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<front>
<journal-meta>
<journal-id journal-id-type="publisher-id">Front. Bioeng. Biotechnol.</journal-id>
<journal-title>Frontiers in Bioengineering and Biotechnology</journal-title>
<abbrev-journal-title abbrev-type="pubmed">Front. Bioeng. Biotechnol.</abbrev-journal-title>
<issn pub-type="epub">2296-4185</issn>
<publisher>
<publisher-name>Frontiers Media S.A.</publisher-name>
</publisher>
</journal-meta>
<article-meta>
<article-id pub-id-type="doi">10.3389/fbioe.2021.677963</article-id>
<article-categories>
<subj-group subj-group-type="heading">
<subject>Bioengineering and Biotechnology</subject>
<subj-group>
<subject>Original Research</subject>
</subj-group>
</subj-group>
</article-categories>
<title-group>
<article-title>Valorization of Enzymatic Hydrolysis Residues from Corncob into Lignin-Containing Cellulose Nanofibrils and Lignin Nanoparticles</article-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name><surname>Xu</surname> <given-names>Rui</given-names></name>
<xref ref-type="aff" rid="aff1"><sup>1</sup></xref>
<xref ref-type="aff" rid="aff2"><sup>2</sup></xref>
<xref ref-type="author-notes" rid="fn002"><sup>&#x2020;</sup></xref>
<uri xlink:href="http://loop.frontiersin.org/people/1268134/overview"/>
</contrib>
<contrib contrib-type="author">
<name><surname>Du</surname> <given-names>Haishun</given-names></name>
<xref ref-type="aff" rid="aff3"><sup>3</sup></xref>
<xref ref-type="author-notes" rid="fn002"><sup>&#x2020;</sup></xref>
<uri xlink:href="http://loop.frontiersin.org/people/1258956/overview"/>
</contrib>
<contrib contrib-type="author">
<name><surname>Wang</surname> <given-names>Hui</given-names></name>
<xref ref-type="aff" rid="aff1"><sup>1</sup></xref>
<xref ref-type="author-notes" rid="fn002"><sup>&#x2020;</sup></xref>
</contrib>
<contrib contrib-type="author">
<name><surname>Zhang</surname> <given-names>Meng</given-names></name>
<xref ref-type="aff" rid="aff1"><sup>1</sup></xref>
</contrib>
<contrib contrib-type="author">
<name><surname>Wu</surname> <given-names>Meiyan</given-names></name>
<xref ref-type="aff" rid="aff2"><sup>2</sup></xref>
</contrib>
<contrib contrib-type="author">
<name><surname>Liu</surname> <given-names>Chao</given-names></name>
<xref ref-type="aff" rid="aff2"><sup>2</sup></xref>
</contrib>
<contrib contrib-type="author">
<name><surname>Yu</surname> <given-names>Guang</given-names></name>
<xref ref-type="aff" rid="aff2"><sup>2</sup></xref>
</contrib>
<contrib contrib-type="author">
<name><surname>Zhang</surname> <given-names>Xinyu</given-names></name>
<xref ref-type="aff" rid="aff3"><sup>3</sup></xref>
<uri xlink:href="http://loop.frontiersin.org/people/321426/overview"/>
</contrib>
<contrib contrib-type="author" corresp="yes">
<name><surname>Si</surname> <given-names>Chuanling</given-names></name>
<xref ref-type="aff" rid="aff1"><sup>1</sup></xref>
<xref ref-type="corresp" rid="c001"><sup>&#x002A;</sup></xref>
<uri xlink:href="http://loop.frontiersin.org/people/120648/overview"/>
</contrib>
<contrib contrib-type="author" corresp="yes">
<name><surname>Choi</surname> <given-names>Sun-Eun</given-names></name>
<xref ref-type="aff" rid="aff4"><sup>4</sup></xref>
<xref ref-type="corresp" rid="c002"><sup>&#x002A;</sup></xref>
<uri xlink:href="http://loop.frontiersin.org/people/1246808/overview"/>
</contrib>
<contrib contrib-type="author" corresp="yes">
<name><surname>Li</surname> <given-names>Bin</given-names></name>
<xref ref-type="aff" rid="aff2"><sup>2</sup></xref>
<xref ref-type="corresp" rid="c003"><sup>&#x002A;</sup></xref>
</contrib>
</contrib-group>
<aff id="aff1"><sup>1</sup><institution>Tianjin Key Laboratory of Pulp and Paper, Tianjin University of Science and Technology</institution>, <addr-line>Tianjin</addr-line>, <country>China</country></aff>
<aff id="aff2"><sup>2</sup><institution>Key Laboratory of Biofuels, Qingdao Institute of Bioenergy and Bioprocess Technology, Chinese Academy of Sciences</institution>, <addr-line>Qingdao</addr-line>, <country>China</country></aff>
<aff id="aff3"><sup>3</sup><institution>Department of Chemical Engineering, Auburn University</institution>, <addr-line>Auburn, AL</addr-line>, <country>United States</country></aff>
<aff id="aff4"><sup>4</sup><institution>Department of Forest Biomaterials Engineering, College of Forest and Environmental Sciences, Kangwon National University</institution>, <addr-line>Chuncheon</addr-line>, <country>South Korea</country></aff>
<author-notes>
<fn fn-type="edited-by"><p>Edited by: Xin Zhou, Nanjing Forestry University, China</p></fn>
<fn fn-type="edited-by"><p>Reviewed by: Bo Pang, Max Planck Institute of Colloids and Interfaces, Germany; Jing Shen, Northeast Forestry University, China</p></fn>
<corresp id="c001">&#x002A;Correspondence: Chuanling Si, <email>sichli@tust.edu.cn</email></corresp>
<corresp id="c002">Sun-Eun Choi, <email>oregonin@kangwon.ac.kr</email></corresp>
<corresp id="c003">Bin Li, <email>libin@qibebt.ac.cn</email></corresp>
<fn fn-type="other" id="fn002"><p><sup>&#x2020;</sup>These authors have contributed equally to this work and share first authorship</p></fn>
<fn fn-type="other" id="fn004"><p>This article was submitted to Industrial Biotechnology, a section of the journal Frontiers in Bioengineering and Biotechnology</p></fn>
</author-notes>
<pub-date pub-type="epub">
<day>16</day>
<month>04</month>
<year>2021</year>
</pub-date>
<pub-date pub-type="collection">
<year>2021</year>
</pub-date>
<volume>9</volume>
<elocation-id>677963</elocation-id>
<history>
<date date-type="received">
<day>08</day>
<month>03</month>
<year>2021</year>
</date>
<date date-type="accepted">
<day>15</day>
<month>03</month>
<year>2021</year>
</date>
</history>
<permissions>
<copyright-statement>Copyright &#x00A9; 2021 Xu, Du, Wang, Zhang, Wu, Liu, Yu, Zhang, Si, Choi and Li.</copyright-statement>
<copyright-year>2021</copyright-year>
<copyright-holder>Xu, Du, Wang, Zhang, Wu, Liu, Yu, Zhang, Si, Choi and Li</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 terms.</p></license>
</permissions>
<abstract>
<p>As a kind of biomass waste, enzymatic hydrolysis residues (EHRs) are conventionally burned or just discarded, resulting in environmental pollution and low economic benefits. In this study, EHRs of corncob residues (CCR) were used to produce high lignin-containing cellulose nanofibrils (LCNFs) and lignin nanoparticles (LNPs) through a facile approach. The LCNFs and LNPs with controllable chemical compositions and properties were produced by tuning the enzymolysis time of CCR and the followed homogenization. The morphology, thermal stability, chemical and crystalline structure, and dispersibility of the resultant LCNFs and LNPs were further comprehensively investigated. This work not only promotes the production of lignocellulose-based nanomaterials but also provides a promising utilization pathway for EHRs.</p>
</abstract>
<kwd-group>
<kwd>lignin-containing cellulose nanofibrils</kwd>
<kwd>enzymatic hydrolysis residues</kwd>
<kwd>homogenization</kwd>
<kwd>corncob</kwd>
<kwd>lignin nanoparticles</kwd>
</kwd-group>
<counts>
<fig-count count="7"/>
<table-count count="1"/>
<equation-count count="0"/>
<ref-count count="69"/>
<page-count count="10"/>
<word-count count="0"/>
</counts>
</article-meta>
</front>
<body>
<sec id="S1">
<title>Introduction</title>
<p>In recent years, along with the increasing concerns derived from fossil resource dependence and environmental pollution, lignocellulosic biomass has been regarded as an alternative source of biofuels and bio-based products because of its large amount of stock and renewability (<xref ref-type="bibr" rid="B61">Xu et al., 2016</xref>; <xref ref-type="bibr" rid="B28">Li et al., 2019</xref>, <xref ref-type="bibr" rid="B27">2020</xref>; <xref ref-type="bibr" rid="B31">Lin et al., 2020</xref>; <xref ref-type="bibr" rid="B66">Yang et al., 2020</xref>; <xref ref-type="bibr" rid="B34">Liu K. et al., 2021</xref>; <xref ref-type="bibr" rid="B69">Zheng et al., 2021b</xref>). It is worth noting that agricultural residues such as wheat straw, corn stalk, bagasse, and corncob are renewable lignocellulosic biomass yet not properly managed or utilized (<xref ref-type="bibr" rid="B2">Anwar et al., 2019</xref>). It has been reported that approximately 900 million tons of agricultural wastes were produced in China each year (<xref ref-type="bibr" rid="B36">Liu et al., 2019</xref>; <xref ref-type="bibr" rid="B62">Xu et al., 2019</xref>; <xref ref-type="bibr" rid="B5">Chen et al., 2020</xref>). However, most of the agricultural wastes are often disposed by burning, which results in low economic benefits and causes severe environmental pollution. Recently, burning of agricultural waste is strictly forbidden to protect the environment and achieve the target carbon neutrality in China. Thus, it is of great importance to valorize these agricultural wastes into valuable products by using sustainable and environmentally friendly processes (<xref ref-type="bibr" rid="B64">Xu et al., 2020</xref>).</p>
<p>Recent studies suggested that converting the cellulose and hemicellulose of biomass to monomeric sugars and biofuels could be a great road to meeting the urgent need for renewable alternative carbon resources (<xref ref-type="bibr" rid="B42">Robertson et al., 2017</xref>; <xref ref-type="bibr" rid="B21">Huang et al., 2019</xref>; <xref ref-type="bibr" rid="B30">Lin et al., 2019</xref>). Among the agricultural wastes, corncob has been widely concerned for its richness in hemicellulose, which is often used to produce xylose, xylitol, xylo-oligosaccharides, or furfural (<xref ref-type="bibr" rid="B50">Si et al., 2009b</xref>, <xref ref-type="bibr" rid="B49">2013b</xref>; <xref ref-type="bibr" rid="B67">Zhang et al., 2014</xref>; <xref ref-type="bibr" rid="B19">Hu et al., 2016</xref>; <xref ref-type="bibr" rid="B32">Liu et al., 2016</xref>; <xref ref-type="bibr" rid="B23">Huang et al., 2020b</xref>). However, a large amount of corncob residue is produced and it is usually used for burning to generate heat or electricity, cultivation, feed, or just discarded. Yet, corncob residues contain abundant cellulose and lignin, which provide the possibility of creating useful materials from waste biomass, which would enable us to replace artificial and non-renewable resources with renewable resources (<xref ref-type="bibr" rid="B24">Kaneko et al., 2006</xref>; <xref ref-type="bibr" rid="B48">Si et al., 2009a</xref>, <xref ref-type="bibr" rid="B47">2013a</xref>). Also, enzymatic hydrolysis of corncob residue is commonly used to produce sugar/ethanol (<xref ref-type="bibr" rid="B60">Xie et al., 2018b</xref>; <xref ref-type="bibr" rid="B63">Xu et al., 2021</xref>). However, the high production cost of enzymatic hydrolysis prevents its large-scale utilization (<xref ref-type="bibr" rid="B29">Lin and Lu, 2021</xref>; <xref ref-type="bibr" rid="B33">Liu H. Y. et al., 2021</xref>). Thus, apart from optimizing the enzymolysis process parameters, making better use of the solid residues produced after enzymatic hydrolysis could be a feasible method to reduce the total cost, based on the concept of integrated biorefinery.</p>
<p>As a kind of biomass waste, enzymatic hydrolysis residues (EHRs) are conventionally burned for heat and power generation, resulting in low economic benefits. Actually, the EHRs contain a significant amount of lignin, a small amount of cellulose, as well as some extractives and ash, and a trace amount of hemicellulose. As a primary starting material, the EHRs are qualified to produce lignocellulosic nanomaterials (<xref ref-type="bibr" rid="B25">Khan et al., 2018</xref>). Moreover, the abundant lignin existing in EHRs would play a good role in some properties such as thermal stability, antioxidation properties, hydrophobicity, and stabilization (<xref ref-type="bibr" rid="B40">Peng et al., 2018</xref>; <xref ref-type="bibr" rid="B1">An et al., 2019</xref>). By the way, in the actual industrial production, high solid enzymatic hydrolysis residue has more universal application. Thanks to the special structure of EHRs, the fiber is in a scattered and short form with a significant amount of lignin. Usually, fiber with a high content of lignin is difficult to disintegrate down to nanoscale due to the cross-linked barrier properties of lignin.</p>
<p>Lignocellulosic nanomaterials have received much attention at the forefront of bio-based economy in which renewable biomass is used as the raw material for the production of various consumer products (<xref ref-type="bibr" rid="B44">Salas et al., 2014</xref>; <xref ref-type="bibr" rid="B53">Song, 2019</xref>; <xref ref-type="bibr" rid="B7">Dai et al., 2020a</xref>). Recently, cellulose nanomaterials, mainly including cellulose nanocrystals (CNCs) and nanofibers (CNFs), have attracted rapidly growing interest from both academic and industrial researchers due to their superior physiochemical properties (<xref ref-type="bibr" rid="B11">Du et al., 2019</xref>; <xref ref-type="bibr" rid="B20">Huang et al., 2020a</xref>; <xref ref-type="bibr" rid="B35">Liu et al., 2020</xref>; <xref ref-type="bibr" rid="B37">Miao et al., 2020</xref>; <xref ref-type="bibr" rid="B56">Wang P. et al., 2020</xref>). However, the preparation of cellulose nanomaterials is facing several challenges such as complicated purification and pretreatment process, large amount of chemical and energy consumption, and environmental issues, which limited their large-scale applications (<xref ref-type="bibr" rid="B59">Xie et al., 2018a</xref>; <xref ref-type="bibr" rid="B8">Dai et al., 2020b</xref>; <xref ref-type="bibr" rid="B55">Wang H. et al., 2020</xref>). Fortunately, recent studies showed that lignin-containing cellulose nanomaterials can be obtained directly from raw materials via sustainable and low-cost approaches, and the presence of lignin endows the LCNM with many advantages such as improved thermal stability, UV-blocking performance, and water barrier property (<xref ref-type="bibr" rid="B38">Nair et al., 2017</xref>; <xref ref-type="bibr" rid="B57">Wang et al., 2018</xref>; <xref ref-type="bibr" rid="B13">Farooq et al., 2019</xref>; <xref ref-type="bibr" rid="B17">Hong et al., 2020</xref>). Especially in the last few years, lignin-containing cellulose nanofibrils (LCNFs) have been gradually arousing people&#x2019;s interest. The preparation of LCNFs was confirmed by various approaches from different lignocellulose biomass including unbleached thermomechanical pulp, corn husk, and tobacco stalks, among others (<xref ref-type="bibr" rid="B3">Bian et al., 2017</xref>; <xref ref-type="bibr" rid="B18">Hu et al., 2018</xref>; <xref ref-type="bibr" rid="B57">Wang et al., 2018</xref>; <xref ref-type="bibr" rid="B58">Wen et al., 2019</xref>). In addition, lignin nanoparticles (LNPs) have gained significant interest among researchers in recent years, which will play a vital role in promoting lignin valorization (<xref ref-type="bibr" rid="B4">Chauhan, 2020</xref>; <xref ref-type="bibr" rid="B9">Dong et al., 2020a</xref>). It should be noted that EHRs contain much more lignin compared to unbleached pulp and most of lignocellulosic biomass (<xref ref-type="bibr" rid="B22">Huang et al., 2018</xref>), and it is expected that LCNFs with high lignin content or LNPs can be produced from EHRs.</p>
<p>In this work, the preparation of EHRs with different enzymatic hydrolysis times (48, 72, and 108 h, respectively, for comparison) was done in accordance with the previous work of our group (<xref ref-type="bibr" rid="B6">Chi et al., 2019</xref>), and subsequently, high-pressure homogenization treatment of the obtained EHR samples was carried out to produce LCNFs or LNPs. The physiochemical properties of the obtained LCNFs and LNPs were further comprehensively investigated. This work will promote the development of lignocellulose-based nanomaterials and provide a promising pathway for the full utilization of agricultural wastes.</p>
</sec>
<sec id="S2" sec-type="materials|methods">
<title>Materials and Methods</title>
<sec id="S2.SS1">
<title>Materials</title>
<p>Corncob residue (CCR) was purchased from Futaste Co., Ltd. (China), where corncob was used as raw material for the manufacture of xylose and xylitol using dilute acid hydrolysis. All the chemicals (e.g., KOH, H<sub>2</sub>SO<sub>4</sub>) used in this study were purchased from Sinopharm Chemical Reagent Co. Ltd. and used directly without further purification. Cellulase enzyme was obtained from Qingdao Vland Biotech Inc. The activity of cellulase was 85 FPU mL<sup>&#x2013;1</sup>, which was measured by the standard procedure (<xref ref-type="bibr" rid="B15">Ghose, 1987</xref>) and the protein content of cellulase was 80 mg-protein per mL, as determined by the standard Bradford method.</p>
</sec>
<sec id="S2.SS2">
<title>Preparation of LCNFs or LNPs</title>
<sec id="S2.SS2.SSS1">
<title>Alkaline Pretreatment of CCR</title>
<p>To improve the enzymatic hydrolysis efficiency of cellulose and effectively utilize the alkali lignin components, the as-received CCR was pretreated with 16 wt.% KOH at 70&#x00B0;C for 90 min following the procedure reported previously (<xref ref-type="bibr" rid="B6">Chi et al., 2019</xref>). After alkaline pretreatment, the collected solid was washed with distilled water to neutral pH and stored at 4&#x00B0;C.</p>
</sec>
<sec id="S2.SS2.SSS2">
<title>Enzymatic Hydrolysis</title>
<p>Enzymatic hydrolysis of the alkaline-pretreated CCR was conducted with a high solid content (20%) under 50&#x00B0;C for different hydrolysis times (48, 72, and 108 h, respectively), and the enzyme dosage for saccharification was 15 FPU/g-cellulose. Finally, the EHRs were obtained by filtration and washed to neutral pH and stored at 4&#x00B0;C.</p>
</sec>
<sec id="S2.SS2.SSS3">
<title>High-Pressure Homogenization</title>
<p>The obtained EHR samples were converted to LCNFs or LNPs using a high-pressure homogenizer (GYB49-10s, China). The EHRs treated in different enzymatic hydrolysis times (named EHRs-48 h, EHRs-72 h, and EHRs-108 h, respectively) were homogenized at a concentration of 2 wt.% in deionized water for three times at 30 MPa and then five times at 60 MPa. The obtained products were noted as LCNFs-48 h, LCNFs-72 h, and LNPs-108 h, respectively.</p>
</sec>
</sec>
<sec id="S2.SS3">
<title>Analytical Method for Composition</title>
<p>The composition of EHRs was determined following the National Renewable Energy Laboratory procedure (NREL). A dried EHR sample (0.30 g) was treated with 3 mL of 72% (w/w) H<sub>2</sub>SO<sub>4</sub> at 30&#x00B0;C for 60 min. Then, the acid concentration was diluted to 4% (w/w) by adding deionized water, and the samples were further hydrolyzed at 121&#x00B0;C for 60 min. The residue (Klason lignin) was filtered with deionized water under vacuum and then dried at 105&#x00B0;C to constant weight. The carbohydrate content in the supernatant was quantified by high-performance liquid chromatography system (HPLC, Waters-1525, United States) analysis. The contents of cellulose and hemicellulose of EHR samples were calculated based on the amount of corresponding monomeric sugars (<xref ref-type="bibr" rid="B52">Sluiter et al., 2008</xref>).</p>
</sec>
<sec id="S2.SS4">
<title>Morphology Analysis</title>
<p>The microstructure of samples was investigated by an S-4800 field-emission scanning electron microscope (SEM, Hitachi, Japan). After homogenization, the samples of LCNFs and LNPs were freeze dried. The freeze-dried samples were sprinkled on a conductive adhesive tape mounted on a specimen stub and coated with gold by a sputter coater (E-1045, Hitachi, Tokyo, Japan) before observation.</p>
<p>A transmission electron microscope (TEM, Hitachi, H-7650) was also used to investigate the microstructure of samples. LCNF or LNP suspensions with a concentration of 0.03% were deposited on carbon-coated TEM grids. After the drying process, the specimen was stained with 2% uranyl acetate solution for 1.5 h. Then, the excess staining solution was removed, and the samples were dried at ambient before characterization.</p>
</sec>
<sec id="S2.SS5">
<title>Thermogravimetric (TG) Analysis</title>
<p>The thermal stability of the freeze-dried samples was evaluated using a TGA Q600 (TA Instruments, United States) instrument at temperatures ranging from 25 to 550&#x00B0;C. The experiment was carried out under a nitrogen atmosphere at a heating rate of 8&#x00B0;C/min (<xref ref-type="bibr" rid="B65">Yang et al., 2007</xref>).</p>
</sec>
<sec id="S2.SS6">
<title>Fourier Transform Infrared Spectroscopy (FTIR)</title>
<p>FTIR spectra of EHR samples were determined using a FTIR spectrometer (Nicolet-6700, America) with a wavenumber region of 4,000&#x2013;500 cm<sup>&#x2013;1</sup>. Freeze-dried samples were diluted with KBr using a KBr tableting process before FTIR analysis.</p>
</sec>
<sec id="S2.SS7">
<title>X-Ray Diffraction (XRD) Analysis</title>
<p>XRD analysis was conducted using an ADVANCE D8 X-ray diffractometer (Bruker Co., Germany) equipped with a Ni-filtered Cu K&#x03B1; radiation operated at 40 kV and 30 mA. Briefly, 0.2 g freeze-dried samples was compressed into a pellet to record patterns from 5&#x00B0; to 60&#x00B0; of diffraction with a scan rate of 4&#x00B0;/min. The crystallinity index (CrI) was calculated according to Segal&#x2019;s method (<xref ref-type="bibr" rid="B46">Segal et al., 1959</xref>) with the subtraction of background of glass.</p>
</sec>
<sec id="S2.SS8">
<title>Zeta Potential and Dynamic Light Scattering (DLS)</title>
<p>The zeta potential and DLS analyses of LCNF and LNP suspensions were detected by a microscopic electrophoresis apparatus (Nano Brook 90Plus Zeta, America) and was calculated by the electrophoretic mobility. All the samples were ultrasonically treated for 20 min before analysis, and the solid concentration was around 0.05 wt.%. The measurements were conducted in triplicate for each sample, and the average data was reported.</p>
</sec>
</sec>
<sec id="S3">
<title>Results and Discussion</title>
<sec id="S3.SS1">
<title>Enzymatic Hydrolysis of CCR</title>
<p>As mentioned in the experiment part, the corncob after dilute acid hydrolysis and the followed alkaline treatment were used as the raw material in this study. As indicated in <xref ref-type="table" rid="T1">Table 1</xref>, the raw material (alkaline pretreated CCR) contains majority of cellulose with a small portion of residual xylan, lignin, and extractives, which could be a great feedstock for the preparation of glucose by enzymatic hydrolysis. <xref ref-type="fig" rid="F1">Figure 1</xref> shows the change of lignin and glucan contents in the EHRs with different enzymatic hydrolysis times. It can be clearly seen that with the increase of enzymolysis time, the content of glucan in the EHRs decreased dramatically, while the relative proportion of lignin significantly increased. The insert photos of the collected suspensions of the nanomaterial after homogenization vividly demonstrate the color change, which correlates with the lignin content. <xref ref-type="table" rid="T1">Table 1</xref> gives a detailed description of the changes of each component in the EHRs. We can easily see that the cellulose and lignin account for most of the compositions of the collected EHRs for all the samples. Also, the content of xylan and extractives did not change greatly with enzymolysis time due to the strong specificity of the enzyme. Notably, the glucan content in the EHRs is only around 3.2% after enzymatic hydrolysis for 108 h. Depending on the chemical composition of the collected EHRs after enzymatic hydrolysis, we marked the samples prepared from EHRs-48 h and EHRs-72 h as LCNFs and the sample prepared from EHRs-108 as LNPs, respectively.</p>
<fig id="F1" position="float">
<label>FIGURE 1</label>
<caption><p>Lignin and glucan content in the EHRs after different enzymatic hydrolysis times.</p></caption>
<graphic xlink:href="fbioe-09-677963-g001.tif"/>
</fig>
<table-wrap position="float" id="T1">
<label>TABLE 1</label>
<caption><p>Chemical composition of raw material and EHRs treated at different enzymatic hydrolysis times.</p></caption>
<table cellspacing="5" cellpadding="5" frame="hsides" rules="groups">
<thead>
<tr>
<td valign="top" align="left">Samples</td>
<td valign="top" align="center">Extractives</td>
<td valign="top" align="center">Glucan</td>
<td valign="top" align="center">Xylan</td>
<td valign="top" align="center">Lignin</td>
</tr>
<tr>
<td/>
<td valign="top" align="center">content (%)</td>
<td valign="top" align="center">content (%)</td>
<td valign="top" align="center">content (%)</td>
<td valign="top" align="center">content (%)</td>
</tr>
</thead>
<tbody>
<tr>
<td valign="top" align="left">Raw material</td>
<td valign="top" align="center">5.3 &#x00B1; 1.1</td>
<td valign="top" align="center">82.2 &#x00B1; 0.9</td>
<td valign="top" align="center">3.4 &#x00B1; 0.2</td>
<td valign="top" align="center">2.5 &#x00B1; 0.2</td>
</tr>
<tr>
<td valign="top" align="left">EHRs-48 h</td>
<td valign="top" align="center">8.7 &#x00B1; 0.8</td>
<td valign="top" align="center">38.8 &#x00B1; 0.6</td>
<td valign="top" align="center">2.6</td>
<td valign="top" align="center">42.1 &#x00B1; 0.6</td>
</tr>
<tr>
<td valign="top" align="left">EHRs-72 h</td>
<td valign="top" align="center">7.1 &#x00B1; 1.0</td>
<td valign="top" align="center">19.3 &#x00B1; 0.5</td>
<td valign="top" align="center">2.4 &#x00B1; 0.2</td>
<td valign="top" align="center">63 &#x00B1; 0.7</td>
</tr>
<tr>
<td valign="top" align="left">EHRs-108 h</td>
<td valign="top" align="center">5.9 &#x00B1; 0.6</td>
<td valign="top" align="center">3.2 &#x00B1; 0.9</td>
<td valign="top" align="center">2.5 &#x00B1; 0.1</td>
<td valign="top" align="center">81.5 &#x00B1; 1</td>
</tr>
</tbody>
</table></table-wrap>
</sec>
<sec id="S3.SS2">
<title>Morphologies of LCNFs and LNPs</title>
<p><xref ref-type="fig" rid="F2">Figures 2a,b</xref> show the morphology of the raw material (the alkaline-pretreated CCR) before enzymolysis. The cellulose fibers and lignin can be clearly seen, and there are some lignin particles anchored on the surface of cellulose fibers. From <xref ref-type="fig" rid="F2">Figures 2c,d</xref>, it can be observed that the LCNFs-48 h was rich in nanofibers, and there were many irregular LNPs adhering on the nanofiber surface. <xref ref-type="fig" rid="F2">Figures 2e,f</xref> display the morphology of LCNFs-72 h. According to these two images, the existence of nanofibers and LNPs on the surface of nanofibers could be seen clearly. <xref ref-type="fig" rid="F2">Figures 2g,h</xref> show the morphology of LNPs-108 h, only a small number of nanofibers can be seen, and the LNPs show an obvious aggregation state (it is speculated to be the aggregate of LNPs before freeze-drying).</p>
<fig id="F2" position="float">
<label>FIGURE 2</label>
<caption><p>SEM images of the raw material <bold>(a,b)</bold>, LCNFss-48 h <bold>(c,d)</bold>, LCNFs-72 h <bold>(e,f)</bold>, and LNPs-108 h <bold>(g,h)</bold>.</p></caption>
<graphic xlink:href="fbioe-09-677963-g002.tif"/>
</fig>
<p>As shown in <xref ref-type="fig" rid="F3">Figure 3</xref>, the morphology of LCNFs and LNPs was further examined by TEM analysis and the particle size was evaluated by DLS. From the TEM images, we can see the coexistence of nanofibers and LNPs for the samples of LCNFs-48 h and LCNFs-72 h. It should be noted that the DLS can only be used as a reference for particle distribution, not as a basis for the real particle size. As shown in <xref ref-type="fig" rid="F3">Figures 3a,b</xref>, a large number of nanofibers with a clear fiber boundary can be seen and some of the nanofibers are anchored with some LNPs. From <xref ref-type="fig" rid="F3">Figures 3d,e</xref>, most of the nanofibers are covered with LNPs, and the fiber boundary can be hardly observed. It can be seen from <xref ref-type="fig" rid="F3">Figures 3g,h</xref> that LNPs with a diameter less than 50 nm can be obtained from EHRs-108 h, but it is speculated that there is still a very small amount of cellulose nanofibers embedded among them according to the component analysis results of EHRs-108 h and <xref ref-type="fig" rid="F3">Figure 3i</xref>.</p>
<fig id="F3" position="float">
<label>FIGURE 3</label>
<caption><p>TEM images and the measured size distribution by DLS of LCNFs-48 h <bold>(a&#x2013;c)</bold>; LCNFs-72 h <bold>(d&#x2013;f)</bold>; and LNPs-108 h <bold>(g&#x2013;i)</bold>.</p></caption>
<graphic xlink:href="fbioe-09-677963-g003.tif"/>
</fig>
<p>In addition, <xref ref-type="fig" rid="F3">Figure 3</xref> indicates the measured particle size decreased with the increased lignin content in the samples. This phenomenon can be explained as follows: (1) the measured data of the sample containing nanocellulose would be larger than the actual, because of the large draw ratio. While, lignin nanoparticles can reduce the interference of draw ratio because of its near spherical shape, which lead to the measurement is closer to the actual. (2) As the lignin content increased in the samples, the possibility of attraction among the nanofibrils decreased, contributing to the separation of nanofibrils. Consequently, the measured data decreased with the increase of lignin content (<xref ref-type="bibr" rid="B14">Ferrer et al., 2012</xref>; <xref ref-type="bibr" rid="B10">Dong et al., 2020b</xref>; <xref ref-type="bibr" rid="B39">Pei et al., 2020</xref>; <xref ref-type="bibr" rid="B68">Zheng et al., 2021a</xref>).</p>
</sec>
<sec id="S3.SS3">
<title>Thermal Stability of LCNFs and LNPs</title>
<p>The thermal stability of the as-prepared LCNFs, LNPs, and raw materials was analyzed by TG analysis, and the results are shown in <xref ref-type="fig" rid="F4">Figure 4</xref>. As shown in the TG and DTG curves, all samples mainly have two stages of thermal decomposition; one is before 250&#x00B0;C, and the other is between 250 and 400&#x00B0;C. For the raw material, only one weight loss peak was observed at the temperature of 350&#x00B0;C (T<sub>max</sub>), at which the weight loss rate was around 17.5%/min. In comparison, the DTG of the LCNFs and LNPs illustrated that these samples containing the high lignin content had two weight loss peaks, and one was around 209&#x00B0;C and the other was around 360&#x00B0;C. It can also be observed from these curves that the weight loss rate at T<sub>max</sub> decreased gradually along with the increase of lignin content. According to the reported literatures, the lignin decomposed slower and in a broad range (between 160 and 900&#x00B0;C), while cellulose decomposition usually occurred in the range of 300&#x2013;400&#x00B0;C. The reason for the decrease of the weight loss rate at T<sub>max</sub> is also related to the content of cellulose in the samples. The content of cellulose in raw material was relatively high, resulting in the high degradation rate of cellulose. However, the content of cellulose in LCNFs and LNPs decreased with the prolonging of enzymatic hydrolysis time, causing the weight loss rate decreased at T<sub>max</sub>. In addition, the comparison of residual carbon produced by lignin was also consistent with the previous results (<xref ref-type="bibr" rid="B57">Wang et al., 2018</xref>).</p>
<fig id="F4" position="float">
<label>FIGURE 4</label>
<caption><p>TG <bold>(A)</bold> and DTG <bold>(B)</bold> curves of LCNFs-48 h, LCNFs-72 h, LNPs-108 h, and raw material.</p></caption>
<graphic xlink:href="fbioe-09-677963-g004.tif"/>
</fig>
</sec>
<sec id="S3.SS4">
<title>Chemical and Crystalline Structures of LCNFs and LNPs</title>
<p><xref ref-type="fig" rid="F5">Figure 5A</xref> shows the FT-IR spectra of LCNF and LNP samples. Since no chemical reaction was performed on the lignin or cellulose during the high homogenization, all the spectra were very similar to the characteristic peak of lignin. The typical aromatic ring peaks of lignin fraction at 1,596 and 1,507 cm<sup>&#x2013;1</sup> were also evident (<xref ref-type="bibr" rid="B45">Schwanninger et al., 2004</xref>). In addition, peaks at 1,125 and 1,329 cm<sup>&#x2013;1</sup> were also observed, which were assigned to the condensed guaiacyl units and syringyl units of lignin, respectively (<xref ref-type="bibr" rid="B41">Rana et al., 2009</xref>). The peak at 1,735 cm<sup>&#x2013;1</sup> (C=O vibration) was observed in EHRs-48 h and EHRs-72 h, indicating the remaining of xylan in short-time EHRs (<xref ref-type="bibr" rid="B51">Sirvio et al., 2016</xref>). The characteristic peaks of cellulose were observed at 1,163 and 897 cm<sup>&#x2013;1</sup> in LCNFs-48 h and LCNFs-72 h, which was not obvious for LNPs-108 h (<xref ref-type="bibr" rid="B45">Schwanninger et al., 2004</xref>).</p>
<fig id="F5" position="float">
<label>FIGURE 5</label>
<caption><p><bold>(A)</bold> FTIR spectra of the LCNFs-48 h, LCNFs-72 h, and LNPs-108 h. <bold>(B)</bold> X-ray diffraction patterns of raw material and the LCNFs and LNPs samples.</p></caption>
<graphic xlink:href="fbioe-09-677963-g005.tif"/>
</fig>
<p>XRD patterns of the raw material and the LCNF and LNP samples are shown in <xref ref-type="fig" rid="F5">Figure 5B</xref>. The raw material displays main characteristic diffraction peaks at 14.6&#x00B0;, 16.5&#x00B0;, 22.6&#x00B0;, and 34.6&#x00B0;, corresponding to the (1&#x2013;10), (110), (200), and (004) lattice planes, respectively, indicating that the raw materials conform to the cellulose I structure (<xref ref-type="bibr" rid="B54">Sun et al., 2015</xref>; <xref ref-type="bibr" rid="B12">Du et al., 2020</xref>). On the contrary, the XRD patterns of the LCNFs and LNPs just show a broad amorphous peak, and the highest peak was around 20.5&#x00B0;. This could be ascribed to the removal of cellulose and the amorphous nature of lignin (<xref ref-type="bibr" rid="B40">Peng et al., 2018</xref>).</p>
</sec>
<sec id="S3.SS5">
<title>Dispersion Stability</title>
<p>The dispersion stability of LCNF and LNP suspension was evaluated by the zeta potential. It is well documented that the closer the value measured by the zeta potential was to zero, the easier the dispersion was to agglomerate and settle, and the worse the relative stability is (<xref ref-type="bibr" rid="B16">Herrera et al., 2018</xref>). As shown in <xref ref-type="fig" rid="F6">Figure 6A</xref>, the zeta-potential value of the dispersion formed by LNPs-108 h was around &#x2212;52 mV, indicating the best stability. It has been demonstrated that the stability of the solution would increase with the increase of lignin content, for it would improve the fibrillation process (<xref ref-type="bibr" rid="B26">Lahtinen et al., 2014</xref>), which increases the surface charge of the material, resulting in repulsion between the fibrils thus allowing an easier separation from each other (<xref ref-type="bibr" rid="B43">Rojo et al., 2015</xref>). Moreover, as shown in <xref ref-type="fig" rid="F6">Figure 6B</xref>, all the samples exhibit very stable colloidal suspensions in aqueous media for over 1 month, indicating excellent dispersibility.</p>
<fig id="F6" position="float">
<label>FIGURE 6</label>
<caption><p>The zeta potential <bold>(A)</bold> and corresponding dispersibility in water <bold>(B)</bold> of LCNFs-48 h (i), LCNFs-72 h (ii), and LNPs-108 h (iii).</p></caption>
<graphic xlink:href="fbioe-09-677963-g006.tif"/>
</fig>
</sec>
</sec>
<sec id="S4">
<title>Proposed Process for the Full Utilization of Corncob</title>
<p>Herein, based on the results obtained in this work and our previous work, we propose the full component utilization of corncob to provide a reference for the full utilization of other similar agricultural wastes. Generally, hemicellulose is extracted firstly from corncob in the industry, which mainly involves acid treatment. On the basis of the research that we had finished (<xref ref-type="bibr" rid="B60">Xie et al., 2018b</xref>; <xref ref-type="bibr" rid="B6">Chi et al., 2019</xref>), alkali treatment was a convenient way to effectively separate alkali lignin from agricultural lignocellulosic waste and promote the downstream enzymatic hydrolysis for the production of fermentable sugars. The current study demonstrated that the EHRs could be an attractive material for the preparation of LCNFs or LNPs, which might find applications in diverse fields such as reinforcing nanofillers and Pickering emulsions. In order to show the operation involved in the proposed process more intuitively, <xref ref-type="fig" rid="F7">Figure 7</xref> is proposed to facilitate understanding. As shown in the proposed flowchart, the solid residue produced in the previous part is used to produce the desired substance in the next step. Specifically, xylose (originated from hemicellulose) was obtained by acid treatment, alkali lignin was obtained by alkali treatment, monosaccharide (derived from cellulose) was obtained by enzymatic hydrolysis, and LCNFs with different lignin contents or LNPs could be obtained by homogenization. Thus, the comprehensive utilization of the whole components of corncob can be realized.</p>
<fig id="F7" position="float">
<label>FIGURE 7</label>
<caption><p>Proposed process for the full utilization of corncob.</p></caption>
<graphic xlink:href="fbioe-09-677963-g007.tif"/>
</fig>
</sec>
<sec id="S5">
<title>Conclusion</title>
<p>In summary, high LCNFs and LNPs were successfully prepared from EHRs of corncob residues via high-pressure homogenization. During enzymatic hydrolysis process, with the increase of enzymolysis time, the lignin content increased and the cellulose content decreased resulting in the EHRs with controllable chemical compositions. It was found that the lignin content had a great influence on the morphology of the obtained nanoparticles after homogenization. The higher the lignin content in the EHRs, the smaller the size and the higher the absolute zeta potential of the obtained nanoparticles observed. This work not only promotes the development of lignocellulose-based nanomaterials but also provides a promising full utilization for the agricultural residue that simultaneously achieves the maximum use of the whole biomass.</p>
</sec>
<sec id="S6">
<title>Data Availability Statement</title>
<p>The original contributions presented in the study are included in the article/supplementary material, further inquiries can be directed to the corresponding author/s.</p>
</sec>
<sec id="S7">
<title>Author Contributions</title>
<p>RX, HD, HW, MZ, MW, CL, GY, and S-EC: investigation. CS, S-EC, and BL: supervision. RX and HD: writing&#x2014;original draft. XZ, BL, S-EC, and CS: writing&#x2014;review and editing. All authors contributed to the article and approved the submitted version.</p>
</sec>
<sec sec-type="COI-statement" id="conf1">
<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>
</body>
<back>
<fn-group>
<fn fn-type="financial-disclosure">
<p><bold>Funding.</bold> This work was supported by the National Natural Science Foundation of China (No. 31870568) and Shandong Provincial Natural Science Foundation for Distinguished Young Scholar of China (No. ZR2019JQ10) to BL, and the Technology development Program (No. S3030198) funded by the Ministry of SMEs (MSS, South Korea) to S-EC. In addition, HD acknowledges the financial support from the China Scholarship Council (No. 201708120052).</p>
</fn>
</fn-group>
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