARTICLE</subject>
</subj-group>
</article-categories>
<title-group>
<article-title>Changes in fermentation characteristics of commercial Kombucha determined by time of inoculation of a mixed culture of bacteria and yeast&#x2014;Gluconobacter oxydans SFT-27, Acetobacter pasteurianus SFT-18, Leuconostoc mesenteroides SFT-45, and Saccharomyces cerevisiae SFT-71</article-title>
</title-group>
<contrib-group content-type="authors">
<contrib contrib-type="author" equal-contrib="yes"><name><surname>Choi</surname> <given-names>Byung-kuk</given-names></name><xref ref-type="aff" rid="aff1">1</xref><xref ref-type="author-notes" rid="afn01">&#x2021;</xref></contrib> 
<contrib contrib-type="author" equal-contrib="yes"><name><surname>Kim</surname> <given-names>Su-Hwan</given-names></name><xref ref-type="aff" rid="aff2">2</xref><xref ref-type="author-notes" rid="afn01">&#x2021;</xref></contrib> 
<contrib contrib-type="author"><name><surname>Song</surname> <given-names>Geun-Ho</given-names></name><xref ref-type="aff" rid="aff1">1</xref></contrib> 
<contrib contrib-type="author"><name><surname>Kim</surname> <given-names>Sang&#x2013;Ah</given-names></name><xref ref-type="aff" rid="aff1">1</xref></contrib> 
<contrib contrib-type="author" corresp="yes"><name><surname>Huh</surname> <given-names>Chang-Ki</given-names></name><xref ref-type="aff" rid="aff2">2</xref><xref ref-type="aff" rid="aff3">3</xref><xref ref-type="corresp" rid="cor1"/></contrib>
<aff id="aff1"><label>1</label>Fermented Food Industry Center, Suncheon, Korea;</aff>
<aff id="aff2"><label>2</label>Research Institute of Food Industry, Sunchon National University, Suncheon, Korea;</aff>
<aff id="aff3"><label>3</label>Department of Food Science and Technology, Sunchon National University, Suncheon, Korea</aff>
</contrib-group>
<author-notes>
<corresp id="cor1"><label>&#x002A;</label><bold>Corresponding Author:</bold> Chang-Ki Huh, Department of Food Science and Technology, Sunchon National University, Suncheon, Korea. Email: <email>hck1008@scnu.ac.kr</email></corresp>
<fn id="afn01" fn-type="equal"><label>&#x2021;</label><p>These authors contributed equally to this work.</p></fn>
<fn id="afn02"><p><bold>Academic Editor:</bold> Prof. Antonietta Baiano &#x2013; University of Foggia, Italy</p></fn>
</author-notes>
<pub-date pub-type="epub">
<day>1</day>
<month>01</month>
<year>2026</year>
</pub-date>
<pub-date pub-type="collection"><year>2026</year></pub-date>
<volume>38</volume>
<issue>1</issue>
<fpage>240</fpage>
<lpage>249</lpage>
<history>
<date date-type="received"><day>07</day><month>08</month><year>2025</year></date> 
<date date-type="accepted"><day>10</day><month>10</month><year>2025</year></date> 
</history>
<permissions>
<copyright-statement>&#x00A9; 2026 Codon Publications</copyright-statement>
<copyright-year>2026</copyright-year>
<license license-type="open-access" xlink:href="http://creativecommons.org/licenses/by-nc-sa/4.0/">
<license-p>This is an Open Access article distributed under the terms of the Creative Commons Attribution-NonCommercial-ShareAlike 4.0 International (CC BY-NC-SA 4.0). License (<ext-link ext-link-type="uri" xlink:href="http://creativecommons.org/licenses/by-nc-sa/4.0/">http://creativecommons.org/licenses/by-nc-sa/4.0/</ext-link>)</license-p>
</license>
</permissions>
<abstract>
<p>Our study aimed to investigate the effects of varied inoculation times of a mixed culture of four microorganisms on the fermentation characteristics of kombucha to standardize the process. We selected strains through prior phenotypic and genotypic screening to establish a controlled, mixed microbial fermentation system for kombucha production. A combination of <italic>Gluconobacter oxydans</italic> SFT-27, <italic>Acetobacter pasteurianus</italic> SFT-18, <italic>Leuconostoc mesenteroides</italic> SFT-45, and <italic>Saccharomyces cerevisiae</italic> SFT-71was used for inoculation at different times (Days 1&#x2013;5) to assess the effects on fermentation characteristics. Green tea extract was prepared and supplemented with sucrose, glucose, and appropriate nitrogen sources. The extract was inoculated with a primary inoculation of acetic acid bacteria (<italic>G. oxydans</italic> SFT-27, <italic>A. pasteurianus</italic> SFT-18). There were subsequent inoculations with yeast (<italic>S. cerevisiae</italic> SFT-71) and lactic acid bacteria (<italic>L. mesenteroides</italic> SFT-45) from Day 1&#x2013;5. We analyzed key fermentation indices, including pH, titratable acidity, ethanol content, &#x00B0;Brix, reducing sugar content, viable microbial counts, and gluconic acid levels over 25 days. Results demonstrated that pH decreased sharply after the third day of inoculation, with titratable acidity peaking at 4.64%, surpassing Korean food code standards. Ethanol peaked on Day 5 and decreased thereafter. There was a steady increase in reducing sugars, particularly in the samples inoculated later, which correlated with enzymatic sucrose hydrolysis and cellulose degradation. Microbial counts indicated stable populations of acetic acid bacteria and yeast when the samples were inoculated on Days 3 and 5. Gluconic acid production was the highest in the sample inoculated on Day 5, exceeding levels reported in symbiotic culture of bacteria and yeast (SCOBY)-based fermentations. These findings suggest that inoculation with yeast and lactic acid bacteria, following prefermentation with acetic acid bacteria, yields superior fermentation performance in terms of acidity, metabolite production, and microbial stability.</p>
</abstract>
<kwd-group>
<kwd>inoculation time</kwd>
<kwd>Kombucha</kwd>
<kwd>metabolite</kwd>
<kwd>mixed culture fermentation</kwd>
<kwd>process optimization</kwd>
</kwd-group>
</article-meta>
</front>
<body>
<sec id="S1">
<title>Introduction</title>
<p>Kombucha is a fermented, carbonated beverage -prepared by adding sugar to tea extract and fermenting it with a symbiotic culture of bacteria and yeast (SCOBY) (<xref ref-type="bibr" rid="ref10">Dufresne and Farnworth, 2000</xref>). It is a noteworthy, functional beverage that contains organic acids, polyphenols, vitamins, and probiotics (<xref ref-type="bibr" rid="ref1">Akbarirad <italic>et al</italic>., 2017</xref>). The microbial composition of the SCOBY is a principal determinant of the quality and functionality of kombucha. Typically, SCOBY exists in the form of a biofilm composed of acetic acid bacteria, yeast, and lactic acid bacteria (<xref ref-type="bibr" rid="ref29">Soares <italic>et al</italic>., 2021</xref>). The interactions among these microorganisms determine key quality indicators, such as fermentation speed, organic acid production, flavor, and antioxidant properties (<xref ref-type="bibr" rid="ref16">I&#x00E7;en <italic>et al</italic>., 2023</xref>; <xref ref-type="bibr" rid="ref19">Kim <italic>et al</italic>., 2020</xref>). There are challenges to standardize the quality of the product during mass production because there is low reproducibility of fermentation based on natural SCOBY due to inconsistent microbial composition and sensitivity to changes in culture conditions (<xref ref-type="bibr" rid="ref20">Laavanya <italic>et al</italic>., 2021</xref>; <xref ref-type="bibr" rid="ref25">Malbasa <italic>et al</italic>., 2011</xref>; <xref ref-type="bibr" rid="ref31">Wang <italic>et al</italic>., 2024</xref>). Recent studies attempted to isolate and identify the major microbial groups that constitute SCOBY and to conduct controlled fermentation using a combined culture of these microorganisms (<xref ref-type="bibr" rid="ref11">Fabricio <italic>et al</italic>., 2023</xref>; <xref ref-type="bibr" rid="ref7">Cheng <italic>et al</italic>., 2024</xref>), However, fermentation using mixed cultures is complex due to differences in growth rates, competition for nutrients, varied acid production patterns among the strains, and different characteristics of fermentation based on the time and the order of inoculation (<xref ref-type="bibr" rid="ref9">De Roos and De Vuyst, 2018</xref>; <xref ref-type="bibr" rid="ref32">Wang <italic>et al</italic>., 2013</xref>; <xref ref-type="bibr" rid="ref13">Grassi <italic>et al</italic>., 2022</xref>). Therefore, it is vital to select specific strains and establish a standardized fermentation system that uses them. In this study, we aimed to analyze the changes in the fermentation characteristics of kombucha with respect to the time of inoculation of a mixed culture of four strains: <italic>Gluconobacter oxydans</italic> SFT-27, <italic>Acetobacter pasteurianus</italic> SFT-18, <italic>Leuconostoc mesenteroides</italic> SFT-45, and <italic>Saccharomyces cerevisiae</italic> SFT-71. Through this, we aim to establish an optimal strategy for inoculation of kombucha based on the composition of mixed cultures and propose the industrial production potential of consistent and highly functional kombucha.</p>
</sec>
<sec id="S2">
<title>Materials and Methods</title>
<sec id="S2_1">
<title>Materials and reagents</title>
<p>The green tea leaves used in this experiment were purchased from Duson Herbal Co., Ltd., Yeongcheon-si, Korea. Yeast extract, tryptone, and -soytone were obtained from Life Technologies Co., Miami, FL, USA. Peptone was purchased from Duksan Pure Chemical Co., Ansan-si, Korea. Glucose was purchased from MB Cell Seocho-gu, Seoul, Korea, and fructose and sucrose were obtained from Daejung, Siheung-si, Korea.</p>
</sec>
<sec id="S2_2">
<title>Strain selection through preliminary research</title>
<p>The four strains used in our study were previously isolated in the Food Fermentation Engineering Laboratory at Sunchon National University (<xref ref-type="bibr" rid="ref17">Jo <italic>et al</italic>., 2024</xref>; <xref ref-type="bibr" rid="ref22">Lee <italic>et al</italic>., 2024</xref>), using the following selection process: Acetic acid bacteria were isolated from vinegar starter, plum extract, wine, and nine types of fruits, which were collected from the Food Fermentation Engineering Laboratory and the Suncheon Agricultural Wholesale Market. Commercially available kombucha and eight types of fruit vinegar were also used as isolation sources. A total of 31 strains were isolated and purified, and their fermentation characteristics were evaluated, including pH, titratable acidity, acid tolerance, ethanol tolerance, microbial count, and contents of gluconic acids. Based on these evaluations, we selected two acetic acid bacterial strains (SFT-18 and SFT-27) and analyzed the base sequence of their 16S ribosomal RNA using primers 785F (5&#x2019;-GGA TTA GAT ACC CTG GTA-3&#x2019;) and 907R (5&#x2019;-CCG TCA ATT CMT TTR AGT TT-3&#x2019;). We also isolated lactic acid bacteria from peach syrup, wine, kombucha, and three types of fruit collected at the same location, as well as from acacia honey and kimchi (including napa cabbage and ponytail radish varieties). We isolated and purified a total of 22 strains. Their biological and morphological characteristics were evaluated (including catalase test, Gram stain, and simple stain), along with their fermentation traits (pH, titratable acidity, acid tolerance, ethanol tolerance, microbial count). Based on the results, a lactic acid bacterial strain (SFT-45) was selected and identified using 16S rRNA sequencing with the same primers as above. Yeasts were selected from a pool of 20 strains stored at the Food Fermentation Engineering Laboratory. Their fermentation characteristics were evaluated, including pH, titratable acidity, acid tolerance, ethanol tolerance, ethanol production capacity, and cellulase activity. Based on this evaluation, we selected the yeast strain SFT-71 and analyzed its 18S rRNA sequence using primers NS1 (5&#x2019;-GTA GTC ATA TGC TTG TCT C-3&#x2019;) and NS24 (5&#x2019;-TCC GCA GGT TCA CCT ACG GA-3&#x2019;).</p>
</sec>
<sec id="S2_3">
<title>Selection of strains</title>
<p>To design an optimized microbial composition for Kombucha production, our study selected strains based on their fermentation characteristics, including excellent acid and ethanol tolerance, as well as robust growth at various temperatures. These strains were deposited in the Korean Culture Center of Microorganisms (KCCM) as follows: Acetic acid bacteria: <italic>A. pasteurianus</italic> SFT-18 (KCCM accession number: KFCC11966P), Acetic acid bacteria: <italic>G. oxydans</italic> SFT-27 (KFCC11967P), Lactic acid bacteria: <italic>L. mesenteroides</italic> SFT-45 (KFCC11968P), Yeast: <italic>S. cerevisiae</italic> SFT-71 (KFCC11969P) (<xref ref-type="table" rid="T1">Table 1</xref>).</p>
<table-wrap id="T1" orientation="portrait" position="float">
<label>Table 1.</label><caption><p>Information on the four strains used in complex fermentation.</p></caption>
<table frame="border" rules="groups">
<thead valign="top">
<tr>
<th align="left">Strains</th>
<th align="left">Function summary</th>
<th align="left">Medium/culture conditions</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="left"><italic>Acetobacter</italic><break/><italic>pasteurianus</italic> SFT-18<break/>(KFCC11966P)</td>
<td align="left">- Purely separated from <italic>Maesil Cheong</italic><break/>- Strong resistance to acid and ethanol<break/>- Excellent growth at 30&#x00B0;C fermentation temperature</td>
<td align="left">Yeast extract 1%, Glucose 5%, Ethanol 3%<break/>Aerobic bacteria/30&#x00B0;C/Shaked culture, Stationary culture</td>
</tr>
<tr>
<td align="left"><italic>Gluconobacter</italic><break/><italic>oxydans</italic> SFT-27<break/>(KFCC11967P)</td>
<td align="left">- Purely separated from grape vinegar<break/>- Strong resistance to acid and ethanol<break/>- Production of metabolites (Glucuronic acid, Gluconate) was confirmed.<break/>- Excellent growth at 30&#x00B0;C fermentation temperature</td>
<td align="left">Yeast extract 1%, Glucose 5%, Ethanol 3%<break/>Aerobic bacteria/30&#x00B0;C/Shaked culture, Stationary culture</td>
</tr>
<tr>
<td align="left"><italic>Leuconostoc mesenteroides</italic> SFT-45<break/>(KFCC11968P)</td>
<td align="left">- Purely separated from the surface of plums<break/>- Confirmed resistance to acid and ethanol<break/>- Excellent growth at 30&#x00B0;C fermentation temperature</td>
<td align="left">MRS broth<break/>Facultative anaerobe/30&#x00B0;C/Stationary culture</td>
</tr>
<tr>
<td align="left"><italic>Saccharomyces cerevisiae</italic> SFT-71<break/>(KFCC11969P)</td>
<td align="left">- Selected as a strain for Kombucha complex fermentation.<break/>- Excellent acid resistance and ethanol resistance<break/>- Excellent CO<sub>2</sub> generation ability<break/>- Strong ethanol production and cellulase activity<break/>- Excellent growth at 30&#x00B0;C fermentation temperature</td>
<td align="left">YM broth<break/>Aerobic bacteria/30&#x00B0;C/Stationary culture</td>
</tr>
</tbody>
</table></table-wrap>
</sec>
<sec id="S2_4">
<title>Preparation of green tea extract</title>
<p>To develop an optimal composition of carbon and nitrogen sources for kombucha production and a mixed starter culture development, we prepared a green tea extract to test for fermentation characteristics. The green tea was prepared by adding 10 g green tea leaves to 1 L of distilled water and extracted at 90&#x00B0;C for 1 h. The extract was then filtered and sterilized at 121&#x00B0;C for 15 min in the autoclave. After the extract was cooled to 30&#x00B0;C, it was used as the fermentation medium (<xref ref-type="fig" rid="F1">Figure 1</xref>).</p>
<fig id="F1" orientation="portrait" position="float">
<label>Figure 1.</label>
<caption><p>The process of mixed culture fermentation according to inoculation time.</p></caption>
<graphic xmlns:xlink="http://www.w3.org/1999/xlink" xlink:href="IJFS-38-240-g001.tif"/>
</fig>
</sec>
<sec id="S2_5">
<title>Inoculation of media with bacteria and yeast at distinct time points</title>
<p>To evaluate the effects of bacterial and yeast inoculations at different time points, we prepared a medium of 1% green tea extract supplemented with 0.01% yeast extract, 0.008% isolated soy protein as a nitrogen source, and 10% sucrose with 5% glucose as a carbon source. The medium was inoculated with 1% each of acetic acid bacteria (<italic>A. pasteurianus</italic> SFT-18 and <italic>G. oxydans</italic> SFT-27), followed by 1% inoculations of <italic>L. -mesenteroides</italic> SFT-45 (lactic acid bacteria) and <italic>S. cerevisiae</italic> SFT-71 (yeast) on different fermentation days (from Day 1&#x2013;5) (<xref ref-type="fig" rid="F1">Figure 1</xref>).</p>
</sec>
<sec id="S2_6">
<title>Measurement of pH and titratable acidity</title>
<p>The pH of 10 mL of the sample was measured using a pH meter (HM-40X, DKK-TOA Co., Tokyo, Japan). For titratable acidity, an appropriate amount of sample was titrated with 0.1 N NaOH after addition of 1% phenolphthalein as an indicator. The lactic acid conversion factor of 0.009 was used to calculate the acidity (<xref ref-type="bibr" rid="ref14">Guangsen <italic>et al</italic>., 2021</xref>).</p>
</sec>
<sec id="S2_7">
<title>Measurement of ethanol content</title>
<p>The ethanol content was measured as per the alcoholic beverage analysis guidelines of the National Tax Service (<xref ref-type="bibr" rid="ref28">NTS, 2020</xref>). The sample was filtered, and 1 &#x03BC;L of the filtrate was injected into a gas chromatograph (GC, 6890N and G1530N, Agilent Co., Santa Clara, CA, USA). Quantitation was performed using the external standard method. Gas chromatograph conditions were as follows: a DB-Wax column (60 m &#x00D7; 0.32 mm &#x00D7; 0.5 &#x03BC;m, Agilent Technologies Inc., Santa Clara, CA, USA) was used with the oven temperature raised from 60 to 100&#x00B0;C at 3&#x00B0;C/min, and then from 100 to 150&#x00B0;C at 5&#x00B0;C/min. Nitrogen (N<sub>2</sub>) was used as the carrier gas. The injector and detector temperatures were set at 150 and 200&#x00B0;C, respectively.</p>
</sec>
<sec id="S2_8">
<title>Measurement of soluble solids (&#x00B0;Brix) and reducing sugars</title>
<p>Soluble solids were measured using a digital refractometer (PAL-3, Atago Co., Tokyo, Japan) and expressed in &#x00B0;Brix. The 3,5-dinitrosalycylic acid (DNS) method was used to measure reducing sugars. 1 g of the sample was diluted 1000-fold, and 1 mL of the diluted solution was mixed with 3 mL of DNS reagent. The mixture was boiled in a water bath for 5 min, cooled, and its absorbance was measured at 550 nm using a microplate reader (SPECTROstar Nano, BMG Labtech, Ortenberg, Germany). We used glucose as the standard (<xref ref-type="bibr" rid="ref27">Miller, 1959</xref>).</p>
</sec>
<sec id="S2_9">
<title>Microbial enumeration</title>
<p>To measure microbial counts during the fermentation with mixed culture, we assessed both total viable counts and yeast counts. A modified standard plate count method (<xref ref-type="bibr" rid="ref26">MFDS, 2024</xref>) was used. The samples were serially diluted with 0.85% NaCl solution and plated on plate count agar (PCA for total bacteria) and yeast malt (YM for yeast) agar, then incubated for 2 days at 35 and 30&#x00B0;C, respectively. Colony-forming units were averaged from three independent experiments and expressed as log CFU/mL.</p>
</sec>
<sec id="S2_10">
<title>Measurement of gluconic acid content</title>
<p>Gluconic acid was analyzed following the method of <xref ref-type="bibr" rid="ref3">Ansari <italic>et al</italic>. (2019)</xref>. The fermentation broth was centrifuged (1000 rpm, 3 min; HA-1000-3, Hanil Science Industrial Co., Incheon, Korea), and the supernatant was filtered through a 0.45 &#x03BC;m PVDF membrane (25 mm, Chromdisc, Daegu, Korea). The filtrate was analyzed using HPLC (Waters 1525 and 717, Waters Co., Milford, MA, USA) with a Supelcogel C-610H column (30 cm &#x00D7; 7.8 mm, Supelco, Bellefonte, PA, USA). The column oven was maintained at 30&#x00B0;C; the mobile phase was 0.1% phosphoric acid with a flow rate of 0.6 mL/min. A UV detector was used for the detection (Waters 996) at 210 nm. Sodium gluconate (Sigma-Aldrich, St. Louis, MO, USA) was used as the standard, and the quantitation was done using the external standard method.</p>
</sec>
<sec id="S2_11">
<title>Statistical analysis</title>
<p>All the experiments were performed in triplicate or more. Statistical analysis was performed using SPSS version 27 (IBM Corp., Armonk, NY, USA). The results were expressed as mean &#x00B1; SD, and Duncan&#x2019;s multiple range test was used to determine the significance between mean values at P &#x003C; 0.05.</p>
</sec>
</sec>
<sec id="S3">
<title>Results and Discussion</title>
<sec id="S3_1">
<title>pH and titratable acidity</title>
<p>In fermented beverages (Kombucha), the pH and titratable acidity are critical indicators of product quality. In kombucha, these values are strongly influenced by the organic acids produced by acetic acid and lactic acid bacteria (<xref ref-type="bibr" rid="ref8">Dartora <italic>et al</italic>., 2023</xref>). The results of pH and titratable acidity measurements based on the time of inoculation of the mixed culture are shown in <xref ref-type="fig" rid="F2">Figures 2</xref> and <xref ref-type="fig" rid="F3">3</xref>. On different days from Day 1 to 5, 1% acetic acid bacteria (<italic>A. pasteurianus</italic> SFT-18 and <italic>G. oxydans</italic> SFT-27) were inoculated, followed by inoculation of each of 1% lactic acid bacteria (<italic>L. mesenteroides</italic> SFT-45) and 1% yeast (<italic>S. cerevisiae</italic> SFT-71). These were labeled as Sample A (inoculation on Day 1), Sample B (inoculation on Day 2), Sample C (inoculation on Day 3), Sample D (inoculation on Day 4), and Sample E (inoculation on Day 5). The pH decreased as the incubation period of the acetic acid bacteria increased, but no difference was observed after Sample C. By Day 25 of fermentation, there was a significant drop in pH in samples C, D, and E compared to that of samples A and B. In contrast, titratable acidity increased as the incubation period progressed and plateaued after the third day of inoculation. By Day 25, the titratable acidity for the inoculations on Days 1, 3, and 5 was 4.28, 4.01, and 4.64%, respectively, all of which exceeded the Korean food code standard for vinegar acidity (&#x2265; 4%).</p>
<fig id="F2" orientation="portrait" position="float">
<label>Figure 2.</label>
<caption><p>Changes in pH at different inoculation dates of a complex strain. (A) Yeast and lactic acid bacteria were inoculated on day 1 of the acetic acid bacteria culture; (B) Yeast and lactic acid bacteria were inoculated on day 2 of the acetic acid bacteria -culture; (C) Yeast and lactic acid bacteria were inoculated on day 3 of the acetic acid bacteria culture; (D) Yeast and lactic acid -bacteria were inoculated on day 4 of the acetic acid bacteria culture; (E) Yeast and lactic acid bacteria were inoculated on day 5 of the acetic acid bacteria culture. All values are mean &#x00B1; SD (n = 3).</p></caption>
<graphic xmlns:xlink="http://www.w3.org/1999/xlink" xlink:href="IJFS-38-240-g002.tif"/>
</fig>
<fig id="F3" orientation="portrait" position="float">
<label>Figure 3.</label>
<caption><p>Changes in titratable acidity at different inoculation dates of a complex strain. Detailed sample information is -provided in Figure 2. All values are mean &#x00B1; SD (n = 3). Means followed by the different lowercase letters at the same fermentation time (day) are significantly different (p&#x003C;0.05, a&#x003E;b&#x003E;c&#x003E;d&#x003E;e).</p></caption>
<graphic xmlns:xlink="http://www.w3.org/1999/xlink" xlink:href="IJFS-38-240-g003.tif"/>
</fig>
</sec>
<sec id="S3_2">
<title>Ethanol content</title>
<p>As shown in <xref ref-type="fig" rid="F4">Figure 4</xref>, most samples reached peak ethanol levels on Day 5 of fermentation, ranging from 0.09 to 0.49%. For Sample E, the peak occurred on Day 10 at 0.11%. The ethanol content then steadily declined to 0.03&#x2013;0.04% by the 25th day. On the fifth day of fermentation, Sample E exhibited an ethanol content nearly 10 times lower than that of the sample with the highest ethanol concentration. This phenomenon can be attributed to two factors. First, an acidic environment is known to inhibit yeast metabolism, resulting in reduced growth rates and lower ethanol production. Second, it may be due to the balance between ethanol production by yeast and the metabolism of acetic acid bacteria (<xref ref-type="bibr" rid="ref5">Casey <italic>et al</italic>., 2010</xref>; <xref ref-type="bibr" rid="ref12">Gomes <italic>et al</italic>., 2018</xref>; <xref ref-type="bibr" rid="ref32">Wang <italic>et al</italic>., 2013</xref>). This inference is supported by the observation that, after Sample C, the total bacterial count in this study exceeded the yeast count.</p>
<fig id="F4" orientation="portrait" position="float">
<label>Figure 4.</label>
<caption><p>Changes in ethanol content at different inoculation dates of a complex strain. Detailed sample information is provided in Figure 2.</p></caption>
<graphic xmlns:xlink="http://www.w3.org/1999/xlink" xlink:href="IJFS-38-240-g004.tif"/>
</fig>
</sec>
<sec id="S3_3">
<title>Soluble solids (&#x00B0;Brix) and reducing sugars</title>
<p>As shown in <xref ref-type="fig" rid="F5">Figure 5</xref>, the initial &#x00B0;Brix ranged from 13.2 to 14.6 and gradually increased over 25 days of fermentation. The levels of reducing sugars (<xref ref-type="fig" rid="F6">Figure 6</xref>) also increased continuously from an initial range of 58.55&#x2013;71.38 to 285.71&#x2013;346.46 mg/mL by the 25th day. Among all the samples, Sample B showed the lowest final values (32.2 &#x00B0;Brix, 287.71 mg/mL), while Sample E showed the highest (67.0 &#x00B0;Brix, 346.46 mg/mL). Our study observed a continuous rise in the levels of reducing sugars, unlike <xref ref-type="bibr" rid="ref30">Tu <italic>et al</italic>. (2024)</xref>, who reported a rise and subsequent fall in the content of reducing sugars during fermentation. However, <xref ref-type="bibr" rid="ref21">Lau and Tang (2025)</xref> reported that the total sugar content increased depending on the type of extract and the added sugar. <xref ref-type="bibr" rid="ref6">Chen <italic>et al</italic>. (2025)</xref> found that sugar content increased based on the yeast strain inoculated, while <xref ref-type="bibr" rid="ref18">Kilmanoglu <italic>et al</italic>. (2024)</xref> observed that sugar levels rose depending on the combination of yeast and acetic acid bacteria strains. This could be attributed to differences in the levels of carbon sources (glucose 5% and sucrose 10%) and the enzymatic hydrolysis of sucrose into glucose and fructose by yeast invertase (<xref ref-type="bibr" rid="ref33">Zhao <italic>et al</italic>., 2023</xref>). Additionally, glucose production from cellulose degradation by acetic acid bacteria (<xref ref-type="bibr" rid="ref15">Guimaraes <italic>et al</italic>., 2024</xref>) likely contributed to the levels of reducing sugars.</p>
<fig id="F5" orientation="portrait" position="float">
<label>Figure 5.</label>
<caption><p>Changes in the &#x00B0;Brix value at different inoculation dates of a complex strain. Detailed sample information is provided in Figure 2.</p></caption>
<graphic xmlns:xlink="http://www.w3.org/1999/xlink" xlink:href="IJFS-38-240-g005.tif"/>
</fig>
<fig id="F6" orientation="portrait" position="float">
<label>Figure 6.</label>
<caption><p>Changes in the reducing sugar content at different inoculation dates of a complex strain. Detailed sample -information is provided in Figure 2. All values are mean &#x00B1; SD (n = 3). Means followed by the different lowercase letters at the same -fermentation time (day) are significantly different (p&#x003C;0.05, a&#x003E;b&#x003E;c&#x003E;d&#x003E;e).</p></caption>
<graphic xmlns:xlink="http://www.w3.org/1999/xlink" xlink:href="IJFS-38-240-g006.tif"/>
</fig>
</sec>
<sec id="S3_4">
<title>Initial microbial count</title>
<p>Initial microbial counts are shown in <xref ref-type="fig" rid="F7">Figure 7</xref>. Yeast counts were higher than the total bacterial counts until the second day of inoculation, while the total bacterial counts surpassed yeast counts after Day 3 in Samples A and B. The average total bacterial count for all five samples was 7.05 log CFU/mL. For Samples C and E (which satisfied the &#x2265; 4% acidity criterion of the food code), the average initial total count was 7.39 log CFU/mL. The average yeast count across the samples was 6.76 log CFU/mL, while for Samples C and E, the yeast count was 6.32 log CFU/mL. Kombucha is known to be dominated by acetic acid bacteria and yeast (<xref ref-type="bibr" rid="ref2">Andreson <italic>et al</italic>., 2022</xref>). <xref ref-type="bibr" rid="ref11">Fabricio <italic>et al</italic>. (2023)</xref> reported an optimal inoculation level of 1 &#x00D7; 10<sup>7</sup> CFU/mL for acetic acid bacteria and 1 &#x00D7; 10<sup>5</sup> CFU/mL for yeast, which aligned with our study.</p>
<fig id="F7" orientation="portrait" position="float">
<label>Figure 7.</label>
<caption><p>Effect of inoculation dates of complex strains on initial total bacterial and yeast counts. Detailed sample information is provided in Figure 2. All values are mean &#x00B1; SD (n = 3). Means followed by the different lowercase letters at the same bar are significantly different (p&#x003C;0.05, a&#x003E;b&#x003E;c). Significant difference between bacteria and yeast of same sample by t-test. *p&#x003C;0.05, **p&#x003C;0.01, ***p&#x003C;0.001.</p></caption>
<graphic xmlns:xlink="http://www.w3.org/1999/xlink" xlink:href="IJFS-38-240-g007.tif"/>
</fig>
</sec>
<sec id="S3_5">
<title>Gluconic acid content</title>
<p>In kombucha, elevated levels of gluconic acid have been reported to correlate with enhanced quality, particularly in terms of taste (<xref ref-type="bibr" rid="ref24">Li <italic>et al</italic>., 2022</xref>). <xref ref-type="fig" rid="F8">Figure 8</xref> shows the gluconic acid levels influenced by the time of inoculation. All the samples contained detectable levels of gluconic acid, ranging from 42.27 to 95.54 mg/mL. From Samples A to D, there was little difference (42.27&#x2013;60.05 mg/mL), but Sample E showed the highest level at 95.54 mg/mL. Using collected SCOBY, <xref ref-type="bibr" rid="ref23">Li <italic>et al</italic>. (2023)</xref> reported maximum gluconic acid production of 6.11 g/L that increased 2.26 times when the SCOBY was reconstructed with a yeast-to-acetic acid bacterial ratio of 1:3. Our study achieved even higher levels that can be attributed to differences in fermentation period, strain composition, and fermentation temperature (<xref ref-type="bibr" rid="ref4">Ariff <italic>et al</italic>., 2023</xref>). Our results confirm that inoculating lactic acid bacteria and yeast on Day 3, following a 3-day prefermentation with acetic acid bacteria, offers superior fermentation outcomes for kombucha.</p>
<fig id="F8" orientation="portrait" position="float">
<label>Figure 8.</label>
<caption><p>The gluconic acid contents at different inoculation dates of complex strains. Detailed sample information is -provided in Figure 2. All values are mean &#x00B1; SD (n = 3). Means followed by the different lowercase letters at the same bar are significantly different (p&#x003C;0.05, a&#x003E;b&#x003E;c).</p></caption>
<graphic xmlns:xlink="http://www.w3.org/1999/xlink" xlink:href="IJFS-38-240-g008.tif"/>
</fig>
</sec>
</sec>
<sec id="S4">
<title>Conclusion</title>
<p>The pH of kombucha varied according to the time of inoculation of the mixed culture. There was a decrease in the pH as the pre-fermentation period of acetic acid bacteria increased, with no further change observed beyond Sample C (inoculated on Day 3). By the 25th day of mixed fermentation, a significant pH drop was observed in Samples C, D (inoculated on Day 4), and E (inoculated on Day 5) compared to Samples A (inoculated on Day 1) and B (inoculated on Day 2). In contrast, titratable acidity increased with prolonged acetic acid bacterial preincubation, stabilizing after the third day. On the 25th day, Samples A, C, and E recorded titratable acidity values of 4.28, 4.01, and 4.64%, respectively, all exceeding the 4% threshold set by Korean food regulations for vinegar products. Ethanol content peaked around Day 5 of fermentation in most samples (0.09&#x2013;0.49%). In Sample E, the highest ethanol level (0.11%) occurred on Day 10, followed by a gradual decline to 0.03&#x2013;0.04% by Day 25 of fermentation. Initial soluble solids ranged from 13.2&#x2013;14.6 &#x00B0;Brix and continued to rise throughout the 25-day fermentation. Reducing sugars also steadily increased from 58.55&#x2013;71.38 mg/mL at the beginning to 285.71&#x2013;346.46 mg/mL by the 25th day of fermentation. Sample B showed the lowest values (32.2 &#x00B0;Brix, 287.71 mg/mL), while Sample E showed the highest (67.0 &#x00B0;Brix, 346.46 mg/mL). Initial total microbial counts averaged 7.05 log CFU/mL across all the samples. Samples C and E, which achieved titratable acidity &#x2265; 4%, had an average initial total count of 7.39 log CFU/mL and a yeast count of 6.32 log CFU/mL. These values are consistent with previous findings on the optimal inoculation levels of acetic acid bacteria and yeast in kombucha production. Gluconic acid was detected in all the samples, ranging from 42.27 to 95.54 mg/mL. Although -samples A through D showed similar levels (42.27&#x2013;60.05 mg/mL), Sample E had a notably high level at 95.54 mg/mL. Our results suggest that inoculating lactic acid bacteria (<italic>L. mesenteroides</italic> SFT-45) and yeast (<italic>S. cerevisiae</italic> SFT-71) on the third day following a 3-day prefermentation with acetic acid bacteria (<italic>A. pasteurianus</italic> SFT-18 and <italic>G. oxydans</italic> SFT-27) provides optimal fermentation performance. This strategy helped to improve cost efficiency, metabolite production, microbial stability, and acidity, which are beneficial factors for industrial kombucha production.</p>
</sec>
<sec id="S5">
<title>Authors Contribution</title>
<p>Byung-kuk Choi: Writing &#x2013; review &#x0026; editing, Writing &#x2013; original draft, Validation, Methodology, Investigation, Formal analysis, Data curation, Conceptualization. Su-Hwan Kim: Writing &#x2013; review &#x0026; editing, Writing &#x2013; original draft, Validation, Methodology, Investigation, Formal analysis, Data curation, Conceptualization. Geun-Ho Song: Validation, Investigation, Formal analysis. Sang&#x2013;Ah Kim: Validation, Investigation, Formal analysis. Chang Ki Huh: Writing &#x2013; review &#x0026; editing, Supervision, Project administration, Methodology, Conceptualization.</p></sec>
</body>
<back>
<sec id="S6" sec-type="COI-statement">
<title>Conflict of Interest</title>
<p>The authors have no conflict of interest to declare.</p>
</sec>
<sec id="S7" sec-type="financial-disclosure">
<title>Funding</title>
<p>None.</p>
</sec>
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