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<front>
<journal-meta>
<journal-id journal-id-type="publisher-id">Front. Nanotechnol.</journal-id>
<journal-title>Frontiers in Nanotechnology</journal-title>
<abbrev-journal-title abbrev-type="pubmed">Front. Nanotechnol.</abbrev-journal-title>
<issn pub-type="epub">2673-3013</issn>
<publisher>
<publisher-name>Frontiers Media S.A.</publisher-name>
</publisher>
</journal-meta>
<article-meta>
<article-id pub-id-type="publisher-id">793528</article-id>
<article-id pub-id-type="doi">10.3389/fnano.2021.793528</article-id>
<article-categories>
<subj-group subj-group-type="heading">
<subject>Nanotechnology</subject>
<subj-group>
<subject>Mini Review</subject>
</subj-group>
</subj-group>
</article-categories>
<title-group>
<article-title>The Expansion of Lignocellulose Biomass Conversion Into Bioenergy <italic>via</italic> Nanobiotechnology</article-title>
<alt-title alt-title-type="left-running-head">Sankaran et&#x20;al.</alt-title>
<alt-title alt-title-type="right-running-head">Lignocellulose Biomass Conversion Into Bioenergy</alt-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname>Sankaran</surname>
<given-names>Revathy</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
</xref>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Markandan</surname>
<given-names>Kalaimani</given-names>
</name>
<xref ref-type="aff" rid="aff2">
<sup>2</sup>
</xref>
</contrib>
<contrib contrib-type="author" corresp="yes">
<name>
<surname>Khoo</surname>
<given-names>Kuan Shiong</given-names>
</name>
<xref ref-type="aff" rid="aff3">
<sup>3</sup>
</xref>
<xref ref-type="corresp" rid="c001">&#x2a;</xref>
<uri xlink:href="https://loop.frontiersin.org/people/969657/overview"/>
</contrib>
<contrib contrib-type="author" corresp="yes">
<name>
<surname>Cheng</surname>
<given-names>Chin Kui</given-names>
</name>
<xref ref-type="aff" rid="aff4">
<sup>4</sup>
</xref>
<xref ref-type="corresp" rid="c001">&#x2a;</xref>
<uri xlink:href="https://loop.frontiersin.org/people/1188721/overview"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Ashokkumar</surname>
<given-names>Veeramuthu</given-names>
</name>
<xref ref-type="aff" rid="aff5">
<sup>5</sup>
</xref>
<xref ref-type="aff" rid="aff6">
<sup>6</sup>
</xref>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Deepanraj</surname>
<given-names>B.</given-names>
</name>
<xref ref-type="aff" rid="aff7">
<sup>7</sup>
</xref>
<uri xlink:href="https://loop.frontiersin.org/people/1319805/overview"/>
</contrib>
<contrib contrib-type="author" corresp="yes">
<name>
<surname>Show</surname>
<given-names>Pau Loke</given-names>
</name>
<xref ref-type="aff" rid="aff3">
<sup>3</sup>
</xref>
<xref ref-type="corresp" rid="c001">&#x2a;</xref>
<uri xlink:href="https://loop.frontiersin.org/people/569354/overview"/>
</contrib>
</contrib-group>
<aff id="aff1">
<sup>1</sup>
<institution>Graduate School, University of Nottingham Malaysia Campus</institution>, <addr-line>Selangor</addr-line>, <country>Malaysia</country>
</aff>
<aff id="aff2">
<sup>2</sup>
<institution>Department of Chemical and Petroleum Engineering, UCSI University</institution>, <addr-line>Kuala Lumpur</addr-line>, <country>Malaysia</country>
</aff>
<aff id="aff3">
<sup>3</sup>
<institution>Department of Chemical and Environmental Engineering, Faculty of Science and Engineering, University of Nottingham Malaysia</institution>, <addr-line>Selangor Darul Ehsan</addr-line>, <country>Malaysia</country>
</aff>
<aff id="aff4">
<sup>4</sup>
<institution>Department of Chemical Engineering, College of Engineering, Khalifa University</institution>, <addr-line>Abu Dhabi</addr-line>, <country>United Arab Emirates</country>
</aff>
<aff id="aff5">
<sup>5</sup>
<institution>Faculty of Science, Center of Excellence in Catalysis for Bioenergy and Renewable Chemicals (CBRC), Chulalongkorn University</institution>, <addr-line>Bangkok</addr-line>, <country>Thailand</country>
</aff>
<aff id="aff6">
<sup>6</sup>
<institution>Department of Energy and Environmental Engineering, Saveetha School of Engineering, Saveetha Institute of Medical and Technical Sciences, Saveetha University</institution>, <addr-line>Chennai</addr-line>, <country>India</country>
</aff>
<aff id="aff7">
<sup>7</sup>
<institution>Department of Mechanical Engineering, Jyothi Engineering College</institution>, <addr-line>Thrissur</addr-line>, <country>India</country>
</aff>
<author-notes>
<fn fn-type="edited-by">
<p>
<bold>Edited by:</bold> <ext-link ext-link-type="uri" xlink:href="https://loop.frontiersin.org/people/627372/overview">Eldon R. Rene</ext-link>, IHE Delft Institute for Water Education, Netherlands</p>
</fn>
<fn fn-type="edited-by">
<p>
<bold>Reviewed by:</bold> <ext-link ext-link-type="uri" xlink:href="https://loop.frontiersin.org/people/1516846/overview">Jingmiao Zhang</ext-link>, Chongqing University, China</p>
<p>
<ext-link ext-link-type="uri" xlink:href="https://loop.frontiersin.org/people/766367/overview">Mukesh Kumar Awasthi</ext-link>, Northwest A and F University, China</p>
<p>
<ext-link ext-link-type="uri" xlink:href="https://loop.frontiersin.org/people/1516656/overview">HC Ong</ext-link>, National Yunlin University of Science and Technology, Taiwan</p>
</fn>
<corresp id="c001">&#x2a;Correspondence: Kuan Shiong Khoo, <email>kuanshiong.khoo@hotmail.com</email>, Chin Kui Cheng, <email>cheng.kui@ku.ac.ae</email>, Pau Loke Show, <email>showpauloke@gmail.com</email>
</corresp>
<fn fn-type="other">
<p>This article was submitted to Nanotechnology for Energy Applications, a section of the journal Frontiers in Nanotechnology</p>
</fn>
</author-notes>
<pub-date pub-type="epub">
<day>20</day>
<month>12</month>
<year>2021</year>
</pub-date>
<pub-date pub-type="collection">
<year>2021</year>
</pub-date>
<volume>3</volume>
<elocation-id>793528</elocation-id>
<history>
<date date-type="received">
<day>12</day>
<month>10</month>
<year>2021</year>
</date>
<date date-type="accepted">
<day>29</day>
<month>11</month>
<year>2021</year>
</date>
</history>
<permissions>
<copyright-statement>Copyright &#xa9; 2021 Sankaran, Markandan, Khoo, Cheng, Ashokkumar, Deepanraj and Show.</copyright-statement>
<copyright-year>2021</copyright-year>
<copyright-holder>Sankaran, Markandan, Khoo, Cheng, Ashokkumar, Deepanraj and Show</copyright-holder>
<license xlink:href="http://creativecommons.org/licenses/by/4.0/">
<p>This is an open-access article distributed under the terms of the Creative Commons Attribution License (CC BY). The use, distribution or reproduction in other forums is permitted, provided the original author(s) and the copyright owner(s) are credited and that the original publication in this journal is cited, in accordance with accepted academic practice. No use, distribution or reproduction is permitted which does not comply with these&#x20;terms.</p>
</license>
</permissions>
<abstract>
<p>Lignocellulosic biomass has arisen as a solution to our energy and environmental challenges because it is rich in feedstock that can be converted to biofuels. Converting lignocellulosic biomass to sugar is a complicated system involved in the bioconversion process. There are indeed a variety of techniques that have been utilized in the bioconversion process consisting of physical, chemical, and biological approaches. However, most of them have drawbacks when used on a large scale, which include the high cost of processing, the development of harmful inhibitors, and the detoxification of the inhibitors that have been produced. These constraints, taken together, hinder the effectiveness of current solutions and demand for the invention of a new, productive, cost-effective, and environmentally sustainable technique for LB processing. In this context, the approach of nanotechnology utilizing various nanomaterials and nanoparticles in treating lignocellulose biomass and bioenergy conversion has achieved increased interest and has been explored greatly in recent times. This mini review delves into the application of nanotechnological techniques in the bioconversion of lignocellulose biomass into bioenergy. This review on nanotechnological application in biomass conversion provides insights and development tools for the expansion of new sectors, resulting in excellent value and productivity, contributing to the long-term economic progress.</p>
</abstract>
<kwd-group>
<kwd>lignocellulose</kwd>
<kwd>bioconversion</kwd>
<kwd>pretreatment</kwd>
<kwd>nanotechnology</kwd>
<kwd>bioenergy</kwd>
</kwd-group>
</article-meta>
</front>
<body>
<sec id="s1">
<title>1 Introduction</title>
<sec id="s1-1">
<title>1.1 Lignocellulose</title>
<p>Lignocellulose is a generic term used to describe the cell wall of plants which constitutes of cellulose (38&#x2013;50%), hemicellulose (17&#x2013;32%), and lignin (15&#x2013;30%), where cellulose and hemicellulose consist of pentose and hexose sugar monomers, whereas lignin consists of polyphenol aromatics (<xref ref-type="bibr" rid="B28">J&#xf6;nsson and Mart&#xed;n, 2016</xref>; <xref ref-type="bibr" rid="B17">Elumalai et&#x20;al., 2018</xref>; <xref ref-type="bibr" rid="B18">Garlapati et&#x20;al., 2020</xref>). The structural functionality of lignocellulose can be elucidated as following, where cellulose forms the structure of the cell walls, while hemicellulose assists in the cross-linking between the non-cellulosic and cellulosic polymers <italic>via</italic> covalent bonding (<xref ref-type="fig" rid="F1">Figure&#x20;1</xref>). On the other hand, lignin which resembles phenol formaldehyde resin encloses the polysaccharide polymers and functions as &#x201c;glue&#x201d; to hold the lignocellulose structure together, thus providing additional mechanical strength to the cell walls for resistance from insects or during wet conditions. Besides, lignin functions as the hydrophobic barrier that enables transport of water and many essential nutrients through the cell wall. Several studies have reported that these polymeric substances are more prominent in larger concentrations within the primary and secondary cell walls of the plant, although the fractional composition may vary significantly based on their species, genetics, or environmental factors (<xref ref-type="bibr" rid="B59">Sun and Cheng, 2002</xref>).</p>
<fig id="F1" position="float">
<label>FIGURE 1</label>
<caption>
<p>Schematic illustration showing bioenergy crop (lignocellulosic biomass), where the plant cell wall is composed of lignocellulose consisting of carbohydrate polymers such as cellulose, hemicellulose, and the aromatic polymer which is known as lignin. The cellulose and hemicellulose accommodate 6 and 5 carbon sugars which are rigidly bounded with the lignin.</p>
</caption>
<graphic xlink:href="fnano-03-793528-g001.tif"/>
</fig>
<p>In recent times, research on lignocellulosic material and its conversion into bioenergy has been growing at a relentless pace owing to the dwindling fossil fuel reserves and the environmental pollution associated with the exploitation of these resources. In an attempt to gradually transit toward a bio-based economy, various renewable energy sources have been explored to date, such as solar, wind, hydrothermal, and biomass. However, biomass-derived energy has remained the only promising renewable energy source that can potentially supersede petroleum-based fuel for transportation or to produce chemicals. The high chemical energy content of lignocellulosic biomass owing to the 75% carbohydrates from cellulose and hemicellulose has been ideal for bioenergy use (<xref ref-type="bibr" rid="B11">Chen, 2014</xref>; <xref ref-type="bibr" rid="B47">Sanusi et&#x20;al., 2021</xref>). Besides, furfural, 5-hydroxymethylfurfural, and levulinic acid obtained from lignocellulose during biorefining are very favorable building blocks for the generation of energy fuels by chemical or biological synthesis processes (<xref ref-type="bibr" rid="B17">Elumalai et&#x20;al., 2018</xref>).</p>
<p>Advantageously, lignocellulosic biomass is available abundantly from agriculture and forestry with an estimated annual production of 1.7-2 &#xd7; 10<sup>11</sup> tonnes per year (<xref ref-type="bibr" rid="B17">Elumalai et&#x20;al., 2018</xref>). Besides, in 2011, 38 million tonnes of biomass were used for biofuels in the EU, out of 1.2 billion tonnes of biomass generated from various crops (<xref ref-type="bibr" rid="B48">Scarlat et&#x20;al., 2015</xref>). In addition, it is reported that by 2030, the supply of lignocellulose biomasses in the United&#x20;States alone would be 450 million dry tonnes per year, which can generate 67 million gallons of ethanol per year (<xref ref-type="bibr" rid="B62">Valdivia et&#x20;al., 2016</xref>).</p>
<p>Despite these advantages, biomasses are recalcitrant in nature owing to their cellulose crystallinity and non-reactive lignin. As such, pretreatment techniques are required to allow the cellulose to be amenable to the enzymatic hydrolysis process that subsequently assists in the extraction of fermentable sugars prior to the biofuel generation processes. Besides, technological limitations such as high cost and inadequacy in the existing infrastructure have posed major challenges in attaining high quality and yield of bioenergy from lignocellulosic material. In view of these limitations, studies have reported various optimization strategies in pretreatment stages as well as enzymes and fermentation stages to enhance bioenergy production in an energy efficient and cost-effective manner. Recently, the growing interest in nanomaterials and their exceptional properties have been vastly exploited to enhance bioenergy generation. As such, in this review, first, the fundamental principles of nanomaterials and their significance in bioenergy generation are discussed thoroughly. <xref ref-type="sec" rid="s2">Section 2</xref> will detail the application of nanotechnology for biomass conversion particularly in lignocellulosic pretreatment and for enzyme immobilization. Next, the utilization of a nanobiocatalyst in bioenergy production will be reviewed. Last, the challenges and perspectives for future progress in bioenergy generation from lignocellulosic biomasses are highlighted.</p>
</sec>
<sec id="s1-2">
<title>1.2 Fundamentals of Nanomaterials and its Significance in Bioenergy Production</title>
<p>The International Standardization Organization (ISO) has defined nanomaterials as any material having external, internal, or surface structure dimensions in the nanoscale range of 1&#x2013;100&#xa0;nm (<xref ref-type="bibr" rid="B25">ISO/TS 27687:2008 Nanotechnologies, 2008</xref>). Nanoparticles (NPs) can be broadly classified into four groups: carbonic, organic, inorganic, and composites. The characteristics of NPs are dependent on their chemical structure which influences their functionality in various environments. Besides, it is interesting to note that the physical and chemical properties of NPs vary significantly from their macro counterparts which can be exploited for use in various applications such as bioenergy, electronics, medicine, ionic liquids, and consumer products (<xref ref-type="bibr" rid="B31">Li et&#x20;al., 2005</xref>; <xref ref-type="bibr" rid="B51">Shuttleworth et&#x20;al., 2014</xref>; <xref ref-type="bibr" rid="B21">He et&#x20;al., 2020</xref>; <xref ref-type="bibr" rid="B41">Production et&#x20;al., 2020</xref>). Moreover, NPs have a faster reaction rate than larger particles while being essential in the bioenergy generation process. The faster reaction rate is associated with the extremely fine particle sizes of NPs that provide a large surface area to volume ratio which in turn increases the number of active sites for various reactions or processes to occur (<xref ref-type="bibr" rid="B36">Misson et&#x20;al., 2015</xref>).</p>
<p>From the perspective of bioenergy production, nanomaterials can be envisioned in many aspects to meet the rapidly growing global energy requirements owing to their exceptional properties such as large surface area, high catalytic activity, crystallinity, durability, stability, adsorption capability, and efficient storage (<xref ref-type="bibr" rid="B69">Zhang et&#x20;al., 2011</xref>; <xref ref-type="bibr" rid="B20">Hamawand et&#x20;al., 2020</xref>). All the aforementioned advantages of NPs can enhance the productivity, hydrolysis, and stability of cellulase enzymes for various bioenergy productions. Generally, NPs in bioenergy production can be advantageous in cellulase production, for cellulase thermal stability, in pretreatment of biomass, waste management, or sugar and biohydrogen production. For instance, in a study by Srivastava et&#x20;al., it was reported that an efficient cellulase process is essential for enzymatic hydrolysis, and the use of NPs such as Fe<sub>3</sub>O<sub>4</sub> and Fe<sub>3</sub>O<sub>4</sub>/alginate showed higher hydrolysis efficiency and enhanced cellulase production by 35 and 40% respectively (<xref ref-type="bibr" rid="B58">Srivastava et&#x20;al., 2015</xref>). A similar group of authors also investigated the efficacy of nickel cobaltite (NiCo<sub>2</sub>O<sub>4</sub>) NPs and reported 40% more cellulase production with an enhanced thermal stability at 80&#xb0;C for 7&#xa0;h (<xref ref-type="bibr" rid="B57">Srivastava et&#x20;al., 2014</xref>). The thermal and pH stability of crude cellulase have also been investigated using zinc oxide (ZnO)-based NPs, and it was shown to exhibit an enhanced thermal stability at 65&#xb0;C for 10&#xa0;h with a maximum pH alkaline value of 10.5; all of which are highly desirable in the field of bioethanol and biohydrogen production (<xref ref-type="bibr" rid="B56">Srivastava et&#x20;al., 2016</xref>). In another study by Dutta et&#x20;al., calcium hydroxyapatite-based NPs increased the thermal stability and enhanced the production of <sc>d</sc>-xylose by 35% (<xref ref-type="bibr" rid="B16">Dutta et&#x20;al., 2014</xref>). The authors reported that the uses of both nanoparticle-activated xylanase and nanoparticle-activated cellulase systems are exclusive for demonstrating high activity at elevated temperatures up to 80&#xb0;C. It was further added that utilization of cofactor calcium in an NP form conferred the increased thermostability and activity to the cellulase and xylanase enzymes.</p>
<p>Magnetic nanoparticles (MNPs) have been most commonly used in comparison with other nanoparticles in bioenergy production since the magnetic properties allow easy recoverability, and have the ability to bind to multiple target compounds, excellent biodegradability, low cytotoxicity to biomass cells, and the ease of synthesis (<xref ref-type="bibr" rid="B40">Pena et&#x20;al., 2012</xref>). The large surface area to volume ratios of MNPs have also been utilized as carriers for the immobilization of enzymes, which leads to increased stability for use in biodiesel or bioethanol production. For instance, Xie and Ma reported that immobilization on the support with magnetic Fe<sub>3</sub>O<sub>4</sub> NPs showed excellent pH tolerance and thermostability with conversion to biodiesel fuels up to 90%, while the immobilized lipase was reusable four more times without compromising its activity or performance (<xref ref-type="bibr" rid="B66">Xie and Ma, 2009</xref>). Other MNPs that were used for immobilization of enzymes include TiO<sub>2</sub> for the hydrolysis of lignocellulosic material for bioethanol production (<xref ref-type="bibr" rid="B3">Ahmad and Sardar, 2014</xref>), a mix of TiO<sub>2</sub>&#x2013;ZnO catalyst for biodiesel production (<xref ref-type="bibr" rid="B34">Madhuvilakku and Piraman, 2013</xref>), and manganese dioxide (MnO<sub>2</sub>) for bioethanol production. Moreover, the usage of nanoparticles or their microemulsion was shown to have a hydrolytic effect that is identical to that observed with chemical pretreatment in lignocellulosic biomass processing. This was seen in the study carried out by Pena and a colleague whereby when wheat straw was treated with perfluoroalkylsulfonic (PFS) and alkylsulfonic (AS) acid-functionalized magnetic nanoparticles, it produced 46% more sugar than the control (35%). The addition of nanoparticles to PFS and AS acid may have led to the stabilization and allotted hemicellulose hydrolysis which has comparable acid strength of sulfuric acid solutions (<xref ref-type="bibr" rid="B63">Wang et&#x20;al., 2012</xref>). The authors highlighted the main advantage of using magnetic nanoparticles which lies in their notable function in pretreating lignocellulosic biomass with little quantities while still being recyclable for future usage. In another study of pretreatment, the combined effect of alkaline pretreatment with magnetite (Fe<sub>3</sub>O<sub>4</sub>) nanoparticles on rice straw for biogas production was explored (<xref ref-type="bibr" rid="B29">Khalid et&#x20;al., 2019</xref>). The application of MNPs demonstrated a major advancement in biogas production that increases biogas and methane yield by 100 and 129%. Nanoparticles have also been used to improve sugar production at the pretreatment level. Yellow poplar sawdust was processed to 96 percent (w/w) hemicellulose at 175&#xb0;C using 0.8 percent (w/v) sulfuric acid. The application of sulfuric acid with PFS and AS nanomaterials converted hemicelluloses by 66 and 61%, respectively, at 50- and 400-fold acid levels (<xref ref-type="bibr" rid="B7">Arora et&#x20;al., 2020</xref>). Some other studies have reported that the high coercivity and excellent paramagnetic properties of MNPs are highly desirable for biogas and methane production. For instance, Abdelsalam et&#x20;al. reported that Fe<sub>3</sub>O<sub>4</sub> MNPs with a concentration up to 20&#xa0;mg/L reduced the time required to achieve highest biogas and methane production (<xref ref-type="bibr" rid="B1">Abdelsalam et&#x20;al., 2017</xref>). Besides, the Fe<sub>3</sub>O<sub>4</sub> MNPs assisted in the effective distribution of the iron ions in the solution which ensured a sustainable supply of iron ions in the bioreactor; all of these bio-stimulated the anaerobic digestion process, thus increasing the production of biogas and methane. <xref ref-type="table" rid="T1">Table&#x20;1</xref> summarizes some of the most recent utilization of nanoparticles to generate bioenergy such as biodiesel, bioethanol, and biogas from biomasses.</p>
<table-wrap id="T1" position="float">
<label>TABLE 1</label>
<caption>
<p>Utilization of various nanoparticles for the generation of bioenergy (biodiesel, biogas, bioethanol, and bioenergy) from biomass feedstock.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th align="left">Feedstock</th>
<th align="center">Nanoparticles</th>
<th align="center">Bioenergy</th>
<th align="center">Yield</th>
<th align="center">Ref</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td rowspan="2" align="left">Weed (<italic>Carthamus oxyacantha</italic>, <italic>Asphodelus tenuifolius</italic>, and <italic>Chenopodium album</italic>)</td>
<td rowspan="2" align="left">Nickel, cobalt</td>
<td align="left">Biodiesel</td>
<td align="left">60%</td>
<td rowspan="2" align="left">
<xref ref-type="bibr" rid="B5">Ali et&#x20;al. (2020)</xref>
</td>
</tr>
<tr>
<td align="left">Biogas</td>
<td align="left">23.75%</td>
</tr>
<tr>
<td rowspan="2" align="left">Weed (<italic>Parthenium hysterophorus</italic> L.)</td>
<td rowspan="4" align="left">Nickel, cobalt</td>
<td align="left">Biodiesel</td>
<td align="left">44%</td>
<td rowspan="4" align="left">
<xref ref-type="bibr" rid="B60">Tahir et&#x20;al. (2020)</xref>
</td>
</tr>
<tr>
<td align="left">Biogas</td>
<td align="left">17.66%</td>
</tr>
<tr>
<td rowspan="2" align="left">Weed (<italic>Cannabis sativa</italic> L.)</td>
<td align="left">Biodiesel</td>
<td align="left">53.33%</td>
</tr>
<tr>
<td align="left">Biogas</td>
<td align="left">12%</td>
</tr>
<tr>
<td rowspan="3" align="left">Spent tea</td>
<td rowspan="3" align="left">Cobalt</td>
<td align="left">Biodiesel</td>
<td align="left">40.79</td>
<td rowspan="3" align="left">
<xref ref-type="bibr" rid="B35">Mahmood and Hussain, (2010)</xref>
</td>
</tr>
<tr>
<td align="left">Biogas</td>
<td align="left">28%</td>
</tr>
<tr>
<td align="left">Bioethanol</td>
<td align="left">57.49%</td>
</tr>
<tr>
<td align="left">Wet microalgal biomass (<italic>Neochloris oleoabundans</italic> UTEX 1185)</td>
<td align="left">Fe<sub>2</sub>O<sub>3</sub>
</td>
<td align="left">Biodiesel</td>
<td align="left">81%</td>
<td align="left">
<xref ref-type="bibr" rid="B8">Banerjee et&#x20;al. (2019)</xref>
</td>
</tr>
<tr>
<td align="left">Microalgae (<italic>Chlorella vulgaris</italic>)</td>
<td align="left">CaO</td>
<td align="left">Biodiesel</td>
<td align="left">92.03%</td>
<td align="left">
<xref ref-type="bibr" rid="B39">Pandit and Fulekar, (2019)</xref>
</td>
</tr>
<tr>
<td align="left">Microalgae (<italic>Chlorella vulgaris</italic>)</td>
<td align="left">Fe<sub>3</sub>O<sub>4</sub>, silica</td>
<td align="left">Biodiesel</td>
<td align="left">97.10%</td>
<td align="left">
<xref ref-type="bibr" rid="B12">Chiang et&#x20;al. (2015)</xref>
</td>
</tr>
<tr>
<td align="left">Potato peels</td>
<td align="left">NiO</td>
<td align="left">Bioethanol</td>
<td align="left">50%</td>
<td rowspan="2" align="left">
<xref ref-type="bibr" rid="B47">Sanusi et&#x20;al. (2021)</xref>
</td>
</tr>
<tr>
<td align="left">Potato peels</td>
<td align="left">Fe<sub>3</sub>O<sub>4</sub>
</td>
<td align="left">Bioethanol</td>
<td align="left">93%</td>
</tr>
<tr>
<td align="left">Corncob</td>
<td align="left">Fe<sub>3</sub>O<sub>4</sub>
</td>
<td align="left">Bioethanol</td>
<td align="left">53.70%</td>
<td align="left">
<xref ref-type="bibr" rid="B46">Rekha and Saravanathamizhan, (2021)</xref>
</td>
</tr>
<tr>
<td align="left">Sugarcane bagasse</td>
<td align="left">Fe<sub>3</sub>O<sub>4</sub>
</td>
<td align="left">Biohydrogen</td>
<td align="left">1.21&#xa0;mol/mol substrate</td>
<td align="left">
<xref ref-type="bibr" rid="B45">Reddy et&#x20;al. (2017)</xref>
</td>
</tr>
<tr>
<td align="left">Sugarcane bagasse</td>
<td align="left">Fe<sub>3</sub>O<sub>4</sub>
</td>
<td align="left">Biohydrogen</td>
<td align="left">3427&#xa0;ml/L cumulative H<sub>2</sub>
</td>
<td align="left">
<xref ref-type="bibr" rid="B55">Srivastava et&#x20;al. (2021)</xref>
</td>
</tr>
<tr>
<td align="left">Algal biomass</td>
<td align="left">Fe<sub>3</sub>O<sub>4</sub>
</td>
<td align="left">Biohydrogen</td>
<td align="left">937&#xa0;ml/L cumulative H<sub>2</sub>
</td>
<td align="left">
<xref ref-type="bibr" rid="B49">Shanmugam et&#x20;al. (2020a)</xref>
</td>
</tr>
<tr>
<td align="left">Grass biomass (<italic>Lolium perenne</italic> L.)</td>
<td align="left">Zero-valent iron NP (Fe<sup>0</sup>)</td>
<td align="left">Biohydrogen</td>
<td align="left">64.7&#xa0;ml/g dry grass</td>
<td align="left">
<xref ref-type="bibr" rid="B67">Yang and Wang, (2018)</xref>
</td>
</tr>
<tr>
<td align="left">Sweet sorghum stover biomass</td>
<td align="left">Fe<sub>3</sub>O<sub>4</sub>, SiO<sub>2</sub>
</td>
<td align="left">Biohydrogen</td>
<td align="left">2.8&#xa0;mol H<sub>2</sub>/mol reducing sugar</td>
<td align="left">
<xref ref-type="bibr" rid="B50">Shanmugam et&#x20;al. (2020b)</xref>
</td>
</tr>
</tbody>
</table>
</table-wrap>
<table-wrap id="T2" position="float">
<label>TABLE 2</label>
<caption>
<p>Various nanomaterials used as support for enzyme immobilization.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th align="left">Nanomaterials support</th>
<th align="center">Type of biomasses/substrates</th>
<th align="center">Enzyme used</th>
<th align="center">Ref</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="left">Zinc magnetic nanoparticle</td>
<td align="left">Hemp hurds (natural cellulosic substrate)</td>
<td align="left">Cellulase</td>
<td align="left">
<xref ref-type="bibr" rid="B2">Abraham et&#x20;al. (2014)</xref>
</td>
</tr>
<tr>
<td align="left">Silica-coated crystalline Fe/Fe<sub>3</sub>O<sub>4</sub> core/shell magnetic nanoparticles</td>
<td align="left">Hemp hurd</td>
<td align="left">Cellulase</td>
<td align="left">
<xref ref-type="bibr" rid="B64">Wang et&#x20;al. (2015)</xref>
</td>
</tr>
<tr>
<td align="left">Silica nanocatalysts</td>
<td align="left">Cellulose</td>
<td align="left">Cellulase</td>
<td align="left">
<xref ref-type="bibr" rid="B10">Chang et&#x20;al. (2011)</xref>
</td>
</tr>
<tr>
<td align="left">Cyclodextrin-based magnetic nanoparticles (&#x3b2;-cyclodextrin-Fe<sub>3</sub>O<sub>4</sub>)</td>
<td align="left">Rice straw</td>
<td align="left">Cellulase (<italic>Aspergillus niger</italic>)</td>
<td align="left">
<xref ref-type="bibr" rid="B22">Huang et&#x20;al. (2015)</xref>
</td>
</tr>
<tr>
<td align="left">Fe<sub>3</sub>O<sub>4</sub>-coated chitosan magnetic nanoparticles</td>
<td align="left">&#x2014;</td>
<td align="left">Xylanase</td>
<td align="left">
<xref ref-type="bibr" rid="B33">Liu et&#x20;al. (2014)</xref>
</td>
</tr>
<tr>
<td align="left">Magnetic chitosan</td>
<td align="left">Straw cellulose</td>
<td align="left">
<italic>&#x3b2;</italic>-Glucosidase</td>
<td align="left">
<xref ref-type="bibr" rid="B70">Zheng et&#x20;al. (2013)</xref>
</td>
</tr>
<tr>
<td align="left">Superparamagnetic nanoparticles</td>
<td align="left">Cellulose</td>
<td align="left">
<italic>&#x3b2;</italic>-Glucosidase A (BglA) and cellobiohydrolase D (CelD)</td>
<td align="left">
<xref ref-type="bibr" rid="B54">Song et&#x20;al. (2016)</xref>
</td>
</tr>
<tr>
<td align="left">ZnO nanoparticles</td>
<td align="left">Cellulose</td>
<td align="left">Cellulase (<italic>Aspergillus fumigatus</italic> AA001)</td>
<td align="left">
<xref ref-type="bibr" rid="B56">Srivastava et&#x20;al. (2016)</xref>
</td>
</tr>
<tr>
<td align="left">Magnetic nanoparticles encapsulated in polymer nanospheres</td>
<td align="left">Cellulose</td>
<td align="left">Cellulase</td>
<td align="left">
<xref ref-type="bibr" rid="B32">Lima et&#x20;al. (2017)</xref>
</td>
</tr>
<tr>
<td align="left">Multiwalled carbon nanotubes (MWCNTs)</td>
<td align="left">Cellulose</td>
<td align="left">Cellulase (<italic>Aspergillus niger</italic>)</td>
<td align="left">
<xref ref-type="bibr" rid="B4">Ahmad and Khare, (2018)</xref>
</td>
</tr>
<tr>
<td align="left">Magneto-responsive graphene</td>
<td align="left">Cellulose</td>
<td align="left">Cellulase</td>
<td align="left">
<xref ref-type="bibr" rid="B19">Gokhale et&#x20;al. (2013)</xref>
</td>
</tr>
<tr>
<td align="left">Chitin-functionalized magnetic nanoparticle</td>
<td align="left">
<italic>p</italic>-nitrophenyl glycoside (pNPG)</td>
<td align="left">
<italic>&#x3b2;</italic>-Glucosidase (<italic>Thermotoga maritima</italic>)</td>
<td align="left">
<xref ref-type="bibr" rid="B6">Alnadari et&#x20;al. (2020)</xref>
</td>
</tr>
</tbody>
</table>
</table-wrap>
</sec>
</sec>
<sec id="s2">
<title>2 Application of Nanotechnology for Biomass Conversion</title>
<p>Lignocellulosic biomass has emerged as a viable remedy to the issue concerning environmental safety. It is a substantial resource for the production of energy, with an extremely large production globally. In 2011, 38 million tonnes of biomass were used for biofuels in the EU, out of 1.2 billion tonnes of biomass generated from various crops (<xref ref-type="bibr" rid="B48">Scarlat et&#x20;al., 2015</xref>). In addition, it is reported that by 2030, the supply of lignocellulose biomasses in the United&#x20;States alone would be 450 million dry tonnes per year, which can create 67 million gallons of ethanol per year (<xref ref-type="bibr" rid="B62">Valdivia et&#x20;al., 2016</xref>). The transformation of LB into fermentable sugars and bioenergy is a multistep process that necessitates precision technologies all the way down to the end result.</p>
<p>The entire conversion process of LB to significance products involves the following steps: 1) pretreatment of LB to disrupt biomass structure and make it suitable for enzymatic process, 2) enzymatic hydrolysis of components to release sugars for fermentation, and 3) fermentation to convert monomer sugars into biofuel or other biochemicals depending on the application. The <xref ref-type="fig" rid="F2">Figure&#x20;2</xref> below, shows the summary of different steps involved in the production of bioenergy via lignocellulose biomasses. The lignocellulosic biomass can be converted into bioethanol and/or biochemical products using a variety of pretreatment processes, including physical, chemical, and biological ones. However, these conventional methods are costly, inconvenient, and have some limitations. These constraints have been circumvented by introducing a unique, cost-effective, efficient, and environmentally friendly method, namely, nanotechnology. The application of nanotechnology presents a promising alternative to existing pretreatment methods. (<xref ref-type="bibr" rid="B68">Zanuso et&#x20;al., 2021</xref>).</p>
<fig id="F2" position="float">
<label>FIGURE 2</label>
<caption>
<p>Graphic representation of steps involved in the production of bioenergy using lignocellulose biomasses. The bioconversion process of lignocellulose involves several steps that begin with the pretreatment stage where the biomass is disrupted into a simpler structure for enzymatic hydrolysis. The enzymatic process involves the use of an enzyme to convert hemicellulose and cellulose into biofuel and other biochemical production either <italic>via</italic> fermentation process or direct enzymatic conversion. The valorization process comprises the conversion of lignin into various products. Valorization of lignin through thermochemical technologies can produce aromatics, bio-oil, and carbon materials.</p>
</caption>
<graphic xlink:href="fnano-03-793528-g002.tif"/>
</fig>
<sec id="s2-1">
<title>2.1 Lignocellulose Pretreatment</title>
<p>Pretreatment of LB is the first step in any bioenergy conversion which breaks down the complex structure of LB to release polymers. The pretreatment of LB is an important stage, and choosing the best pretreatment procedure is critical. However, suitable pretreatment procedures must fulfill the specific criteria, including the following: 1) improving the generation of sugars from LB or having the ability to generate sugars eventually <italic>via</italic> hydrolysis, 2) high resisting ability of the degradation or depletion of sugars, 3) they must limit the creation of by-products that obstruct succeeding hydrolysis and fermentation processes, and 4) the technique must be cost-efficient (<xref ref-type="bibr" rid="B23">Ingle et&#x20;al., 2019</xref>).</p>
<p>The nanotechnology method is widely used in numerous industries, including biofuel production (<xref ref-type="bibr" rid="B44">Rai et&#x20;al., 2019</xref>). In the nanotechnology-based approaches, nanomaterials are used, and due to their smaller size, they can easily penetrate lignocellulosic biomass cell walls and interact with lignocellulosic components (cellulose and hemicellulose) to release monomeric and oligomeric sugars (<xref ref-type="bibr" rid="B43">Rai et&#x20;al., 2017</xref>). Nanomaterials employed for pretreatment are capable of improving the chemistry of biomass at a molecular basis. Magnetic nanoparticles are preferred because they aid in their retrieval out from reaction media for reusing, as a consequence, making the entire procedure more economical (<xref ref-type="bibr" rid="B40">Pena et&#x20;al., 2012</xref>). The usage of nanoparticles or their microemulsion has been shown to have a hydrolytic effect that is identical to that seen with chemical pretreatment for LB processing. This was seen in the study carried out by Pena and a colleague whereby when wheat straw was treated with perfluoroalkylsulfonic (PFS) and alkylsulfonic (AS) acid-functionalized magnetic nanoparticles, it produced 46% that is more sugar than the control (35%). The addition of nanoparticles to PFS and AS acid may have caused the stabilization and allotted hemicellulose hydrolysis which has comparable acid strength of sulfuric acid solutions (<xref ref-type="bibr" rid="B63">Wang et&#x20;al., 2012</xref>). The main advantage of using nanoparticles is their notable function in pretreating LB substances with little quantities while still being recyclable for future usage. In another study of pretreatment, the combined effect of alkaline pretreatment with magnetite (Fe<sub>3</sub>O<sub>4</sub>) nanoparticles on rice straw for biogas production was explored. The application of magnetite nanoparticles (MNPs) demonstrated a major advancement in biogas production that increases biogas and methane yield by 100 and 129%, respectively (<xref ref-type="bibr" rid="B29">Khalid et&#x20;al., 2019</xref>). Nanoparticles have been used to improve sugar production at the pretreatment level. Yellow poplar sawdust was processed to 96 percent (w/w) hemicellulose at 175&#xb0;C using 0.8 percent (w/v) sulfuric acid. The application of sulfuric acid with PFS and AS nanomaterials converted hemicelluloses by 66 and 61%, respectively, at 50- and 400-fold acid levels (<xref ref-type="bibr" rid="B7">Arora et&#x20;al., 2020</xref>).</p>
<p>Nano-shear hybrid alkaline (NSHA) pretreatment is another emerging approach of nano-based pretreatment of LB. This technique involves a combination of high-speed shear and chemical reagent synergy, as well as a gentler thermal action. This reaction commonly is performed in a specific reactor known as nanomixing. The high shearing work axis is transported to the biomass nanostructure, allowing efficient lignin removal with cellulose and hemicellulose exposure in a short time. Wang developed a corn stover pretreatment method using the NSHA technique (<xref ref-type="bibr" rid="B65">Wang et&#x20;al., 2013</xref>). In the study of using the NSHA method, findings indicated that hemicellulose and lignin were removed from the original content, leaving with up to 82% cellulose content (<xref ref-type="bibr" rid="B7">Arora et&#x20;al., 2020</xref>). The synergetic action of cellulase enzymes degraded biomass recalcitrance and created nanoscale polysaccharide agglomeration that can be readily converted to simple sugars by NSHA pretreatment. Indeed, utilizing immobilized cellulase, the NSHA pretreatment technique exhibited a four-fold and five-fold increase in enzymatic degradation of cellulose and hemicellulose into sugars. Owing to the high shear rate of synergic effects, this mechanism indicates benefits in adding high shearing into current pretreatment procedures and many other chemical products (<xref ref-type="bibr" rid="B14">de Oliveira et&#x20;al., 2017</xref>).</p>
<p>In an alternative study of the NSHA pretreatment of corn stover, a positively charged polyelectrolyte composing poly (diallyldimethylammonium chloride) (PDAC) is employed as an additive to alter the cellulosic surfaces and stabilize lignin (<xref ref-type="bibr" rid="B15">Duque Leidy Eugenia Pe&#xf1;a, 2013</xref>). The morphology and chemical components of pretreated biomass were studied using scanning electron microscopy (SEM) and transmission electron microscopy (TEM). Lignin develops a globular aggregate with PDAC polyelectrolyte, altering the cell wall&#x2019;s shape. The procedure using polyelectrolyte offers a benefit in the reduction of chemical consumption. Despite the potential advantages, reports on biomass pretreatment utilizing nanoparticles are scarce at the moment, as the application of nanotechnology in biomass refineries is still in its infancy.</p>
</sec>
<sec id="s2-2">
<title>2.2 Enzyme Immobilization Using Nanomaterials</title>
<p>Hydrolysis of lignocellulosic biomass utilizing nanoparticles or nanomaterials can be accomplished in two approaches: physical adsorption or covalent bonding of different enzymes on nanomaterials (<xref ref-type="bibr" rid="B17">Elumalai et&#x20;al., 2018</xref>), and employing functionalized nanoparticles (<xref ref-type="bibr" rid="B18">Garlapati et&#x20;al., 2020</xref>). In the biofuel production process, enzymatic hydrolysis is considered a critical stage; however, the stability of the enzymes employed in the process is a significant concern. Nanotechnology is applied in this step as it can help to stabilize these biocatalysts. Nanotechnology has recently advanced to the point that it can be utilized to immobilize enzymes. Immobilizing enzymes on nanostructures is a novel method of improving enzyme catalytic efficiency (<xref ref-type="bibr" rid="B53">Song et&#x20;al., 2018</xref>). The term &#x201c;nanobiocatalyst&#x201d; refers to enzymes immobilized on NPs, and it is evidence of nanobiotechnology&#x2019;s constantly developing and pioneering discoveries (<xref ref-type="bibr" rid="B36">Misson et&#x20;al., 2015</xref>). Enzyme immobilization provides benefits in regards to simple enzyme reutilization, proving itself as a key tool for the development of second-generation biorefineries (<xref ref-type="bibr" rid="B68">Zanuso et&#x20;al., 2021</xref>). Because of the spacer, enzyme immobilization on nanomaterials by cross-linking causes it to be more specific for substrates and more versatile (<xref ref-type="bibr" rid="B24">Ingle et&#x20;al., 2017</xref>).</p>
<p>Adsorption, covalent bonding, entrapment/encapsulation, and cross-linking are the four basic types of immobilization strategies, based on how the enzymes engage with the support or with one another as shown in <xref ref-type="fig" rid="F3">Figure&#x20;3</xref>. Each has its pros and cons; for example, the adsorption technique is regarded as a low-cost and straightforward approach. The weakening of the interactions and the possibility of enzyme leakage when medium conditions such as pH, temperature, or polarity are altered are the major disadvantages of this approach (<xref ref-type="bibr" rid="B38">Nguyen and Kim, 2017</xref>). Because covalent bonding enhances enzyme stabilization and the generated bonds are strong enough to resist enzyme outflow, it is commonly utilized for enzyme immobilization (<xref ref-type="bibr" rid="B68">Zanuso et&#x20;al., 2021</xref>). Owing to the presence of inhibitors in lignocellulose hydrolysates, the encapsulation technique provides an advantage by its ability to generate a microenvironment that protects the enzymes from hostile environments. Cross-linking is considered a different kind of immobilization approach where it involves the creation of enzyme aggregation, also known as cross-linking enzyme aggregates (CLEAs).</p>
<fig id="F3" position="float">
<label>FIGURE 3</label>
<caption>
<p>Different strategies involved in enzyme immobilization.</p>
</caption>
<graphic xlink:href="fnano-03-793528-g003.tif"/>
</fig>
<p>The matrix utilized to immobilize enzymes differs, and it comprises nanofibers, nanoparticles (NPs), and organic metal frames, all of which serve the same purpose (<xref ref-type="bibr" rid="B30">Khoshnevisan et&#x20;al., 2017</xref>). MNPs, nickel nanoparticles (NiNPs), iron nanoparticles (FeNPs), and other metal oxide nanoparticles have all been utilized as transporters for enzyme immobilization. The table below displays nanomaterials used for enzyme immobilization in treating&#x20;LB.</p>
<p>Carbon nanotubes are a potential material for immobilizing enzymes. In a study by Tang et&#x20;al., they used the adsorption technique to immobilize glucose oxidase (GOD) on a carbon nanotube (CNT) electrode coated with platinum nanoparticles (<xref ref-type="bibr" rid="B61">Tang et&#x20;al., 2004</xref>). The use of nanotubes enhances the immobilization process. In another study, CD spectra investigation found that lipase bound to carbon nanotubes retained 62 percent of the native lipase&#x2019;s a-helix composition (<xref ref-type="bibr" rid="B27">Ji et&#x20;al., 2010</xref>). In general, enzyme immobilization on nanoparticles or other relevant support elements was used to improve the enzyme&#x2019;s characteristics, allowing it to be used in LB pretreatment operations at a lower cost. Immobilization has been shown to counteract several inhibitory effects by preventing inhibitors from binding to the enzyme&#x2019;s active site. Inhibitor tolerance may have improved as a result of this (<xref ref-type="bibr" rid="B42">Qi et&#x20;al., 2018</xref>). The thermal stability of cellulase enzymes is essential for large-scale industrial lignocellulosic operations because high temperatures enhance biomass degradation. Immobilized cellulases have higher thermal stability, which is one of their greatest benefits for large-scale production (<xref ref-type="bibr" rid="B4">Ahmad and Khare, 2018</xref>). One main limitation of cellulase immobilization is that the majority of research on cellulase immobilization employs artificial cellulose as the substrate, for instance, microcrystalline cellulose or carboxymethyl cellulose. The structure of microcrystalline seems to have a consistent diameter of approximately 20&#x2013;200&#xa0;mm, which makes for easier mass transport as contrasted to actual LCM substrates (<xref ref-type="bibr" rid="B68">Zanuso et&#x20;al., 2021</xref>). Mo et&#x20;al. proposed the construction of scaffolds with a larger specific area and open porous structure to give more locations for enzyme immobilization to address these impacts on enzyme immobilization. In addition to offering more surface area for the enzyme to uptake, an open porosity shape makes it easier for the substrate to reach the enzyme (<xref ref-type="bibr" rid="B37">Mo and Qiu, 2020</xref>).</p>
</sec>
</sec>
<sec id="s3">
<title>3 Nanobiocatalyst for Bioenergy Production</title>
<p>Despite decades of research and development work aimed at increasing the value of biomass, commercialized synthesis of bioenergy such as biodiesel and bioethanol from lignocellulose biomass thus far requires technological and economic improvement. By means of a nanotechnology application, an efficient microbial system incorporating a new metabolic pathway can be employed to produce sustainable biofuels. It is reported that with the application of nanomaterials/nanoparticles during the fermentation process, the total cost of LB to biofuel could be reduced (<xref ref-type="bibr" rid="B52">Singhvi and Kim, 2020</xref>). To enhance the production of bioethanol, more cost-effective and a variety of methods employing nanotechnology have been&#x20;used.</p>
<p>Cellulases, cellobiases, and <italic>&#x3b2;</italic>-glucosidase were some examples of enzymes that were immobilized on various NPs and employed for the bioethanol fermentation process. This process is proven to exhibit better characteristics <italic>versus</italic> free enzymes (<xref ref-type="bibr" rid="B13">Datta et&#x20;al., 2013</xref>). In a recent study of employing the immobilization technique, Verma et&#x20;al. demonstrated that by covalently immobilizing thermostable <italic>&#x3b2;</italic>-glucosidase produced from <italic>Aspergillus niger</italic> on magnetic nanoparticle, they were able to preserve approximately 50% of the enzyme following numerous recycling (<xref ref-type="bibr" rid="B6">Alnadari et&#x20;al., 2020</xref>). In performing the continuous process, one obvious benefit of immobilization is the potential to readily retrieve and recycle enzymes, as well as an enzyme-free product recovery and minimal inhibition of end product.</p>
<p>Hydrogenase enzyme plays a key role in the dark fermentation process for the production of biohydrogen. The use of nanoparticles and materials is considered a novel method for enhancing metabolic activity in the biohydrogen generation process. The employment of nanotechnology showed promise in increasing ferredoxin-oxidoreductase activities, resulting in increased electron transfer rates and enhanced catalytic efficiency (<xref ref-type="bibr" rid="B9">Bunker and Smith, 2011</xref>). In a separate study of biohydrogen production, sugarcane bagasse feedstock was hydrolyzed in a mixture of diluted sulfuric acid and titanium dioxide nanoparticles under UV light. By using this strategy, sugar and hydrogen production increased by 260 and 127%, respectively (<xref ref-type="bibr" rid="B26">Jafari and Zilouei, 2016</xref>). Most of the investigations addressed the interaction that occurs between enzymes and nanomaterials in enhancing the electron transfer rate, thus improving biohydrogen output and productivities. The lignocellulose biomass will be much more receptive to enzyme treatment for substrate hydrolysis into sugars and subsequent microbial fermentation to yield bioenergy and other bio-based products following interactions with nanobiocatalysts.</p>
</sec>
<sec id="s4">
<title>4 Conclusion and Future Perspective</title>
<p>In conclusion, the depleting fossil fuel reserves have necessitated the exploration and use of alternative resources such as lignocellulosic biomass which is an environmentally friendly approach. To address the challenges associated with biomass transformation, nanotechnology has gained importance in various applications such as in operation of catalysts and for amendments in feedstock. Besides, nanoscale instrumentation such as atomic force microscopy has assisted in measuring cellulose fibril, while other nanotechnology-based instruments have facilitated in comprehending the cell wall ultrastructure, deconstruction microscopic analysis, and enzymatic mechanisms, all of which are extremely beneficial information in the biofuel production field. On the other hand, the exceptional properties of nanomaterials such as large surface area and high catalytic activity are particularly useful to enhance the productivity of bioenergy.</p>
<p>Despite the advantages of nanotechnology and nanomaterials in the generation of bioenergy from lignocellulosic biomasses, there are several concerns that need to be addressed. For instance, immobilization <italic>via</italic> covalent binding is an essential technique to prevent leaching of enzymes during the reaction, especially while using solid materials as carriers. However, to date, the information relating to interaction between lipase and carrier is still scarce and needs further exploring to fully utilize the potential of nanomaterials in bioenergy generation. Besides, although the in-depth mechanism of toxicity due to nanoparticles has hitherto not been understood, the small size of nanoparticles such as some metal nanocatalyst may disrupt the normal functioning of human cells or induce toxicity among living organisms. Nanoparticles that exist in biofuel, when emitted as exhaust from vehicles or industries, can deposit in lung tissue <italic>via</italic> respiration, thus causing respiratory ailments such as asthma or bronchitis. As such, safety assessment is of utmost importance and needs to be addressed meticulously to minimize concerns around energy, safety, and environmental issues while utilizing nanomaterials for biofuel generation. A general concern exists with the current pretreatment technique which is considered non-economical for the generation of biofuel such as the hydrolysis process of biomass which consumes significant amount of energy. To overcome this limitation, microwave reactors for chemical processes can be considered to minimize length of reaction, thereby reducing energy consumption. A thorough investigation is also required pertaining to process intensification and its economics while using nanotechnology-based <italic>Fischer tropsch</italic> synthesis implemented in biomass-derived syngas. Besides, advancement in nanotechnology is also essential to develop more versatile nano-based catalytic systems which are capable of processing a wide variety of biomasses while also persisting impurities that may harm the bioenergy generation process such as acids or alkali metals. Nevertheless, if the overriding problems associated with lignocellulosic biomasses, their processes, and utilization of nanomaterials can be addressed, it is likely to expedite bioenergy generation which can represent a milestone in the green fuel sector.</p>
</sec>
</body>
<back>
<sec id="s5">
<title>Author Contributions</title>
<p>RS and KM wrote the first draft of the manuscript. KK, CC, and VA contributed to the conception and design of the topic. BD and PS reviewed the entire manuscript. All authors contributed to manuscript revision, read, and approved the submitted version.</p>
</sec>
<sec id="s6">
<title>Funding</title>
<p>This research was supported by the MyPAIR-PHC-Hibiscus Grant (MyPAIR/1/2020/STG05/UNIM/1) to Professor Ir Ts PS (Ministry of Higher Education, Malaysia) and Professor Eric Leroy (French Ministry of National Education, Higher Education and Research).</p>
</sec>
<sec sec-type="COI-statement" id="s7">
<title>Conflict of Interest</title>
<p>The authors declare that the research was conducted in the absence of any commercial or financial relationships that could be construed as a potential conflict of interest.</p>
</sec>
<sec sec-type="disclaimer" id="s8">
<title>Publisher&#x2019;s Note</title>
<p>All claims expressed in this article are solely those of the authors and do not necessarily represent those of their affiliated organizations, or those of the publisher, the editors, and the reviewers. Any product that may be evaluated in this article, or claim that may be made by its manufacturer, is not guaranteed or endorsed by the publisher.</p>
</sec>
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