<?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">JSBS</journal-id><journal-title-group><journal-title>Journal of Sustainable Bioenergy Systems</journal-title></journal-title-group><issn pub-type="epub">2165-400X</issn><publisher><publisher-name>Scientific Research Publishing</publisher-name></publisher></journal-meta><article-meta><article-id pub-id-type="doi">10.4236/jsbs.2023.134007</article-id><article-id pub-id-type="publisher-id">JSBS-128706</article-id><article-categories><subj-group subj-group-type="heading"><subject>Articles</subject></subj-group><subj-group subj-group-type="Discipline-v2"><subject>Engineering</subject></subj-group></article-categories><title-group><article-title>
 
 
  Biodiesel Production from &lt;i&gt;Rhynchophorus ferrugineus&lt;/i&gt; Larvae Oil: Physichochemical Properties and Acid Composition of Oil as Affected by Oil Extraction Protocol
 
</article-title></title-group><contrib-group><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Arnaude</surname><given-names>Folepe Azemo Esther</given-names></name><xref ref-type="aff" rid="aff1"><sup>1</sup></xref><xref ref-type="corresp" rid="cor1"><sup>*</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Julius</surname><given-names>K. Tangka</given-names></name><xref ref-type="aff" rid="aff2"><sup>2</sup></xref></contrib><contrib contrib-type="author" xlink:type="simple"><name name-style="western"><surname>Nsah-ko</surname><given-names>Tchoumboue</given-names></name><xref ref-type="aff" rid="aff3"><sup>3</sup></xref></contrib></contrib-group><aff id="aff2"><addr-line>Renewable Energy Laboratory, Faculty of Agronomy and Agricultural Sciences, University of Dschang, Dschang, Cameroon</addr-line></aff><aff id="aff3"><addr-line>Mechanical Engineering Department, College of Technology, University of Buea, Buea, Cameroon</addr-line></aff><aff id="aff1"><addr-line>Renewable Energy Laboratory, University of Dschang, Dschang, Cameroon</addr-line></aff><pub-date pub-type="epub"><day>31</day><month>10</month><year>2023</year></pub-date><volume>13</volume><issue>04</issue><fpage>117</fpage><lpage>130</lpage><history><date date-type="received"><day>16,</day>	<month>February</month>	<year>2023</year></date><date date-type="rev-recd"><day>28,</day>	<month>October</month>	<year>2023</year>	</date><date date-type="accepted"><day>31,</day>	<month>October</month>	<year>2023</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>
 
 
  Biodiesel, a renewable energy source made from natural oils and fats, can be produced using white raffia larvae as a raw material. These larvae have a high lipid content and a short life cycle, making them suitable for this purpose. O
  ne crucial step in biodiesel production is oil extraction, and this study aimed to investigate how the extraction protocol affects the fuel properties of the oil.
   
  To study the impact of solvent type, solvent volume,
   
  and residence time on oil yield, 200 grams of Rhynchophorus ferrugineus were used in a Soxhlet extractor. The researchers examined the physicochemical properties and fatty acid composition of the crude grease using the European biodiesel standard (EN14214) and gas chromatography methods, respectively. The study found that hexane as a solvent produced the highest oil yield (64.44%) during a four-hour extraction period with a solvent ratio of 300
   
  ml. Furthermore, the hexane-extracted oil had the highest iodine number (3.02 g/100 g) and cetane number (55.69). These values indicate favorable properties for biodiesel production.
   
  The Rhynchophorus ferrugineus larvae oil proved to be a rich source of monounsaturated fatty acids 
  (76%)
  , which were found to be significantly affected by the solvent type.
   
  Base
  d
   on quality assessment, Rhynchophorus ferrugineus can be suitable for biodiesel production. In summary, under the given operational conditions, hexane is the most suitable solvent for Rhynchophorus ferrugineus oil extraction for biodiesel production. Further research in optimizing the extraction process can contribute to the efficient utilization of renewable energy sources like white raffia larvae for biodiesel production.
 
</p></abstract><kwd-group><kwd>Biodiesel</kwd><kwd> Extraction Process</kwd><kwd> Fatty Acid Composition</kwd><kwd> Physico-Chemical Properties</kwd><kwd> &lt;i&gt;Rhynchophorus ferrugineus&lt;/i&gt; Larvae</kwd></kwd-group></article-meta></front><body><sec id="s1"><title>1. Introduction</title><p>The energy model that currently prevails is highly dependent on the usage of fossil fuels and supports various sectors such as transportation, industry, and agriculture, among others [<xref ref-type="bibr" rid="scirp.128706-ref1">1</xref>] . However, this model has become less and less viable due to the reduction in the non-renewable energy source, its increasing price, and the fact that this type of fuel favors an elevation in greenhouse gas emissions, some of which have been shown to have an impact on people’s health as they are related to various types of cancer [<xref ref-type="bibr" rid="scirp.128706-ref2">2</xref>] [<xref ref-type="bibr" rid="scirp.128706-ref3">3</xref>] [<xref ref-type="bibr" rid="scirp.128706-ref4">4</xref>] . As stated by the United Nations’ Sustainable Development Goals (SDG), regarding sustainable energy access (SDG7) and climate change (SDG13), several countries have started to take actions to reduce carbon emissions by at least 43% by 2030 and to not reach an increase in global temperature of 1.5˚C between 2030 and 2050 (IPCC, 2018) [<xref ref-type="bibr" rid="scirp.128706-ref5">5</xref>] . The supply of oil has led to geopolitical tensions, and concerns about its scarcity and environmental impact have sparked significant interest in alternative energy sources like solar, wind, and biomass energy [<xref ref-type="bibr" rid="scirp.128706-ref1">1</xref>] . Biomass biofuels are considered one of the most intriguing alternative fuels to fossil fuels [<xref ref-type="bibr" rid="scirp.128706-ref6">6</xref>] . However, they are still a topic of controversy on a global scale. The initial generation of biofuels utilizes edible plant matter, which creates a competition issue between the food and biofuel industries [<xref ref-type="bibr" rid="scirp.128706-ref7">7</xref>] . To overcome this problem, current research in bioenergy, specifically biofuel, is focusing on finding new raw materials with superior physicochemical properties. Non-edible plant matter such as Jatrophaor castor oil [<xref ref-type="bibr" rid="scirp.128706-ref8">8</xref>] , as well as microalgae [<xref ref-type="bibr" rid="scirp.128706-ref9">9</xref>] [<xref ref-type="bibr" rid="scirp.128706-ref10">10</xref>] , are being developed for biodiesel production. Nevertheless, the extraction of oil from these seeds requires significant effort due to their low efficiency, and they also have a lengthy renewal process.</p><p>As a substitute fuel, biomass biofuels appear to be one of the most interesting alternatives to fossil fuels [<xref ref-type="bibr" rid="scirp.128706-ref11">11</xref>] . Currently, there is a new source of raw materials for insect-based products, such as the Rhynchophorus ferrugineus, also known as PW [<xref ref-type="bibr" rid="scirp.128706-ref12">12</xref>] . This insect can be found in various rural areas in Cameroon, as well as in other parts of Africa and Asia [<xref ref-type="bibr" rid="scirp.128706-ref12">12</xref>] . Although PW is known to cause damage to palm, coconut, sago, and date plantations, the industry has been using insecticides to control their population [<xref ref-type="bibr" rid="scirp.128706-ref13">13</xref>] . However, it is interesting to note that Rhynchophorus has potential as a biodiesel feedstock [<xref ref-type="bibr" rid="scirp.128706-ref14">14</xref>] due to its high lipid content compared to other insects, ranging from 31.4% to 69.78% of its dry weight. Additionally, these larvae have a high reproductive capacity and require relatively little space for breeding, with each crossbreed laying 250 - 500 eggs [<xref ref-type="bibr" rid="scirp.128706-ref12">12</xref>] .</p><p>One of the important steps in biodiesel production is oil extraction. The three most commonly employed conventional oil extraction methods are mechanical, chemical (solvent), and enzymatic [<xref ref-type="bibr" rid="scirp.128706-ref15">15</xref>] . In commercial oil extraction, solvent extraction and mechanical pressing are the most commonly used methods. Most of the time, oilseed extractions are made using mechanical processes, which are time- and energy-consuming. However, solvent extraction is more efficient in terms of oil recovery [<xref ref-type="bibr" rid="scirp.128706-ref16">16</xref>] . In solvent extraction, the soxhlet method is the most known because it is simple to use and economical [<xref ref-type="bibr" rid="scirp.128706-ref17">17</xref>] . The choice of solvents for extraction plays an important role in the final outcome. Solvents used for oil extraction can affect the oil yield [<xref ref-type="bibr" rid="scirp.128706-ref18">18</xref>] , fatty acid profiles [<xref ref-type="bibr" rid="scirp.128706-ref19">19</xref>] , and physicochemical properties [<xref ref-type="bibr" rid="scirp.128706-ref20">20</xref>] . In fact, for some known raw materials like jatropha [<xref ref-type="bibr" rid="scirp.128706-ref21">21</xref>] , turber [<xref ref-type="bibr" rid="scirp.128706-ref22">22</xref>] , etc., the oil extraction protocols are already known.</p><p>Rhynchophorus ferrugineus, unlike other species, does not have sufficient research on its oil extraction process. Although there have been some studies on extracting oil from Rhynchophrus errugineus using physical extraction methods [<xref ref-type="bibr" rid="scirp.128706-ref14">14</xref>] , further investigation is needed to establish a suitable oil extraction process specifically for the larvae of this species. Hence, the objective of this study is to evaluate how different oil extraction protocols impact the fatty acid composition and physicochemical properties of Rhynchophrus errugineus.</p></sec><sec id="s2"><title>2. Materials and Methods</title><p>WPL used in this experiment were collected from the palm plantation in the forests of East Cameroon. After collection, the larvae were dried in an oven at 70˚C for 1 hour. Next, the larvae were dried and subsequently processed in a grinding mill to obtain a fine powder. This powder was further utilized for extracting oil by conducting an analysis of the impact of different solvents, time, and solvent volume on the physicochemical properties and fatty acid of oil.</p><sec id="s2_1"><title>2.1. Oil Extraction</title><sec id="s2_1_1"><title>2.1.1. Solvent Type</title><p>In order to study the effect of solvent type, two different solvents (n-hexane and petroleum ether) were independently used. Grounded larvae (5 g) were placed in a 250 cm<sup>3</sup> laboratory Soxhlet apparatus made in a porous cellulose thimble (<xref ref-type="fig" rid="fig1">Figure 1</xref>). Oil was extracted by repeated percolation using the above two organic solvents as described by Adejumo et al. [<xref ref-type="bibr" rid="scirp.128706-ref23">23</xref>] .</p></sec><sec id="s2_1_2"><title>2.1.2. Solvent Ratio and Resident Time</title><p>Twelve extraction experiments were performed to evaluate the impact of extraction time and solvent volume on extraction yield. The parameters of extraction time and solvent volume were varied based on the experimental design presented in <xref ref-type="table" rid="table1">Table 1</xref>.</p><p>After the extraction, the flask containing the solvent and oil mixture was removed, and the solvent was evaporated. The extracted oil was then dried at 100˚C for 60 minutes in an oven to eliminate any remaining solvent residue. The mass</p><table-wrap id="table1" ><label><xref ref-type="table" rid="table1">Table 1</xref></label><caption><title> Experimental design summary</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >Solvent type</th><th align="center" valign="middle" >Residence time (h)</th><th align="center" valign="middle" >Solvent quantity(ml)</th></tr></thead><tr><td align="center" valign="middle"  rowspan="6"  >Petroleum ether</td><td align="center" valign="middle"  rowspan="3"  >4</td><td align="center" valign="middle" >300</td></tr><tr><td align="center" valign="middle" >250</td></tr><tr><td align="center" valign="middle" >200</td></tr><tr><td align="center" valign="middle"  rowspan="3"  >6</td><td align="center" valign="middle" >300</td></tr><tr><td align="center" valign="middle" >250</td></tr><tr><td align="center" valign="middle" >200</td></tr><tr><td align="center" valign="middle"  rowspan="6"  >Hexane</td><td align="center" valign="middle"  rowspan="3"  >4</td><td align="center" valign="middle" >300</td></tr><tr><td align="center" valign="middle" >250</td></tr><tr><td align="center" valign="middle" >200</td></tr><tr><td align="center" valign="middle"  rowspan="3"  >6</td><td align="center" valign="middle" >300</td></tr><tr><td align="center" valign="middle" >250</td></tr><tr><td align="center" valign="middle" >200</td></tr></tbody></table></table-wrap><p>of the dried oil was measured, and the oil extraction yield was calculated using Equation (1).</p><p>Formula (1).</p><p>O y = W b − W a W b (1)</p><p>where:</p><p>O<sub>y</sub> = oil yield %;</p><p>W<sub>b</sub> = weight before extraction;</p><p>W<sub>a</sub> = Weight after extraction.</p></sec></sec><sec id="s2_2"><title>2.2. Fatty Acid Composition and Chemical Characteristic of White Palm Weevil (WPL) Crude Grease</title><sec id="s2_2_1"><title>2.2.1. Fatty Acid Composition Analysis of Crude Grease</title><p>Fatty acid profiles of WPL oil were performed in the Biochemistry Laboratory, Friedrich Alexander University of Erlangen-Nuremberg, Germany using gaz chromatography method according to the procedure of AOAC, (2000) as described by Jayanegara et al. [<xref ref-type="bibr" rid="scirp.128706-ref24">24</xref>] .</p></sec><sec id="s2_2_2"><title>2.2.2. Chemical Characteristic</title><p>a) Acid Index</p><p>The acid index was measured by titration with potassium hydroxide (ASTM D-664) as described by Asmare and Gabbiye [<xref ref-type="bibr" rid="scirp.128706-ref25">25</xref>] . For acid index determination, the oil samples were titrated in triplicate using 0.5 g &#177; 0.1 g in a 125 ml Erlenmeyer. Then 10.0 mL of ethanol and ethyl ether (1:1 mixture (v/v) and phenolphthalein drops (0.1% in ethanol) as the indicator were added. The titration was performed with an aqueous solution of KOH (0.01 mol∙L<sup>−1</sup>), properly standardized with a solution of potassium biphthalate. The volume 𝑉<sub>0</sub> of KOH used was noted at the end of the titration and the acid index was calculated using equation 2:</p><p>I a = V 1 − V 0 m &#215; 56.1 &#215; T (2)</p><p>b) Iodine Number</p><p>The Iodine Number (IN) was measured according to ASTM D664, NFT60-204 standard. For iodine number determination, approximately 0.5 g of WP larval oil was placed in a 250 ml conical flask. Cyclohexane: glacial acetic acid (1:1 V/V) (20 ml) and 10 ml of Wijs reagent solution were added into the flask. The entire solution was thoroughly mixed and kept in the dark for an hour. About 15 and 100 ml of 15% Potassium iodide (KI) and distilled water were added to the flask and the solution was titrated against 0.1 M sodium thiosulphate (Na<sub>2</sub>S<sub>2</sub>O<sub>3</sub>) solution to a colorless end point using starch as an indicator. The IV was calculated using Equation (3.3).</p><p>Iodine Value g∙I<sub>2</sub>∙g<sup>−100</sup> oil = B ∗ S ∗ M ∗ 126.9 ∗ 100 W g ∗ 1000 (3)</p><p>where B = volume 0.1 M sodium thiosulphate used in titrating the blank, S = volume of 0.1 M sodium thiosulphate used in titrating the sample, 126.9 = molar mass of iodine, M = Molarity of sodium thiosulphate, W = sample weight in gram.</p><p>c) Saponification Value</p><p>The saponification number was determined according to Ogbunuga et al., [<xref ref-type="bibr" rid="scirp.128706-ref26">26</xref>] . White palm larvae (WPL) oil weighing 5 g was placed in a flask and 50 ml of 1.0 M ethanolic potassium hydroxide (KOH) was added. The flask was connected to a reflux condenser and was refluxed for 1 h until the solution became clear. A blank sample containing only 50 ml ethanolic potassium hydroxide was similarly treated as the sample. The solution was then titrated to a faint pink color endpoint against 1.0 M hydrochloric acid (HCl) using a phenolphthalein indicator. The saponification value (SV) was calculated using Equation (3.5):</p><p>SV (mg∙KOH∙g<sup>−1</sup>) oil = ( A − B ) ∗ N ∗ 56.02 W (4)</p><p>where A = Blank ethanolic HCl volume in ml, B = sample ethanolic HCl volume in ml, N = Normality of HCl, W = Weight of sample/oil in grams.</p></sec><sec id="s2_2_3"><title>2.2.3. Physical Characteristic</title><p>Physical characteristics of white palm larvae such as cetane number (CN) and calorific value (CV) were determined. The cetane number was determined by applying Equation (5), as proposed by Molla and Nigus [<xref ref-type="bibr" rid="scirp.128706-ref27">27</xref>] , which relies on an empirical formula incorporating the saponification value and the iodine number.</p><p>C N = 46.3 + ( 5458 ∗ S V ) − ( 0.225 ∗ I N ) (5)</p><p>where CN: Cetane number;</p><p>SV: Saponification number;</p><p>IN: iodine number.</p><p>Calorific Value (CV), which represents the quantity of heat released by the complete combustion of biofuel, was calculated from Equation (6) [<xref ref-type="bibr" rid="scirp.128706-ref28">28</xref>] .</p><p>C V = 49.43 − ( 0.04 ∗ S V ) − ( 0.015 ∗ I N ) (6)</p><p>where CV: calorific value (MJ/Kg);</p><p>SV: Saponification number;</p><p>IN: iodine number.</p></sec></sec><sec id="s2_3"><title>2.3. Statistical Analysis</title><p>Each experiment was repeated three times. Data for oil extraction were subjected to the analysis of variance (ANOVA test) Duncan’s post hoc test (p ≤ 0.05) was used to determine the homogeneity subsets whenever significant differences existed among the treatments. The statistical software used was SPSS for Windows, version 2.0.</p></sec></sec><sec id="s3"><title>3. Results and Discussion</title><sec id="s3_1"><title>3.1. Effect of Extraction Protocol on WPL oil Extraction Yield</title><p>The design layout for WPL oil extraction and their responses on oil extraction yield percentage are presented in <xref ref-type="table" rid="table2">Table 2</xref>. It can be seen that the values of oil yield vary from 56.34 &#177; 2.62 to 64.44 &#177; 4.39. The oil yields recorded during this work were higher than the oil yield obtained by chemical extraction from black soldier fly larvae (30.1%; 29.1%; and 32.2%), which are the most requested insects for biodiesel production [<xref ref-type="bibr" rid="scirp.128706-ref29">29</xref>] . Additionally, they also outperformed the yield (38% to 46%) reported by Atabani et al. [<xref ref-type="bibr" rid="scirp.128706-ref15">15</xref>] for rapeseed oil extracted using Soxhlet extraction. On the other hand, the oil yield was significantly (p &lt; 0.05) affected by time, solid-to-solvent ratio, and type of solvent.</p><p>1) Effect of Solvent Type and Time on Extracted Yield</p><p>The oil yield was significantly (p &lt; 0.05) affected by three factors: time, solvent type, and solvent volume. Based on this study, the optimal oil extraction times were 4 hours for hexane and 6 hours for petroleum ether. Hexane solvent produced the highest extraction yield (64.44 &#177; 4.39) compared to petroleum ether (56.89 &#177; 1.47) This can be explained by the low dynamic viscosity of hexane, which facilitates the extraction of oil from the cells [<xref ref-type="bibr" rid="scirp.128706-ref30">30</xref>] . The extraction time specifically had a significant impact on the yield of n-hexane and petroleum ether extracted WPL oil. According to <xref ref-type="table" rid="table2">Table 2</xref>, the oil yield percentage obtained through</p><table-wrap id="table2" ><label><xref ref-type="table" rid="table2">Table 2</xref></label><caption><title> Solvent extracted Oil yield percentage</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >Reagents</th><th align="center" valign="middle" >Time</th><th align="center" valign="middle" >Solvent volume (ml)</th><th align="center" valign="middle" >Oil extraction yield (%)</th></tr></thead><tr><td align="center" valign="middle"  rowspan="6"  >Hexane</td><td align="center" valign="middle"  rowspan="3"  >4 h</td><td align="center" valign="middle" >300</td><td align="center" valign="middle" >66.44 &#177; 0.44<sup>a</sup></td></tr><tr><td align="center" valign="middle" >250</td><td align="center" valign="middle" >57.39 &#177; 2.16<sup>ab</sup></td></tr><tr><td align="center" valign="middle" >200</td><td align="center" valign="middle" >48.06 &#177; 2.1<sup>bc</sup></td></tr><tr><td align="center" valign="middle"  rowspan="3"  >6 h</td><td align="center" valign="middle" >300</td><td align="center" valign="middle" >57.04 &#177; 1.72<sup>c</sup></td></tr><tr><td align="center" valign="middle" >250</td><td align="center" valign="middle" >56.88 &#177; 0.59<sup>c</sup></td></tr><tr><td align="center" valign="middle" >200</td><td align="center" valign="middle" >42.28 &#177; 0.23<sup>bc</sup></td></tr><tr><td align="center" valign="middle"  rowspan="6"  >Petroleum ether</td><td align="center" valign="middle"  rowspan="3"  >4 h</td><td align="center" valign="middle" >300</td><td align="center" valign="middle" >56.89 &#177; 1.47<sup>c</sup></td></tr><tr><td align="center" valign="middle" >250</td><td align="center" valign="middle" >56.34 &#177; 2.62<sup>c</sup></td></tr><tr><td align="center" valign="middle" >200</td><td align="center" valign="middle" >50.56+1.5<sup>ac</sup></td></tr><tr><td align="center" valign="middle"  rowspan="3"  >6 h</td><td align="center" valign="middle" >300</td><td align="center" valign="middle" >59.77 &#177; 1.03<sup>cb</sup></td></tr><tr><td align="center" valign="middle" >250</td><td align="center" valign="middle" >61.35 &#177; 1.11<sup>b</sup></td></tr><tr><td align="center" valign="middle" >200</td><td align="center" valign="middle" >35.48 &#177; 2.1 <sup>cd</sup></td></tr></tbody></table></table-wrap><p>a, b, c: means with the same superscript are not significantly diffrent at 5%.</p><p>petroleum ether extraction increased from 56.34 to 61.35 percent as the extraction time extended from 4 to 6 hours. This observation aligns with the study conducted by [<xref ref-type="bibr" rid="scirp.128706-ref31">31</xref>] , which also found that the oil yield percentage rises with longer extraction times. However, the oil yield obtained from hexane extraction decreased with increasing reaction time, indicating that the maximum extraction yield with this solvent is obtained after 4 hours. This finding is in accordance with the research of Bayisa and Bullo, [<xref ref-type="bibr" rid="scirp.128706-ref32">32</xref>] on Croton macrostachyus seed oil extraction.</p><p>2) Effect of Solvent Volume on Extraction Yield</p><p>The results depicted in <xref ref-type="fig" rid="fig2">Figure 2</xref> show the impact of solvent volume on the extracted oil yield. The graphs indicate that increasing the amount of solvent from 200 to 250 ml led to a higher oil extraction yield for Hexane and petroleum ether solvents. This result can be explained by the increased concentration gradient between the solid and liquid phases leading to enhanced mass transfer. Similar findings were reported by Ntalikwa, [<xref ref-type="bibr" rid="scirp.128706-ref33">33</xref>] in their study on jatropha. However, increasing the solvent volume from 250 ml to 300 ml did not significantly improve the oil yield for hexane extraction at 6 hours and petroleum ether at 4 and 6 hours. The study found that the optimal oil extraction yield of 66.44% &#177; 0.44% was achieved with a solvent volume of 300 ml and a reaction time of 4 hours for hexane.</p></sec><sec id="s3_2"><title>3.2. Effect of Solvent Type on Fatty Acid Composition of WPL Oil</title><p>The effect of solvent type (hexane and petroleum ether) used for extraction on the fatty acid composition of WPL oil is presented in <xref ref-type="table" rid="table3">Table 3</xref>.</p><p>The study found that oleic acid was the predominant fatty acid in both hexane-extracted oil (56.52%) and petroleum-extracted oil (58.04%). Palmitic acid</p><table-wrap id="table3" ><label><xref ref-type="table" rid="table3">Table 3</xref></label><caption><title> Fatty acid composition of palm weevil larvae oil according to the extraction solvent type</title></caption><table><tbody><thead><tr><th align="center" valign="middle" >Fatty acid group</th><th align="center" valign="middle" >Fatty acid type</th><th align="center" valign="middle" >Hexane</th><th align="center" valign="middle" >Petroleum ether</th><th align="center" valign="middle" >p</th></tr></thead><tr><td align="center" valign="middle"  rowspan="3"  >Saturated fatty acid</td><td align="center" valign="middle" >Palmitic (16:00)</td><td align="center" valign="middle" >13.50 &#177; 0.46<sup>b</sup></td><td align="center" valign="middle" >14.13 &#177; 0.24<sup>a</sup></td><td align="center" valign="middle" >0.006</td></tr><tr><td align="center" valign="middle" >Lauric acid (12:00</td><td align="center" valign="middle" >0.59 &#177; 0.09<sup>a</sup></td><td align="center" valign="middle" >0.65 &#177; 0.16<sup>a</sup></td><td align="center" valign="middle" >0.120</td></tr><tr><td align="center" valign="middle" >Heptad&#233;canoic acid (17:00)</td><td align="center" valign="middle" >1.12 &#177; 0.19<sup>a</sup></td><td align="center" valign="middle" >1.32 &#177; 0.45<sup>a</sup></td><td align="center" valign="middle" >0.587</td></tr><tr><td align="center" valign="middle" ></td><td align="center" valign="middle" >Stearic acid (18:00)</td><td align="center" valign="middle" >4.07 &#177; 0.55<sup>b</sup></td><td align="center" valign="middle" >3.93 &#177; 0.28<sup>a</sup></td><td align="center" valign="middle" >0.048</td></tr><tr><td align="center" valign="middle" ></td><td align="center" valign="middle" >Myristic acid (14:00)</td><td align="center" valign="middle" >9.85 &#177; 0.24<sup>b</sup></td><td align="center" valign="middle" >9.27 &#177; 0.23<sup>a</sup></td><td align="center" valign="middle" >0.015</td></tr><tr><td align="center" valign="middle"  rowspan="2"  >Polyunsaturated fatty acid</td><td align="center" valign="middle" >Linoleic acid (18:02)</td><td align="center" valign="middle" >8.48 &#177; 0.18<sup>b</sup></td><td align="center" valign="middle" >10.02 &#177; 0.35<sup>a</sup></td><td align="center" valign="middle" >0.004</td></tr><tr><td align="center" valign="middle" >Linolenic acid (18:03)</td><td align="center" valign="middle" >0.36 &#177; 0.18<sup>a</sup></td><td align="center" valign="middle" >0.67 &#177; 0.10<sup>a</sup></td><td align="center" valign="middle" >0.109</td></tr><tr><td align="center" valign="middle"  rowspan="2"  >Mono unsaturated acid</td><td align="center" valign="middle" >Oleic acid (18:01)</td><td align="center" valign="middle" >58.04 &#177; 0.87<sup>b</sup></td><td align="center" valign="middle" >56.52 &#177; 0.74<sup>a</sup></td><td align="center" valign="middle" >0.036</td></tr><tr><td align="center" valign="middle" >Palmitoleic acid (16:01)</td><td align="center" valign="middle" >2.70 &#177; 0.45<sup>a</sup></td><td align="center" valign="middle" >2.50 &#177; 0.55<sup>a</sup></td><td align="center" valign="middle" >0.250</td></tr></tbody></table></table-wrap><p>a, b: means with the same superscript are not significantly diffrent at 5%.</p><p>was the second-highest fatty acid in the oil and was significantly higher (p &lt; 0.05) in petroleum-extracted oil (14.13%) compared to hexane-extracted oil. Myristic acid was also influenced by the solvent type and was higher in percentage in hexane-extracted oil (9.85%) compared to petroleum ether-extracted oil (8.45%). There were no significant differences in the levels of lauric, heptadecanoic, linolenic, or palmitoleic acid between hexane and petroleum-extracted oil. The presence of monounsaturated fatty acids (oleic and palmitoleic acid) was predominant in the oil from WPL. This finding aligns with the finding of Jedidi et al. [<xref ref-type="bibr" rid="scirp.128706-ref34">34</xref>] on Tecoma stans seed oil. The high concentration of monounsaturated fatty acids in the oil suggests that the biodiesel produced from it will have a high cetane number [<xref ref-type="bibr" rid="scirp.128706-ref35">35</xref>] , leading to improved ignition and fuel emissions [<xref ref-type="bibr" rid="scirp.128706-ref36">36</xref>] . Additionally, unsaturation in the fatty acid chain enhances the cold flow property and offers better stability and a longer shelf life to the biodiesel [<xref ref-type="bibr" rid="scirp.128706-ref37">37</xref>] . Similar results have also been reported for para-rubber seed oil [<xref ref-type="bibr" rid="scirp.128706-ref38">38</xref>] and pumpkin oil [<xref ref-type="bibr" rid="scirp.128706-ref30">30</xref>] extracted using different solvents.</p></sec><sec id="s3_3"><title>3.3. Effect on Physico-Chemical Properties of the WPL Oil</title><sec id="s3_3_1"><title>3.3.1. Acid Value</title><p>The solvent type had a significant impact on the acid value, as shown in <xref ref-type="table" rid="table4">Table 4</xref> (p &lt; 0.05). The highest acid value was observed in petroleum extracted oil, with a measurement of 4.90 mg KOH/g. The acid value of the HEO (Hexane Extracted Oil) used in this study was similar to the value of 4.37 mg KOH/g reported for R. phoenicis larvae oil [<xref ref-type="bibr" rid="scirp.128706-ref39">39</xref>] , but higher than the values of 0.4 mg KOH/g for Moringa stenopetala seed crude oil [<xref ref-type="bibr" rid="scirp.128706-ref31">31</xref>] and 0.53 mg KOH/g for jatropha oil [<xref ref-type="bibr" rid="scirp.128706-ref21">21</xref>] . However, the acid value in this study is lower than the value of 51.81 mg KOH/g reported by Atabani and colleagues [<xref ref-type="bibr" rid="scirp.128706-ref15">15</xref>] for WPL oil extract obtained with a mechanical press. This difference could be attributed to the fact that oil extracted with organic solvents tends to have a lower acid value compared to oil obtained through mechanical extraction [<xref ref-type="bibr" rid="scirp.128706-ref40">40</xref>] .</p></sec><sec id="s3_3_2"><title>3.3.2. Iodine Value</title><p>The influence of solvent type on the iodine value is evident from the data presented in <xref ref-type="table" rid="table4">Table 4</xref>. The iodine value was significantly affected by the choice of solvent (p &lt; 0.05). Specifically, the use of hexane solvent resulted in the highest iodine value of 3.02 g/100 g, whereas petroleum ether yielded a lower value of 2.05 g/100 g. The iodine value is a measure of unsaturation and serves as an indicator of the amount of double bonds present in the oil, which is related to its susceptibility to oxidation. This finding is consistent with previous research conducted by Lesten and Kingsley [<xref ref-type="bibr" rid="scirp.128706-ref30">30</xref>] , who also reported a difference in iodine values between hexane-extracted oil and petroleum-extracted oil from pumpkin seeds. Furthermore, the iodine values obtained in this study were lower than those reported by Tangka et al. [<xref ref-type="bibr" rid="scirp.128706-ref14">14</xref>] , who extracted Rhynchophorus phoenicis oil using a mechanical press and obtained a value of 36.83 g/100 g. This difference can be attributed to the lower level of double bonding (polyunsaturated acid value of 8.85%) found in the fatty acid composition of the WPL oil in our study.</p></sec><sec id="s3_3_3"><title>3.3.3. Cetane Number and Calorific Value</title><p>When R. phoenicis was extracted with hexane solvent instead of petroleum ether, the cetane number and colorific value increased (<xref ref-type="table" rid="table4">Table 4</xref>). The cetane number of WPL oil was higher than that of conventional diesel (50) and rapeseed vegetable (39) oil, [<xref ref-type="bibr" rid="scirp.128706-ref41">41</xref>] but lower than that of WPL mechanically extracted oil. This difference can be attributed to the high concentration of unsaturated fatty acids in the WPL oils obtained in this study. Oils with a higher content of saturated fatty acids have a higher cetane number and are more likely to self-ignite under compression [<xref ref-type="bibr" rid="scirp.128706-ref42">42</xref>] .</p></sec></sec></sec><sec id="s4"><title>4. Conclusion</title><p>The oil content of WPL ranged from 56.36% to 64.44% at the conclusion of this study. The results also confirm that n-hexane is a suitable solvent for the extraction of WPL oil, and the optimal conditions are as follows: extraction time of</p><table-wrap id="table4" ><label><xref ref-type="table" rid="table4">Table 4</xref></label><caption><title> Effect of solvent type (hexane and petroleum ether) used for extraction on physico-chemical properties of WPL oil</title></caption><table><tbody><thead><tr><th align="center" valign="middle"  rowspan="2"  >Extraction</th><th align="center" valign="middle" >Solvent</th><th align="center" valign="middle" >Parameters</th></tr></thead><tr><td align="center" valign="middle" >Hexane</td><td align="center" valign="middle" >Pretroleum ether</td></tr><tr><td align="center" valign="middle" >Acid value (mg/g)</td><td align="center" valign="middle" >3.58 &#177; 0.11<sup>b</sup></td><td align="center" valign="middle" >4.90 &#177; 0.18<sup>a</sup></td></tr><tr><td align="center" valign="middle" >Saponification value (mg/g)</td><td align="center" valign="middle" >535.00 &#177; 52.33<sup>b</sup></td><td align="center" valign="middle" >699.50 &#177; 6.36<sup>a</sup></td></tr><tr><td align="center" valign="middle" >Iodine number (g/100 g)</td><td align="center" valign="middle" >3.02 &#177; 0.21<sup>a</sup></td><td align="center" valign="middle" >2.05 &#177; 0.21<sup>b</sup></td></tr><tr><td align="center" valign="middle" >Cetane number</td><td align="center" valign="middle" >55.69</td><td align="center" valign="middle" >53</td></tr><tr><td align="center" valign="middle" >Calorific value (Mj/Kg)</td><td align="center" valign="middle" >27.44</td><td align="center" valign="middle" >20.68</td></tr></tbody></table></table-wrap><p>a, b: means with the same superscript are not significantly diffrent at 5%.</p><p>4 h, a volume solvent of 300 ml, extraction temperature of 68 &#176;C, and an oil yield of 64.44%. In addition, the study shows that WPL oil is a rich source of monounsaturated acids (oleic and palmitoleic acids) and palmitic acid, which is significantly affected by the solvent. Furthermore, the physicochemical properties of WPL oil in this study indicate low iodine and a high saponification value, which implies a high monounsaturated to saturated fatty acid ratio and might be an acceptable substitute for highly saturated oils such as olive oil and palm oil. The current finding demonstrated that the WPL oil has great potential to be utilized as a raw material for biodiesel production, and its full potential should be exploited.</p></sec><sec id="s5"><title>Author Contributions</title><p>This work was carried out in collaboration among all authors. Author AFEA designed the study, performed the statistical analysis, wrote the protocol and wrote the first draft of the manuscript. Authors JKT and Nsah-ko T managed the analyses of the study and the literature searches. All authors read and approved the final manuscript.</p></sec><sec id="s6"><title>Acknowledgements</title><p>This work was supported by the Renewwable Energies Laboratory of the University of Dschang, with the collaboration of Sol sciences Laboratory, and Animal Nutrition Laboratory of the same university. The author is grateful to Dr DJABOU MOUAFI Astride St&#233;phanie for bringing and carring her analysis in the Biochemistry Laboratory of the Friedrich Alexander University of Erlangen-Nuremberg.</p></sec><sec id="s7"><title>Conflicts of Interest</title><p>Authors have declared that no competing interests exist</p></sec><sec id="s8"><title>Cite this paper</title><p>Esther, A.F.A., Tangka, J.K. and Tchoumboue, N. (2023) Biodiesel Production from Rhynchophorus ferrugineus Larvae Oil: Physichochemical Properties and Acid Composition of Oil as Affected by Oil Extraction Protocol. Journal of Sustainable Bioenergy Systems, 13, 117-130. https://doi.org/10.4236/jsbs.2023.134007</p></sec></body><back><ref-list><title>References</title><ref id="scirp.128706-ref1"><label>1</label><mixed-citation publication-type="other" xlink:type="simple">Ogunkunle, O. and Ahmed, N.A. (2019) A Review of Global Current Scenario of Biodiesel Adoption and Combustion in Vehicular Diesel Engines. Energy Reports, 5, 1560-1579. https://doi.org/10.1016/j.egyr.2019.10.028</mixed-citation></ref><ref id="scirp.128706-ref2"><label>2</label><mixed-citation publication-type="other" xlink:type="simple">Kasirajan, R. (2021) Biodiesel Production by Two Step Process from an Energy Source of Chrysophyllum albidum Oil Using Homogeneous Catalyst. 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