<?xml version="1.0" encoding="UTF-8"?><!DOCTYPE article  PUBLIC "-//NLM//DTD Journal Publishing DTD v3.0 20080202//EN" "http://dtd.nlm.nih.gov/publishing/3.0/journalpublishing3.dtd"><article xmlns:mml="http://www.w3.org/1998/Math/MathML" xmlns:xlink="http://www.w3.org/1999/xlink" dtd-version="3.0" xml:lang="en" article-type="research article"><front><journal-meta><journal-id journal-id-type="publisher-id">AiM</journal-id><journal-title-group><journal-title>Advances in Microbiology</journal-title></journal-title-group><issn pub-type="epub">2165-3402</issn><publisher><publisher-name>Scientific Research Publishing</publisher-name></publisher></journal-meta><article-meta><article-id pub-id-type="doi">10.4236/aim.2024.146024</article-id><article-id pub-id-type="publisher-id">AiM-133854</article-id><article-categories><subj-group subj-group-type="heading"><subject>Articles</subject></subj-group><subj-group subj-group-type="Discipline-v2"><subject>Biomedical&amp;Life Sciences</subject></subj-group></article-categories><title-group><article-title>
 
 
  Short Communication: Enhancing the Drying Process of Microbial-Based Products with a Dehumidifier
 
</article-title></title-group><contrib-group><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Nor</surname><given-names>Hidayah Bohari</given-names></name><xref ref-type="aff" rid="aff1"><sup>1</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Elya</surname><given-names>Masya Mohd Fishal</given-names></name><xref ref-type="aff" rid="aff1"><sup>1</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Ili</surname><given-names>Bazilah Abd Razak</given-names></name><xref ref-type="aff" rid="aff1"><sup>1</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Muhammad</surname><given-names>Ashraf Arif Mohd Nasir</given-names></name><xref ref-type="aff" rid="aff1"><sup>1</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Cik</surname><given-names>Mohd Rizuan Zainal Abidin</given-names></name><xref ref-type="aff" rid="aff1"><sup>1</sup></xref></contrib></contrib-group><aff id="aff1"><addr-line>Crop Protection and Biosolutions Department, FGV R&amp;amp;D Sdn Bhd, Bandar Enstek, Malaysia</addr-line></aff><pub-date pub-type="epub"><day>06</day><month>06</month><year>2024</year></pub-date><volume>14</volume><issue>06</issue><fpage>333</fpage><lpage>339</lpage><history><date date-type="received"><day>3,</day>	<month>July</month>	<year>2023</year></date><date date-type="rev-recd"><day>15,</day>	<month>June</month>	<year>2024</year>	</date><date date-type="accepted"><day>18,</day>	<month>June</month>	<year>2024</year></date></history><permissions><copyright-statement>&#169; Copyright  2014 by authors and Scientific Research Publishing Inc. </copyright-statement><copyright-year>2014</copyright-year><license><license-p>This work is licensed under the Creative Commons Attribution International License (CC BY). http://creativecommons.org/licenses/by/4.0/</license-p></license></permissions><abstract><p>
 
 
  The development of microbial-based products requires certain criteria for them to be successfully commercialized. The product must meet the following desirable criteria: effectiveness, contamination free, stability, cost-effectiveness, and a prolonged shelf life. Controlling the drying process is crucial for ensuring the stability and durability of the product. The traditional approach, which involved mechanical and natural drying, led to decreased productivity and quality. The objective of this research endeavour was to achieve a dry process enhancement while preserving the microbial quality of 
  Trichoderma asperellum (M103). The temperature and relative humidity during the drying period were monitored under two conditions: with and without a dehumidifier. The results demonstrate that the dehumidifier increases drying period efficiency by up to 63%.
 
</p></abstract><kwd-group><kwd>Dehumidifier</kwd><kwd> Drying</kwd><kwd> Relative Humidity</kwd><kwd> Microbial-Based Product</kwd></kwd-group></article-meta></front><body><sec id="s1"><title>1. Introduction</title><p>Microbial-based products can be produced either in solid or liquid form, depending on their target and mode of application. One of the common microbial-based products that have been marketed around the world is a product containing Trichoderma sp. This fungus has been proven to function as a biocontrol agent and biostimulant for plants [<xref ref-type="bibr" rid="scirp.133854-ref1">1</xref>] [<xref ref-type="bibr" rid="scirp.133854-ref2">2</xref>] . The use of Trichoderma-based products in oil palm plantations has emerged as a promising strategy to mitigate the severity of Ganoderma infection [<xref ref-type="bibr" rid="scirp.133854-ref3">3</xref>] [<xref ref-type="bibr" rid="scirp.133854-ref4">4</xref>] . The consequential yield losses in oil palm due to Ganoderma disease have led to substantial economic setbacks in the industry [<xref ref-type="bibr" rid="scirp.133854-ref5">5</xref>] . Most of the Trichoderma-based products are typically formulated in dry powder form, employing various production methods. The preference for dry formulation was due to its simple manufacturing process, cost-effectiveness, easy handling, reduced susceptibility to contamination, and easy of store at room temperature [<xref ref-type="bibr" rid="scirp.133854-ref6">6</xref>] .</p><p>In a way to produce dried powder Trichoderma-based products, proper drying process is essential. The dried powder formulation serves to prevent microbial contamination and ensure an extended product shelf-life [<xref ref-type="bibr" rid="scirp.133854-ref7">7</xref>] . Even though drying process is a crucial step in the production of microbial-based products, the reduction of water content might cause a negative effect such as cell damaged and loss of cell viability [<xref ref-type="bibr" rid="scirp.133854-ref8">8</xref>] . The cell viability might be affected at elevated temperature during the drying process [<xref ref-type="bibr" rid="scirp.133854-ref9">9</xref>] [<xref ref-type="bibr" rid="scirp.133854-ref10">10</xref>] . Therefore, the selection of suitable drying methods for microbial-based products is important. Commonly, freeze-drying, spray-drying and fluidized bed drying are selected as the dehydration method in the production of microbial based products [<xref ref-type="bibr" rid="scirp.133854-ref7">7</xref>] [<xref ref-type="bibr" rid="scirp.133854-ref11">11</xref>] . However, the use of these three drying methods may require some new machinery with the high investment cost [<xref ref-type="bibr" rid="scirp.133854-ref9">9</xref>] [<xref ref-type="bibr" rid="scirp.133854-ref12">12</xref>] .</p><p>In this study, considering the limitations in production costs, it is crucial to adopt an economical and practical approach to improve the drying process without incurring higher additional costs. The use of dehumidifier is a common practice in various industries for managing moisture and providing a straightforward solution to excess humidity [<xref ref-type="bibr" rid="scirp.133854-ref13">13</xref>] [<xref ref-type="bibr" rid="scirp.133854-ref14">14</xref>] . The dehumidifier works by absorbing the excess moisture and changing the moisture from its vapors state to liquid state. The water vapor in the airstream condenses and is gathered in a reservoir. The dehumidified air then passes through the condenser, where it is warmed and recirculated back into the room as dry air [<xref ref-type="bibr" rid="scirp.133854-ref15">15</xref>] [<xref ref-type="bibr" rid="scirp.133854-ref16">16</xref>] . The application of dehumidifier-based drying technology was subsequently incorporated to enhance the drying process of microbial-based products.</p><p>The microbial product containing Trichoderma asperellum M103 was mass cultivated and formulated in powder form through a simple and straightforward production process involving submerged fermentation and clay-mixing procedure. Mass-scale production took place in an open-area plant, posing the potential risk of bacterial contamination. The product was air-dried at a room temperature by spreading the product on a polyethylene (PE) tarpaulin. However, this drying method was time-consuming and susceptible to weather conditions. To address these challenges, the study aimed to assess the use of a dehumidifier to enhance the drying process of the microbial-based product in powder formulation without affecting cell viability or increasing the risk of product contamination.</p></sec><sec id="s2"><title>2. Materials and Methods</title><sec id="s2_1"><title>2.1. Preparation of Microbial Culture and Submerged Fermentation</title><p>The Trichoderma asperellum M103 was acquired from the Microbial Culture Collection of the Beneficial Microbes Laboratory at FGV R&amp;D Sdn. Bhd., Malaysia. The isolate was grown on the potato dextrose agar (PDA) plate and incubated at 28˚C for 5 to 6 days. A 5 mm of M103 agar plug was transferred into Erlenmeyer flask (1 L) contains 300 mL Potato Dextrose Broth (PDB). Then the inoculated flask was incubated at orbital shaker at 100rpm and temperature of 28 &#177; 2˚C for 3 days. Next, the prepared M103 inoculum was transferred into a 30L bioreactor for mass production. The fermentation in the bioreactor took 3 to 4 days in the room temperature of 28 &#177; 2˚C.</p></sec><sec id="s2_2"><title>2.2. Clay-Mixing Process</title><p>Ready M103 culture broth was mixed with clay powder thoroughly to ensure homogeneity. The mixed product was spread on Polyethene (PE) tarpaulin for drying process (<xref ref-type="fig" rid="fig1">Figure 1</xref>). The initial moisture content after mixing process was measured by using moisture analyzer (MA160-Sartorius).</p></sec><sec id="s2_3"><title>2.3. Drying Process</title><p>The drying process was conducted in a drying room with the dimensions of 6 m (length) &#215; 6 m (width) &#215; 5 m (height) (<xref ref-type="fig" rid="fig2">Figure 2</xref>). The room temperature was maintained at a temperature of 28 &#177; 2˚C according to the optimum temperature of M103. One standing and rotating fan was used to circulate the moisture in the drying room. The microbial-based product (M103), with a capacity of 1000 kg, is spread on PE tarpaulin in the drying room with an initial moisture content of 10 to 11%. The product is left to dry until the moisture content reaches below 8% [<xref ref-type="bibr" rid="scirp.133854-ref17">17</xref>] .</p><p>During the drying process, the products were mixed three times a day to ensure that all products are dried evenly. For the experiment without a dehumidifier, the drying process was solely dependent on the fan. While, for the experiment with a dehumidifier, the relative humidity (RH) was set at 50% with the</p><p>machine running continuously. A relative humidity of 50% was selected, as many types of bacteria may not find a favorable environment for their survival under these conditions [<xref ref-type="bibr" rid="scirp.133854-ref18">18</xref>] [<xref ref-type="bibr" rid="scirp.133854-ref19">19</xref>] . This dehumidifier operates with a rotary compressor with a capacity of 50 L per day. The room temperature and relative humidity were recorded everyday by using a data logger.</p></sec></sec><sec id="s3"><title>3. Results and Discussion</title><p>The drying process of a microbial-based product cannot involve high temperatures as the microbial cell or spores might lose viability, except for thermophile bacteria or fungi. In this study, the microbial-based product (M103) was left to dry without using any heating elements. The moisture inside the product will evaporate to become water vapors, and the fan used helps to circulate the moisture inside the drying room.</p><p>In normal conditions without a dehumidifier, the drying process takes a long time to achieve the targeted moisture content of the final product. In addition, the drying process is also affected by the current weather. Sometimes, if the drying process was delayed for too long to achieve the targeted moisture content, bacterial contamination might take place. <xref ref-type="table" rid="table1">Table 1</xref> shows the RH and temperature readings in the drying room with and without the dehumidifier. The RH value decreased upon using a dehumidifier, reducing the product’s moisture content.</p><table-wrap id="table1" ><label><xref ref-type="table" rid="table1">Table 1</xref></label><caption><title> Drying room condition and product moisture content during drying process</title></caption><table><tbody><thead><tr><th align="center" valign="middle"  rowspan="2"  >Drying Day</th><th align="center" valign="middle"  colspan="3"  >Without Dehumidifier</th><th align="center" valign="middle"  colspan="3"  >With Dehumidifier (RH 50%)</th></tr></thead><tr><td align="center" valign="middle" >Drying Room, Temp (˚C)</td><td align="center" valign="middle" >Drying Room, RH (%)</td><td align="center" valign="middle" >Product Moisture Content (%)</td><td align="center" valign="middle" >Drying Room, Temp (˚C)</td><td align="center" valign="middle" >Drying Room, RH (%)</td><td align="center" valign="middle" >Product Moisture Content (%)</td></tr><tr><td align="center" valign="middle" >Initial</td><td align="center" valign="middle" >27.20</td><td align="center" valign="middle" >78.50</td><td align="center" valign="middle" >12.54</td><td align="center" valign="middle" >27.33</td><td align="center" valign="middle" >71.77</td><td align="center" valign="middle" >12.63</td></tr><tr><td align="center" valign="middle" >1</td><td align="center" valign="middle" >27.00</td><td align="center" valign="middle" >83.10</td><td align="center" valign="middle" >11.00</td><td align="center" valign="middle" >27.53</td><td align="center" valign="middle" >61.30</td><td align="center" valign="middle" >10.30</td></tr><tr><td align="center" valign="middle" >2</td><td align="center" valign="middle" >26.53</td><td align="center" valign="middle" >82.17</td><td align="center" valign="middle" >10.50</td><td align="center" valign="middle" >27.57</td><td align="center" valign="middle" >59.03</td><td align="center" valign="middle" >8.30</td></tr><tr><td align="center" valign="middle" >3</td><td align="center" valign="middle" >26.67</td><td align="center" valign="middle" >86.57</td><td align="center" valign="middle" >9.80</td><td align="center" valign="middle" >27.43</td><td align="center" valign="middle" >61.57</td><td align="center" valign="middle" >6.60</td></tr><tr><td align="center" valign="middle" >4</td><td align="center" valign="middle" >26.50</td><td align="center" valign="middle" >88.13</td><td align="center" valign="middle" >9.00</td><td align="center" valign="middle" >-</td><td align="center" valign="middle" >-</td><td align="center" valign="middle" >-</td></tr><tr><td align="center" valign="middle" >5</td><td align="center" valign="middle" >26.80</td><td align="center" valign="middle" >87.30</td><td align="center" valign="middle" >8.60</td><td align="center" valign="middle" >-</td><td align="center" valign="middle" >-</td><td align="center" valign="middle" >-</td></tr><tr><td align="center" valign="middle" >6</td><td align="center" valign="middle" >27.20</td><td align="center" valign="middle" >86.77</td><td align="center" valign="middle" >8.10</td><td align="center" valign="middle" >-</td><td align="center" valign="middle" >-</td><td align="center" valign="middle" >-</td></tr><tr><td align="center" valign="middle" >7</td><td align="center" valign="middle" >27.33</td><td align="center" valign="middle" >87.50</td><td align="center" valign="middle" >7.30</td><td align="center" valign="middle" >-</td><td align="center" valign="middle" >-</td><td align="center" valign="middle" >-</td></tr><tr><td align="center" valign="middle" >8</td><td align="center" valign="middle" >26.63</td><td align="center" valign="middle" >82.40</td><td align="center" valign="middle" >6.40</td><td align="center" valign="middle" >-</td><td align="center" valign="middle" >-</td><td align="center" valign="middle" >-</td></tr></tbody></table></table-wrap><p>According to <xref ref-type="fig" rid="fig3">Figure 3</xref>, without a dehumidifier, the drying process takes around 8 days to achieve targeted moisture content, while with a dehumidifier, it requires only 3 days. The excess moisture from the microbial-based product and surrounding area of the room were removed efficiently. In general, humidity refers to the amount of moisture or water vapor in the air [<xref ref-type="bibr" rid="scirp.133854-ref20">20</xref>] . Without a dehumidifier, the relative humidity was around 82 to 88% in the drying room. Compared to the addition of a dehumidifier, the relative humidity of the drying room can be reduced to 50 to 60% (<xref ref-type="table" rid="table1">Table 1</xref>). The dehumidifier works by removing excess moisture from the air through the condensation process.</p></sec><sec id="s4"><title>4. Conclusion</title><p>As a conclusion, the dehumidifier proves to be a useful, straightforward, and cost-effective tool for the drying process of microbial-based products, ensuring no adverse effects on their viability. Utilizing a dehumidifier enhances manufacturing efficiency by reducing the required drying time, thereby increasing the overall productivity of microbial-based products.</p></sec><sec id="s5"><title>Acknowledgements</title><p>This research was funded by FGV R&amp;D Sdn. Bhd. The authors would like to thank FGV Agriculture Services Sdn. Bhd. for lending some machinery and to Applied Air Quality Specialists Sdn. Bhd. forallowing us to rent the dehumidifier for this study.</p></sec><sec id="s6"><title>Conflicts of Interest</title><p>The authors declare no conflicts of interest regarding the publication of this paper.</p></sec><sec id="s7"><title>Cite this paper</title><p>Bohari, N.H., Fishal, E.M.M., Razak, I.B.A., Nasir, M.A.A.M. and Abidin, C.M.R.Z. (2024) Short Communication: Enhancing the Drying Process of Microbial-Based Products with a Dehumidifier. 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