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<front>
<journal-meta>
<journal-id journal-id-type="publisher-id">Front. Chem. Eng.</journal-id>
<journal-title>Frontiers in Chemical Engineering</journal-title>
<abbrev-journal-title abbrev-type="pubmed">Front. Chem. Eng.</abbrev-journal-title>
<issn pub-type="epub">2673-2718</issn>
<publisher>
<publisher-name>Frontiers Media S.A.</publisher-name>
</publisher>
</journal-meta>
<article-meta>
<article-id pub-id-type="publisher-id">790261</article-id>
<article-id pub-id-type="doi">10.3389/fceng.2021.790261</article-id>
<article-categories>
<subj-group subj-group-type="heading">
<subject>Chemical Engineering</subject>
<subj-group>
<subject>Original Research</subject>
</subj-group>
</subj-group>
</article-categories>
<title-group>
<article-title>Enhancing Squalene Production in <italic>Saccharomyces cerevisiae</italic> by Metabolic Engineering and Random Mutagenesis</article-title>
<alt-title alt-title-type="left-running-head">Xia et&#x20;al.</alt-title>
<alt-title alt-title-type="right-running-head">Enhancing Squalene Production in <italic>S. cerevisiae</italic>
</alt-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname>Xia</surname>
<given-names>Lu</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
</xref>
<xref ref-type="aff" rid="aff2">
<sup>2</sup>
</xref>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Lv</surname>
<given-names>Yunbin</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
</xref>
<xref ref-type="aff" rid="aff2">
<sup>2</sup>
</xref>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Liu</surname>
<given-names>Song</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
</xref>
<xref ref-type="aff" rid="aff3">
<sup>3</sup>
</xref>
<xref ref-type="aff" rid="aff4">
<sup>4</sup>
</xref>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Yu</surname>
<given-names>Shiqin</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
</xref>
</contrib>
<contrib contrib-type="author" corresp="yes">
<name>
<surname>Zeng</surname>
<given-names>Weizhu</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="corresp" rid="c001">&#x2a;</xref>
<uri xlink:href="https://loop.frontiersin.org/people/1456036/overview"/>
</contrib>
<contrib contrib-type="author" corresp="yes">
<name>
<surname>Zhou</surname>
<given-names>Jingwen</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="aff" rid="aff3">
<sup>3</sup>
</xref>
<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/234372/overview"/>
</contrib>
</contrib-group>
<aff id="aff1">
<sup>1</sup>
<institution>National Engineering Laboratory for Cereal Fermentation Technology</institution>, <institution>Jiangnan University</institution>, <addr-line>Wuxi</addr-line>, <country>China</country>
</aff>
<aff id="aff2">
<sup>2</sup>
<institution>School of Biotechnology and Key Laboratory of Industrial Biotechnology</institution>, <institution>Ministry of Education</institution>, <institution>Jiangnan University</institution>, <addr-line>Wuxi</addr-line>, <country>China</country>
</aff>
<aff id="aff3">
<sup>3</sup>
<institution>Science Center for Future Foods</institution>, <institution>Jiangnan University</institution>, <addr-line>Wuxi</addr-line>, <country>China</country>
</aff>
<aff id="aff4">
<sup>4</sup>
<institution>Jiangsu Provisional Research Center for Bioactive Product Processing Technology</institution>, <institution>Jiangnan University</institution>, <addr-line>Wuxi</addr-line>, <country>China</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/91094/overview">Zongbao K. Zhao</ext-link>, Dalian Institute of Chemical Physics (CAS), China</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/264400/overview">Hui Wu</ext-link>, East China University of Science and Technology, China</p>
<p>
<ext-link ext-link-type="uri" xlink:href="https://loop.frontiersin.org/people/234264/overview">Xiao-Jun Ji</ext-link>, Nanjing Tech University, China</p>
</fn>
<corresp id="c001">&#x2a;Correspondence: Weizhu Zeng, <email>zwzeng@jiangnan.edu.cn</email>; Jingwen Zhou, <email>zhoujw1982@jiangnan.edu.cn</email>
</corresp>
<fn fn-type="other">
<p>This article was submitted to Biochemical Engineering, a section of the journal Frontiers in Chemical Engineering</p>
</fn>
</author-notes>
<pub-date pub-type="epub">
<day>19</day>
<month>01</month>
<year>2022</year>
</pub-date>
<pub-date pub-type="collection">
<year>2021</year>
</pub-date>
<volume>3</volume>
<elocation-id>790261</elocation-id>
<history>
<date date-type="received">
<day>06</day>
<month>10</month>
<year>2021</year>
</date>
<date date-type="accepted">
<day>20</day>
<month>12</month>
<year>2021</year>
</date>
</history>
<permissions>
<copyright-statement>Copyright &#xa9; 2022 Xia, Lv, Liu, Yu, Zeng and Zhou.</copyright-statement>
<copyright-year>2022</copyright-year>
<copyright-holder>Xia, Lv, Liu, Yu, Zeng and Zhou</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>Squalene is an important polyunsaturated triterpene with wide applications in the food, cosmetics, and pharmaceutical industries. Currently, the main method for squalene production is extraction from oil-producing plants, but the scale is limited. The microbial fermentation with <italic>Saccharomyces cerevisiae</italic> still needs improvement to be economically viable. This study aimed to improve squalene production by metabolic engineering and random mutagenesis. First, the mevalonate (MVA) pathway was enhanced, by integrating <italic>tHMG1</italic> and <italic>IDI1</italic> into multi-copy site <italic>Ty2</italic>. Subsequently, the <italic>ACL</italic> gene from <italic>Yarrowia lipolytica</italic>, encoding citrate lyase was introduced and the &#x3b2;-oxidation pathway was enhanced with multiple copies of key genes. In addition, a high throughput screening strategy based on Nile red staining was established for high squalene-producer screening. After treatment with ARTP mutagenesis, a higher-producing mutant was obtained, with squalene production enhanced by 18.4%. A two-stage fermentation of this mutant in a 5&#xa0;L bioreactor produced 8.2&#xa0;g/L of squalene. These findings may facilitate the development of industrial squalene production by fermentation and potentially, other terpenoids.</p>
</abstract>
<kwd-group>
<kwd>
<italic>Saccharomyces cerevisiae</italic>
</kwd>
<kwd>promotor substitution</kwd>
<kwd>multi-copy site integration</kwd>
<kwd>high-throughput screening</kwd>
<kwd>&#x3b2;-oxidation</kwd>
</kwd-group>
<contract-sponsor id="cn001">National Key Research and Development Program of China<named-content content-type="fundref-id">10.13039/501100012166</named-content>
</contract-sponsor>
<contract-sponsor id="cn002">National Outstanding Youth Science Fund Project of National Natural Science Foundation of China<named-content content-type="fundref-id">10.13039/100014717</named-content>
</contract-sponsor>
</article-meta>
</front>
<body>
<sec id="s1">
<title>Introduction</title>
<p>Squalene is a natural product found in vegetable oils, fish oils, and human sebum. It is the main hydrocarbon component of human epidermal fats, accounting for about 10% by weight. Deep sea shark livers from the South Pacific, around Australia are the main source of squalene at present (<xref ref-type="bibr" rid="B1">Bhattacharjee et&#x20;al., 2001</xref>). Squalene also exists in plant tissues, especially the oil in plant seeds, which is also an important industrial source of squalene (<xref ref-type="bibr" rid="B7">Gutierrez et&#x20;al., 2014</xref>). Squalene is a lipophilic, acyclic triterpenoid compound formed from six isoprene units. It is the precursor of many biologically active compounds, including steroids and hopene (<xref ref-type="bibr" rid="B9">Katabami et&#x20;al., 2015</xref>). Squalene itself also has useful applications, as a moisturizing ingredient in cosmetics (<xref ref-type="bibr" rid="B13">Kohno et&#x20;al., 1995</xref>) and in pharmaceuticals (<xref ref-type="bibr" rid="B29">Reddy and Couvreur, 2009</xref>), based on its in anti-tumor (<xref ref-type="bibr" rid="B28">Rao et&#x20;al., 1998</xref>), anti-fungal (<xref ref-type="bibr" rid="B33">Smith, 2000</xref>), and cholesterol-lowering (<xref ref-type="bibr" rid="B10">Kelly, 1999</xref>) effects. Currently, the main method of squalene production is extraction from plant materials, but the scale is limited by the long growing cycle of the plants (<xref ref-type="bibr" rid="B20">Lou-Bonafonte et&#x20;al., 2018</xref>).</p>
<p>Compared with the conventional way of producing squalene from plant sources, microbial fermentation has the advantages in sustainability and greater environmental friendliness (<xref ref-type="bibr" rid="B12">Kim et&#x20;al., 2019</xref>). For example, high titer squalene was obtained from the fungus, <italic>Yarrowia lipolytica</italic> by optimizing the fermentation medium (<xref ref-type="bibr" rid="B37">Tang et&#x20;al., 2021</xref>), and 230&#xa0;mg/L of squalene was obtained from <italic>Escherichia coli</italic> in flask culture by co-expressing mevalonate pathway with heterogeneous squalene synthase (<xref ref-type="bibr" rid="B9">Katabami et&#x20;al., 2015</xref>). The cyanobacterium, <italic>Synechocystis</italic>, produced 5.1&#xa0;mg/L of squalene, after introduction of a green algal squalene synthase (<xref ref-type="bibr" rid="B26">Pattanaik et&#x20;al., 2020</xref>). However, few microorganisms possess a natural pathway for squalene synthesis. Enabling the production of squalene requires introduction of exogenous genes. Recently, the production of squalene with <italic>Saccharomyces cerevisiae</italic> has received considerable attention, because <italic>S. cerevisiae</italic> has a natural metabolic pathway for squalene synthesis, i.e.,&#x20;the mevalonate (MVA) pathway. In addition, <italic>S. cerevisiae</italic> is a well-developed eukaryotic producer microorganism and has been applied to produce many valuable plant natural products, including linalool, artemisinic acid and ginsenoside (<xref ref-type="bibr" rid="B18">Liu et&#x20;al., 2013</xref>; <xref ref-type="bibr" rid="B24">Paramasivan and Mutturi, 2017a</xref>; <xref ref-type="bibr" rid="B17">Lian et&#x20;al., 2018</xref>).</p>
<p>Many metabolic engineering strategies have been implemented to optimize squalene production by <italic>S. cerevisiae</italic>. The MVA pathway has been improved by overexpressing HMG-CoA reductase (HMGR) (<xref ref-type="bibr" rid="B42">Westfall et&#x20;al., 2012</xref>). A truncated HMG-CoA reductase enzyme was overexpressed to eliminate feedback inhibition by ergosterol, (<xref ref-type="bibr" rid="B27">Polakowski et&#x20;al., 1998</xref>). Metabolic flux optimization and NADH regeneration were achieved by co-overexpressing <italic>tHMG1</italic> with <italic>POS5</italic> (encoding NADH kinase), resulting in a 27.5-fold increase in squalene production (<xref ref-type="bibr" rid="B25">Paramasivan and Mutturi, 2017b</xref>). An engineered strain able to use ethanol as carbon source, with increased squalene synthesis, was obtained by overexpressing acetaldehyde dehydrogenase and alcohol dehydrogenase encoded by <italic>ADA</italic> and <italic>ADH2</italic>, respectively (<xref ref-type="bibr" rid="B15">Li et&#x20;al., 2020b</xref>). Squalene production was also enhanced by increasing the storage capacity for hydrophobic compounds, by overexpressing <italic>DGA1</italic>, coding for diacylglycerol acyltransferase (<xref ref-type="bibr" rid="B41">Wei et&#x20;al., 2018</xref>), and by cytoplasmic and peroxisomal engineering (<xref ref-type="bibr" rid="B19">Liu et&#x20;al., 2020</xref>).</p>
<p>Practical industrial squalene production, however, still needs further enhancement of production by <italic>S. cerevisiae</italic>. Insufficient flux through the MVA pathway is an important limiting factor and the natural biosynthesis rate of the essential precursor, acetyl-CoA is insufficient for high squalene production. In this study, several strategies were implemented to enhance the production of squalene. To reduce the conversion of squalene into downstream compounds by squalene monooxygenase, 13 promoters were tested to replace the native promoter of the squalene monooxygenase gene, <italic>ERG1</italic> (P<sub>ERG1</sub>). To enhance the MVA pathway flux, <italic>IDI1</italic> (isoprenoid diphosphate isomerase), and <italic>tHMG1</italic> (HMG-CoA reductase, HMGR) were integrated at the multi-copy site <italic>Ty2</italic> and <italic>NADH-HMG1</italic> derived from <italic>Silicibacter pomeroyi</italic> was introduced. To supply more acetyl-CoA for squalene synthesis in the cytoplasm, <italic>TGL3, CIT2</italic>, <italic>FOX1</italic>, <italic>FOX2</italic>, <italic>FOX3,</italic> related to &#x3b2;-oxidation in peroxisomes, were overexpressed, and <italic>ACL</italic> from <italic>Y. lipolytica</italic> was heterologously expressed (<xref ref-type="fig" rid="F1">Figure 1</xref>). In addition, a high-throughput screening method was established, to efficiently screen for high squalene-producing strains, resulting in a high-producing mutant, obtained by ARTP mutagenesis. The production of squalene was enhanced by 18.4%, permitting 8.2&#xa0;g/L of squalene to be produced by a two-stage fermentation strategy, in a 5-L bioreactor.</p>
</sec>
<sec sec-type="materials|methods" id="s2">
<title>Materials and Methods</title>
<sec id="s2-1">
<title>Strains, Growth Media, and Reagents</title>
<p>
<italic>S. cerevisiae</italic> C800 (CEN.PK2-1D; <italic>MAT&#x3b1;</italic>; <italic>ura3-52</italic>; <italic>his3&#x394;1</italic>; <italic>trp1-289</italic>; <italic>leu2-3,112</italic>; <italic>MAL2-8</italic>
<sup>
<italic>C</italic>
</sup>; <italic>SUC2</italic>; <italic>gal80</italic>:<italic>KanMX</italic>) (<xref ref-type="bibr" rid="B5">Gao et&#x20;al., 2020</xref>) was used for modification. <italic>Escherichia coli</italic> JM109 was used for routine transformation and plasmid storage. The composition of synthetic complete medium (SC medium) was as follows: Yeast nitrogen base (Sangon Biotech, No. B540132), 20&#xa0;g/L glucose, and 50&#xa0;mg/L amino acid. The composition of YPD medium was as follows: 20&#xa0;g/L glucose, 10&#xa0;g/L yeast extract, and 20&#xa0;g/L peptone. Standard squalene was from Sigma-Aldrich (St. Louis, MO, United&#x20;States). Yeast genome extraction kits were from Takara (Dalian, China). Other chemicals were from Titan tech. (Shanghai, China).</p>
</sec>
<sec id="s2-2">
<title>Plasmid Construction</title>
<p>Empty vectors were amplified from pY26 to construct gene expression cassettes. Promoters, terminators, and endogenous genes were all amplified from the genome of CENPK2-1D and assembled by Gibson assembly. The 20&#xa0;nt of sgRNA plasmids were designed by Benchling (<ext-link ext-link-type="uri" xlink:href="https://benchling.com/">https://benchling.com/</ext-link>) and constructed with PCR and Gibson assembly. Donor DNAs were constructed with no less than each 400&#xa0;bp upstream and downstream homologous arms. The templates were digested with <italic>Dpn</italic>I. All vectors were cloned in <italic>E.&#x20;coli</italic> JM109. DNA polymerase and DNA ligase were purchased from Vazyme (Nanjing, China). Genes were synthesized by GENEWIZ, Inc. (Suzhou, China). All constructed plasmids were sequencing by Saisofi Biotech. (Wuxi, China). Primers were from Sangon and their sequences are shown in <xref ref-type="sec" rid="s10">Supplementary Table&#x20;S1</xref>.</p>
</sec>
<sec id="s2-3">
<title>Yeast Strain Construction</title>
<p>The yeast strains used in this study are listed in <xref ref-type="sec" rid="s10">Supplementary Table S2</xref>. All plasmids and linearized DNAs were transformed into <italic>S. cerevisiae</italic> by using the Frozen-EZ-Yeast Transformation &#x2161; Kit<sup>&#x2122;</sup> (Irvine, CA, United&#x20;States). SC-X solid medium (X represents the amino acids that need to be added) was used to screen transformants. Colony PCR was used to verify positive transformants. To carry out following gene editing, SC-5-FoA plate was used to eliminate sgRNA plasmids.</p>
</sec>
<sec id="s2-4">
<title>Promoter Adjustment for <italic>ERG1</italic> Optimization</title>
<p>Thirteen promoters with different strengths were chosen to optimize <italic>ERG1</italic> expression levels. The original promoter <italic>P</italic>
<sub>
<italic>ERG1</italic>
</sub> was replaced by <italic>P</italic>
<sub>
<italic>TDH1</italic>
</sub>, <italic>P</italic>
<sub>
<italic>CCW12</italic>
</sub>, <italic>P</italic>
<sub>
<italic>TDH3p</italic>
</sub>, <italic>P</italic>
<sub>
<italic>CIT1p</italic>
</sub>, <italic>P</italic>
<sub>
<italic>PDC1p</italic>
</sub>, <italic>P</italic>
<sub>
<italic>ATP3p</italic>
</sub>, <italic>P</italic>
<sub>
<italic>RPS5</italic>
</sub>, <italic>P</italic>
<sub>
<italic>ADE6</italic>
</sub>, <italic>P</italic>
<sub>
<italic>ARO7</italic>
</sub>, <italic>P</italic>
<sub>
<italic>FAD1</italic>
</sub>, <italic>P</italic>
<sub>
<italic>TRP1</italic>
</sub>, <italic>P</italic>
<sub>
<italic>GPD2</italic>
</sub>, and <italic>P</italic>
<sub>
<italic>HXT1</italic>
</sub> (listed in strength order from high to low) (<xref ref-type="bibr" rid="B5">Gao et&#x20;al., 2020</xref>). Promoters with homologous arm list above were amplified from plasmids pUC19-x (x represents the promoter name). These PCR products along with sgRNA were then transformed into <italic>S. cerevisiae</italic>. SC-His-Leu-Trp agar plate was used to screen transformants. These agar plates were cultured at 30&#xb0;C for 2&#x2013;4&#xa0;days and then incubated in liquid medium. After 4&#xa0;days culture in shake-flasks, the best performing strain was selected as in <italic>Extraction and Quantification of Squalene</italic>.</p>
</sec>
<sec id="s2-5">
<title>Multiple Copy Sites Integration</title>
<p>Leucine degradation tags were connected to the integrated gene fragments and leucine-deficient YNB plates were used to screen high-copy strains of <italic>tHMG1</italic> and <italic>IDI1</italic>. The first colony on the plate after the transformation was recorded, and 20&#x20;fast-growing, large, and round strains were selected for plate fermentation.</p>
</sec>
<sec id="s2-6">
<title>Culture Conditions</title>
<p>Shake flask condition: At least 10 colonies were grown in 50&#xa0;ml flask containing 5&#xa0;ml SC-X liquid medium at 30&#xb0;C, 220&#xa0;rpm for 24&#xa0;h, and 2% (v/v) of the culture was reinoculated into 250&#xa0;ml flask containing 25&#xa0;ml YPD liquid medium, then cultured at 30&#xb0;C, 220&#xa0;rpm for 96&#xa0;h.</p>
<p>Fed-batch fermentation condition: Bioreactor fermentation was carried out in a 5&#xa0;L bioreactor containing 2.5&#xa0;L of the YPD medium (containing 10&#xa0;g/L CaCO<sub>3</sub>, which is used for maintaining the pH). The feeding medium was modified as described previously (<xref ref-type="bibr" rid="B14">Li et&#x20;al., 2020a</xref>), including 400&#xa0;g/L glucose, 10.24&#xa0;g/L MgSO<sub>4</sub>&#xb7;7H<sub>2</sub>O, 50&#xa0;g/L (NH<sub>4</sub>)<sub>2</sub>SO<sub>4</sub>, 18&#xa0;g/L KH<sub>2</sub>PO<sub>4</sub>, 0.56&#xa0;g/L Na<sub>2</sub>SO<sub>4</sub>, 7&#xa0;g/L K<sub>2</sub>SO<sub>4</sub>, 20&#xa0;ml/L vitamin solution, and 24&#xa0;ml/L trace metal solution. At least 10 colonies were grown in 250&#xa0;ml flask containing 25&#xa0;ml SC medium and cultured at 30&#xb0;C and 220&#xa0;rpm for 24&#xa0;h, then the seed solution was reinoculated to a 250&#xa0;ml flask containing 25&#xa0;ml SC medium for another 24&#xa0;h. The seed culture was then inoculated into a 5&#xa0;L bioreactor containing YPD medium. The temperature was controlled at 30&#xb0;C and the pH was maintained at 5.5&#x20;<italic>via</italic> automated addition of 50% ammonia. The concentration of dissolved oxygen (DO) was maintained at 50% by adjusting the stirring rate (250&#x2013;800&#xa0;rpm) up to 72&#xa0;h, then at 30% after 72&#xa0;h. The feeding medium was added at 6&#xa0;ml/h from 14&#x2013;24&#xa0;h, then 8&#xa0;ml/h from 24&#x2013;72&#xa0;h for maintaining the cell growth. In the second stage, the feeding medium was added at 5&#xa0;ml/h from 72 to 120&#xa0;h for accumulating squalene.</p>
</sec>
<sec id="s2-7">
<title>High-Throughput Screening Procedure for Mutants Based on Nile Red Staining</title>
<p>The harvested yeast cells were washed twice with PBS and diluted to a concentration of OD<sub>600</sub> &#x3d; 1.0. Then each diluted strain (1.0&#xa0;ml) was stained with 0.5, 1, and 1.5&#xa0;&#x3bc;g/ml Nile red for 30&#xa0;min at room temperature, respectively. The Nile Red stock solution was prepared at 1.0&#xa0;mg/ml in dimethyl sulfoxide (<xref ref-type="bibr" rid="B3">Choi et&#x20;al., 2018</xref>). Stained sample (200&#xa0;&#x3bc;L) was measured with a fluorescence microplate reader. The greatest fluorescence intensity was achieved at an excitation wavelength of 505&#xa0;nm and an emission wavelength of 585&#xa0;nm, so these wavelengths were used for the high-throughput screening. The wild-type strain stained with Nile Red was used as the control.</p>
</sec>
<sec id="s2-8">
<title>Extraction and Quantification of Squalene</title>
<p>After fermentation, cell suspension (1.0&#xa0;ml) was added to a tube of Lysing Matrix C and then centrifuged at 13,000 &#xd7; <italic>g</italic> for 5&#xa0;min. After removing the supernatant, beads and 1.0&#xa0;ml of acetone were added to the tube. The samples were mechanically disrupted with FastPrep-24 (MP Biomedicals, Irvine, CA, United&#x20;States) and the squalene acetone mixture was analyzed by HPLC. The HPLC system (Waters, Milford MA, United&#x20;States) was equipped with a C18 column (30&#xa0;m &#xd7; 0.25&#xa0;mm, 0.25&#xa0;&#x3bc;m film thickness), maintained at 40&#xb0;C. The squalene was separated by isocratic elution with acetonitrile (100%) of 1.6&#xa0;ml/min for 15&#xa0;min.</p>
</sec>
<sec id="s2-9">
<title>Mating Type Switch and Hybridization in Yeast</title>
<p>CRISPR/cas9-based approach was used to carry out mating-type change from &#x201c;&#x3b1;&#x201d; to &#x201c;a&#x201d; (<xref ref-type="bibr" rid="B43">Xie et&#x20;al., 2018</xref>). Transformants with switched mating type were identified by colony PCR and sequencing. To realize the construction of diploids, two different mating type strains with different amino acid labels (one with LEU, another with TRP) were mixed in 25&#xa0;ml of YPD medium in a 250&#xa0;ml flask and cultured for 60&#xa0;h at 30&#xb0;C. SC-URA-HIS plate was used to screen diploids.</p>
</sec>
</sec>
<sec sec-type="results" id="s3">
<title>Results</title>
<sec id="s3-1">
<title>Effect of ERG1 Inhibition on Cell Growth and Squalene Accumulation</title>
<p>13 promoters of different strengths were chosen to replace the native promoter of <italic>ERG1</italic> to weaken the expression of <italic>ERG1</italic>, thereby promoting the accumulation of squalene. All these promoters were chosen from a promoter library and had different translation levels. Most of the promoters with low transcription levels resulted in increased squalene accumulation. When promoter <italic>P</italic>
<sub>
<italic>ERG1</italic>
</sub> was replaced by promoter <italic>P</italic>
<sub>
<italic>HXT1</italic>
</sub>, the titer of squalene was highest from the corresponding engineered strain, reaching 826.5&#xa0;mg/L at 96&#xa0;h, 1.94-fold higher than the original strain, CP12, whereas cell growth was significantly lower (<xref ref-type="fig" rid="F2">Figure&#x20;2</xref>).</p>
<fig id="F1" position="float">
<label>FIGURE 1</label>
<caption>
<p>Engineered metabolic pathway of squalene production in <italic>S. cerevisiae</italic>. Heterologous expressed genes are highlighted in orange. Over-expressed genes are highlighted in red; downregulated genes are highlighted in green. HMG-CoA, 3-hydroxyl-3-methyl-glutaryl-CoA; IPP, isopentenyl diphosphate; DMAPP, dimethylallyl diphosphate; GPP, geranyl diphosphate; FPP, farnesyl diphosphate.</p>
</caption>
<graphic xlink:href="fceng-03-790261-g001.tif"/>
</fig>
<fig id="F2" position="float">
<label>FIGURE 2</label>
<caption>
<p>Biomass concentrations and squalene contents of constructed strains, resulting from promoter substitution, after 96&#xa0;h of culture. The promoter of <italic>ERG1</italic> (the squalene monooxygenase gene) was replaced by 13 different promoters: P<sub>TDH1</sub>, P<sub>CCW12</sub>, P<sub>TDH3</sub>, P<sub>CIT1</sub>, P<sub>PDC1</sub>, P<sub>ATP3</sub>, P<sub>RPS5</sub>, P<sub>ADE6</sub>, P<sub>ARO7</sub>, P<sub>FAD1</sub>, P<sub>TRP1</sub>, P<sub>GPD2</sub>, and P<sub>HXT1</sub>. Error bars show SD values.</p>
</caption>
<graphic xlink:href="fceng-03-790261-g002.tif"/>
</fig>
</sec>
<sec id="s3-2">
<title>Effect of tHMG1 and IDI1 Copy Number on Squalene Accumulation</title>
<p>To investigate the influence of <italic>tHMG1</italic> and <italic>IDI1</italic> copy number on the enhancement of the MVA pathway, five strains were established with different copy numbers, namely wild-type strains C800, CP02 (1&#x20;<italic>tHMG1</italic>), CP05 (1&#x20;<italic>tHMG1</italic> and 1&#x20;<italic>IDI1</italic>), CP08 (2&#x20;<italic>tHMG1</italic> and 2&#x20;<italic>IDI1</italic>), and CP12 (3&#x20;<italic>tHMG1</italic> and 3&#x20;<italic>IDI1</italic>), respectively. The accumulation of squalene was positively correlated with the copy number of <italic>tHMG1</italic> and <italic>IDI1</italic> (<xref ref-type="fig" rid="F3">Figure&#x20;3A</xref>). Therefore, the multi-copy site <italic>Ty2</italic> was selected for integration of <italic>tHMG1</italic> and <italic>IDI1</italic> to increase their copy numbers. After culturing in 24-well plates for 96&#xa0;h, the production of squalene was enhanced by all these engineered strains, integrating different copy numbers, of which the highest-yielding strain (SQ10) could accumulate 781.2&#xa0;mg/L of squalene (<xref ref-type="fig" rid="F3">Figure&#x20;3B</xref>). The obtained engineered strain SQ10 could accumulate 703.7&#xa0;mg/L of squalene for 96&#xa0;h in shaking flasks, which was superior to CP12. To further improve HMGR activity without breaking of balance of redox status, an HMG-CoA reductase NADH-HMGR with high specificity for NADH from <italic>S. pomeroyi</italic> was introduced into SQ10 to produce strain SQ11. The titer of squalene with SQ11 was further increased, reaching 787.3&#xa0;mg/L (<xref ref-type="fig" rid="F3">Figure&#x20;3C</xref>).</p>
<fig id="F3" position="float">
<label>FIGURE 3</label>
<caption>
<p>The influence of copy numbers of tHMG1/IDI1. <bold>(A)</bold> Growth and squalene accumulation of strains with different copy numbers of <italic>tHMG1</italic> and <italic>IDI1</italic> in shake-flasks at 96&#xa0;h. <bold>(B)</bold> Growth and squalene accumulation of strains of integrating <italic>tHMG1</italic> and <italic>IDI1</italic> in multiple copy site <italic>Ty2</italic> in 24-well plates at 96&#xa0;h. <bold>(C)</bold> Growth and squalene accumulation of different strains in shake flasks at 96&#xa0;h. Error bars show SD values.</p>
</caption>
<graphic xlink:href="fceng-03-790261-g003.tif"/>
</fig>
</sec>
<sec id="s3-3">
<title>Strengthening &#x3b2;-oxidation to Enhance Squalene Production</title>
<p>Based on the above findings, a strain (SQ13) was obtained, by replacing the original promoter with <italic>P</italic>
<sub>
<italic>HXT1</italic>
</sub> and integrating <italic>tHMG1</italic> and <italic>IDI1</italic> at the <italic>Ty2</italic> site. To increase the accumulation of acetyl-CoA in the cytoplasm, citrate lyase (encoded by <italic>ACL</italic>) from <italic>Yarrowia lipolytica</italic> was introduced. In addition, <italic>TGL3</italic>, <italic>CIT2</italic>, <italic>FOX1</italic>, <italic>FOX2</italic>, <italic>FOX3</italic>, related to &#x3b2;-oxidation in peroxisomes, were also overexpressed in different combinations. The squalene production of strain SQB1 that heterologous expressed <italic>ACL</italic> was increased by 257&#xa0;mg/L compared with the original strain SQ13 (<xref ref-type="fig" rid="F4">Figure&#x20;4</xref>). Compared with the heterologous expression of <italic>ACL</italic> alone, the expression of other &#x3b2;-oxidation-related genes had no obvious effect on squalene accumulation, while overexpression of <italic>FOX1</italic> could slightly improve the squalene production to 293&#xa0;mg/L (<xref ref-type="fig" rid="F4">Figure&#x20;4</xref>). To enhance the resistance of strains to environmental and metabolic stress, another strain SQ6 (mating type a, <italic>P</italic>
<sub>
<italic>ERG1</italic>
</sub> was replaced by promoter <italic>P</italic>
<sub>
<italic>HXT1</italic>
</sub>) had been constructed. Two haploid strains SQB4 and SQ6, with different mating types, were hybridized, resulting in a diploid strain SQ9. There was a marked improvement in cell growth of SQ9, which was increased by 15.5% compared with that of&#x20;SQB4.</p>
<fig id="F4" position="float">
<label>FIGURE 4</label>
<caption>
<p>Biomass concentrations and squalene contents of engineered strains after 96&#xa0;h of culture. SQB1-SQB12 were modified from SQ13. &#x2b; signs signify genes are strengthened. Error bars show SD values.</p>
</caption>
<graphic xlink:href="fceng-03-790261-g004.tif"/>
</fig>
</sec>
<sec id="s3-4">
<title>Enhancing Squalene Production by Mutagenesis and High-Throughput Screening</title>
<p>To establish a method for rapid determination of the intracellular squalene concentration, samples of 3 different strains fermented for 72&#xa0;h were coped with 3 different concentrations of Nile red (0.5, 1.0, and 1.5&#xa0;&#x3bc;g/ml) to stain the cells. The fluorescence intensity of the stained cells was determined and correlated with the content of squalene determined by HPLC. A linear relationship between the squalene content and the fluorescence intensity was obtained (<xref ref-type="fig" rid="F5">Figure&#x20;5</xref>). The best linear relationship was obtained at a Nile Red concentration of 1.0&#xa0;&#x3bc;g/ml. The relationship between squalene content and the fluorescence intensity could be expressed as <italic>Y</italic>&#x20;&#x3d; 1057.8<italic>X</italic>-9945.5 (<italic>R</italic>
<sup>
<italic>2</italic>
</sup> &#x3d; 0.9313), indicating that the staining method was suitable for the high-throughput screening procedure. The fatality curve showed that the fatality rate was 80.46% after 75&#xa0;s of ARTP treatment. The strain SQ9 was treated with three rounds of ARTP mutagenesis and high-throughput screening (<xref ref-type="fig" rid="F6">Figure&#x20;6</xref>) identified a mutant strain which accumulated 1470.9&#xa0;mg/L of squalene, 18.4% higher than the initial strain. The mutant strain was tested for practical squalene production in a 5&#xa0;L bioreactor, with a two-stage, high density cell fermentation, producing 8.2&#xa0;g/L of squalene, and a final OD<sub>600</sub> of 156.3 (<xref ref-type="fig" rid="F7">Figure&#x20;7</xref>).</p>
<fig id="F5" position="float">
<label>FIGURE 5</label>
<caption>
<p>Establishment of the high-throughput intracellular squalene assay. Relationship between fluorescence intensity and squalene production at different Nile Red cell-staining concentrations: <bold>(A)</bold> 0.5&#xa0;&#x3bc;g/ml; <bold>(B)</bold> 1&#xa0;&#x3bc;g/ml; <bold>(C)</bold> 1.5&#xa0;&#x3bc;g/ml. Error bars show SD values.</p>
</caption>
<graphic xlink:href="fceng-03-790261-g005.tif"/>
</fig>
<fig id="F6" position="float">
<label>FIGURE 6</label>
<caption>
<p>Cell populations under different fluorescence intensities of the flow cytometer. <bold>(A)</bold>: Cell grouping under Nile Red staining of non-squalene-producing <italic>S. cerevisiae</italic>. <bold>(B)</bold>: Cell grouping under Nile Red staining of squalene-producing <italic>S. cerevisiae</italic>. &#x201c;Sort&#x201d; represents the distribution of cells that we need to screen&#x20;out.</p>
</caption>
<graphic xlink:href="fceng-03-790261-g006.tif"/>
</fig>
<fig id="F7" position="float">
<label>FIGURE 7</label>
<caption>
<p>Time course of squalene accumulation in a 5-L bioreactor. Time courses showing changes in squalene production and cell growth by strain SQ9 in a 5&#xa0;L bioreactor. Error bars indicate SD values.</p>
</caption>
<graphic xlink:href="fceng-03-790261-g007.tif"/>
</fig>
</sec>
</sec>
<sec sec-type="discussion" id="s4">
<title>Discussion</title>
<p>
<italic>S. cerevisiae</italic> is one of the most common microbial hosts for synthetic biology and metabolic engineering. It is a promising platform to produce squalene compared with natural resource extraction, or chemical synthesis (<xref ref-type="bibr" rid="B27">Polakowski et&#x20;al., 1998</xref>; <xref ref-type="bibr" rid="B38">Thompson et&#x20;al., 2014</xref>). In this study, the highest accumulation of squalene was achieved after the native promoter <italic>P</italic>
<sub>
<italic>ERG1</italic>
</sub> was replaced by <italic>P</italic>
<sub>
<italic>HXT1</italic>
</sub>. By randomly integrating <italic>tHMG1</italic> and <italic>IDI1</italic> into the multi-copy site <italic>Ty2</italic>, squalene production of 703.7&#xa0;mg/L was obtained. Squalene production was further increased by 257&#xa0;mg/L by increasing &#x3b2;-oxidation capacity. A high-throughput screening method was then established for screening high-efficiency squalene producers. After treatment by ARTP mutagenesis, a higher producing mutant strain was obtained, which accumulated 1470.9&#xa0;mg/L squalene in a shake flask and 8.2&#xa0;g/L in a 5&#xa0;L fed-batch fermentation.</p>
<p>Weaker promoters of the squalene monooxygenase gene, <italic>ERG1</italic>, were tested to lower its expression level and minimize the conversion of squalene into downstream compounds. None of the weaker promoters resulted in significant squalene accumulation except <italic>P</italic>
<sub>
<italic>HXT1</italic>
</sub>, which increased the squalene yield by 94.3% compared with the original strain. This indicated that&#x20;the inducible promoter <italic>P</italic>
<sub>
<italic>HXT1</italic>
</sub> was important for regulation of key genes related to yeast growth. <italic>P</italic>
<sub>
<italic>HXT1</italic>
</sub> can also respond to the concentration of glucose (<xref ref-type="bibr" rid="B23">Ozcan and Johnston, 1995</xref>). During the growth stage of yeast, when the glucose concentration in the medium is relatively high, <italic>ERG1</italic> is normally expressed, and the synthesis of sterols is sufficient to&#x20;promote the rapid growth of the yeast cells. When the glucose in the culture medium is exhausted, expression of <italic>ERG1</italic> is inhibited, thereby increasing the accumulation of squalene in the yeast cells (<xref ref-type="bibr" rid="B44">Zhao et&#x20;al., 2017</xref>). Many reports have highlighted the importance of <italic>tHMG1</italic> and <italic>IDI1</italic> in increasing mevalonate (MVA) pathway flux and promoting squalene production (<xref ref-type="bibr" rid="B18">Liu et&#x20;al., 2013</xref>). In this study, making various combinations of different copy numbers of <italic>tHMG1</italic> and <italic>IDI1</italic> showed that the production of squalene was proportional to&#x20;their copy numbers. The integration of pathway genes in one&#x20;or&#x20;several copies, especially those encoding rate-limiting steps,&#x20;is&#x20;usual insufficient to maintain high metabolic fluxes (<xref ref-type="bibr" rid="B21">Maury&#x20;et&#x20;al., 2016</xref>). In addition, the expression of a multi-copy plasmid is unstable. The <italic>Ty2</italic> element, with 34 insertions in the <italic>S. cerevisiae</italic> genome (<xref ref-type="bibr" rid="B11">Kim et&#x20;al., 1998</xref>), was selected as the integration site for <italic>tHMG1</italic> and&#x20;<italic>IDI1</italic>.</p>
<p>Acetyl-CoA is a crucial precursor metabolite for terpene biosynthesis (<xref ref-type="bibr" rid="B8">Hellgren et&#x20;al., 2020</xref>). In <italic>S. cerevisiae</italic>, acetyl-CoA metabolism is complex, because of its compartmentalized biosynthesis pathway and its involvement in various key cellular processes, including the tricarboxylic acid (TCA) cycle, biosynthesis of sterols, fatty acids, and polyketides (<xref ref-type="bibr" rid="B22">Nielsen, 2014</xref>). Strategies have been applied to enhance the supply of acetyl-CoA to the MVA pathway, such as introducing heterologous acetyl-CoA synthetase to increase acetyl-CoA (<xref ref-type="bibr" rid="B31">Shiba et&#x20;al., 2007</xref>), removing bypass genes to eliminate competitive products (<xref ref-type="bibr" rid="B16">Lian et&#x20;al., 2014</xref>), and establishing an efficient acetyl-CoA-producing bypass (<xref ref-type="bibr" rid="B31">Shiba et&#x20;al., 2007</xref>; <xref ref-type="bibr" rid="B15">Li et&#x20;al., 2020b</xref>). In addition, acetyl-CoA is a metabolite of fatty acid oxidation. In the peroxisome, it can be converted into citric acid and transported out of the peroxisome, through the glyoxylic acid cycle. The acetyl-CoA is converted to citric acid by citrate synthase (encoded by <italic>CIT2</italic>) and the resulting citric acid can be transported out of the peroxisomes to the cytoplasm (<xref ref-type="bibr" rid="B40">van Rossum et&#x20;al., 2016</xref>). A heterologous citrate lyase, encoded by <italic>ACL1</italic> and&#x20;<italic>ACL2</italic>, was introduced, which converted citrate to acetyl-CoA, can promote the supply of acetyl-CoA to the cytoplasm. Genes involved in &#x3b2;-oxidation were also overexpressed. The citric&#x20;acid generated by &#x3b2;-oxidation could be catalyzed to acetyl-CoA by the heterologous citrate lyase and further promoted squalene production. Furthermore, to enhance the growth of engineered strains, a diploid yeast was hybridized with two haploid, stress tolerant (e.g., to ethanol and starvation) yeasts, SQB4, and SQ6 (<xref ref-type="bibr" rid="B39">Tomova et&#x20;al., 2019</xref>) (<xref ref-type="sec" rid="s10">Supplementary Table&#x20;S2</xref>).</p>
<p>The content of squalene in microorganisms is usually detected by high-performance liquid chromatography, which complicated and slow, because the cells must be disrupted, and extracted with organic solvent. It is, therefore, not suitable for high-throughput screening of high squalene-yield yeasts. Intracellular squalene is present as lipid droplets, which can be detected by Nile red staining (<xref ref-type="bibr" rid="B6">Greenspan et&#x20;al., 1985</xref>; <xref ref-type="bibr" rid="B2">Chen et&#x20;al., 2009</xref>; <xref ref-type="bibr" rid="B32">Sitepu et&#x20;al., 2012</xref>; <xref ref-type="bibr" rid="B30">Rostron and Lawrence, 2017</xref>; <xref ref-type="bibr" rid="B3">Choi et&#x20;al., 2018</xref>). After Nile red staining, the accumulation of squalene and lipid droplets in <italic>S. cerevisiae</italic> can be observed with a fluorescence microscope (<xref ref-type="bibr" rid="B36">Ta et&#x20;al., 2012</xref>). This facilitated the establishment of a high-throughput screen, based on fluorescent Nile red staining of <italic>S. cerevisiae</italic>. The quantitative correlation between fluorescence intensity and squalene concentration from Nile red staining was analyzed with numerous cells of different squalene productivity. A high-throughput screening method was established, with a good linear relationship between squalene production and fluorescence intensity, by optimizing the concentration of Nile Red. Combined with the ARTP mutagenesis strategy and flow cytometry sorting technology (<xref ref-type="fig" rid="F6">Figure&#x20;6</xref>), the screening efficiency was enhanced and a mutant strain was obtained, with squalene production increased by&#x20;18.4%.</p>
<p>Compared with previous reports, it appeared that the use of multi-copy site integration was an efficient way to increase MVA pathway flux and squalene production. However, the target sites for genomic integration have not been identified and there is a risk of DNA loss (<xref ref-type="bibr" rid="B21">Maury et&#x20;al., 2016</xref>). A more accurate screening approach should be used after multi-copy site integration, such as whole genome sequencing. Furthermore, to promote the utilization of citric acid from &#x3b2;-oxidation, the glyoxylic acid cycle, which may be a competitive pathway, should be regulated to enhance squalene production. Except strengthening the supply of acetyl-CoA, overproduction of squalene can also be achieved by introducing a partial MVA pathway from acetyl-CoA to mevalonate in mitochondria (<xref ref-type="bibr" rid="B45">Zhu et&#x20;al., 2021</xref>). It provides a new insight into the production of squalene and other terpenes in yeasts. Squalene distribution in yeast cells was visualized by Nile Red staining in this study, dense and large lipid droplets, spread over the whole cell were visualized by laser scanning confocal microscopy. Transporting squalene to the extracellular space appeared to be the main impediment to increased squalene accumulation. However, there are few reports on the transport of terpenoids in microorganisms, particularly hydrophobic terpenoids like squalene. The proteins most reported as being related to the transport of terpenoids are mainly ABC transporters, like SpTUR2 (<italic>Spirodela polyrrhiza</italic>) for the diterpene sclareol (<xref ref-type="bibr" rid="B34">Stukkens et&#x20;al., 2005</xref>) and Snq2p for &#x3b2;-carotene (<xref ref-type="bibr" rid="B35">Sun et&#x20;al., 2020</xref>). These findings indicated that the production of squalene could be further increased by discovering potential new transporters. Metabolic engineering has great potential to be applied to various cell factories to enhance the secretion of squalene.</p>
</sec>
</body>
<back>
<sec id="s5">
<title>Data Availability Statement</title>
<p>The original contributions presented in the study are included in the article/<xref ref-type="sec" rid="s10">Supplementary Material</xref>, further inquiries can be directed to the corresponding authors.</p>
</sec>
<sec id="s6">
<title>Author Contributions</title>
<p>LX, WZ, and JZ designed the study and wrote the article. LX, WZ, and JZ critically revised the article. LX, YL, SL, SY, WZ, and JZ performed the experiments and analyzed the results. WZ and JZ designed and supervised the project. All authors discussed the results and commented on the article.</p>
</sec>
<sec id="s7">
<title>Funding</title>
<p>This work was supported by the National Key Research and Development Program of China (2019YFA0905300), the National Outstanding Youth Foundation (21822806), and the Qingdao Biomanufacturing Industry Joint Fund of Think Tank (QDSWZK202110).</p>
</sec>
<sec sec-type="COI-statement" id="s8">
<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="s9">
<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>
<sec id="s10">
<title>Supplementary Material</title>
<p>The Supplementary Material for this article can be found online at: <ext-link ext-link-type="uri" xlink:href="https://www.frontiersin.org/articles/10.3389/fceng.2021.790261/full#supplementary-material">https://www.frontiersin.org/articles/10.3389/fceng.2021.790261/full&#x23;supplementary-material</ext-link>
</p>
<supplementary-material>
<label>Supplementary Table&#x20;1</label>
<caption>
<p>Primers used in this&#x20;study.</p>
</caption>
</supplementary-material>
<supplementary-material>
<label>Supplementary Table&#x20;2</label>
<caption>
<p>Plasmids and strains used in this&#x20;study.</p>
</caption>
</supplementary-material>
<supplementary-material xlink:href="DataSheet1.docx" id="SM1" mimetype="application/docx" xmlns:xlink="http://www.w3.org/1999/xlink"/>
</sec>
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