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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="publisher-id">1650600</article-id>
<article-id pub-id-type="doi">10.3389/fbioe.2025.1650600</article-id>
<article-categories>
<subj-group subj-group-type="heading">
<subject>Bioengineering and Biotechnology</subject>
<subj-group>
<subject>Review</subject>
</subj-group>
</subj-group>
</article-categories>
<title-group>
<article-title>Regeneration of cofactor NAD(P)<sup>&#x2b;</sup> with NAD(P)H oxidase for the production of value-added chemicals</article-title>
<alt-title alt-title-type="left-running-head">Zhou et al.</alt-title>
<alt-title alt-title-type="right-running-head">
<ext-link ext-link-type="uri" xlink:href="https://doi.org/10.3389/fbioe.2025.1650600">10.3389/fbioe.2025.1650600</ext-link>
</alt-title>
</title-group>
<contrib-group>
<contrib contrib-type="author" equal-contrib="yes">
<name>
<surname>Zhou</surname>
<given-names>Li-Jian</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
</xref>
<xref ref-type="author-notes" rid="fn001">
<sup>&#x2020;</sup>
</xref>
<role content-type="https://credit.niso.org/contributor-roles/Writing - review &#x26; editing/"/>
<role content-type="https://credit.niso.org/contributor-roles/conceptualization/"/>
</contrib>
<contrib contrib-type="author" equal-contrib="yes">
<name>
<surname>Long</surname>
<given-names>Shuai-Xi</given-names>
</name>
<xref ref-type="aff" rid="aff2">
<sup>2</sup>
</xref>
<xref ref-type="author-notes" rid="fn001">
<sup>&#x2020;</sup>
</xref>
<role content-type="https://credit.niso.org/contributor-roles/writing-original-draft/"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Huan</surname>
<given-names>Tong</given-names>
</name>
<xref ref-type="aff" rid="aff3">
<sup>3</sup>
</xref>
<uri xlink:href="https://loop.frontiersin.org/people/3183461/overview"/>
<role content-type="https://credit.niso.org/contributor-roles/writing-original-draft/"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Wu</surname>
<given-names>Yue</given-names>
</name>
<xref ref-type="aff" rid="aff3">
<sup>3</sup>
</xref>
<uri xlink:href="https://loop.frontiersin.org/people/3183918/overview"/>
<role content-type="https://credit.niso.org/contributor-roles/writing-original-draft/"/>
</contrib>
<contrib contrib-type="author" corresp="yes">
<name>
<surname>Zhang</surname>
<given-names>Ye-Wang</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/61244/overview"/>
<role content-type="https://credit.niso.org/contributor-roles/Writing - review &#x26; editing/"/>
<role content-type="https://credit.niso.org/contributor-roles/conceptualization/"/>
<role content-type="https://credit.niso.org/contributor-roles/supervision/"/>
</contrib>
</contrib-group>
<aff id="aff1">
<sup>1</sup>
<institution>The People&#x2019;s Hospital of Danyang, Affiliated Danyang Hospital of Nantong University</institution>, <addr-line>Zhenjiang</addr-line>, <country>China</country>
</aff>
<aff id="aff2">
<sup>2</sup>
<institution>School of Medicine, Nantong University</institution>, <addr-line>Nantong</addr-line>, <country>China</country>
</aff>
<aff id="aff3">
<sup>3</sup>
<institution>School of Pharmacy, Jiangsu University</institution>, <addr-line>Zhenjiang</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/827486/overview">Jung-Kul Lee</ext-link>, Konkuk University, Republic of Korea</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/2092176/overview">Shulai Liu</ext-link>, Zhejiang University of Technology, China</p>
<p>
<ext-link ext-link-type="uri" xlink:href="https://loop.frontiersin.org/people/2414281/overview">Jeya Marimuthu</ext-link>, National Institute of Ocean Technology, India</p>
<p>
<ext-link ext-link-type="uri" xlink:href="https://loop.frontiersin.org/people/2733216/overview">Mugesh Sankaranarayanan</ext-link>, Vel Tech Rangarajan Dr.Sagunthala R&#x26;D Institute of Science and Technology, India</p>
<p>
<ext-link ext-link-type="uri" xlink:href="https://loop.frontiersin.org/people/3109314/overview">Hao Dong</ext-link>, Ocean University of China, China</p>
</fn>
<corresp id="c001">&#x2a;Correspondence: Ye-Wang Zhang, <email>zhangyewang@ujs.edu.cn</email>
</corresp>
<fn fn-type="equal" id="fn001">
<label>
<sup>&#x2020;</sup>
</label>
<p>These authors have contributed equally to this work</p>
</fn>
</author-notes>
<pub-date pub-type="epub">
<day>01</day>
<month>09</month>
<year>2025</year>
</pub-date>
<pub-date pub-type="collection">
<year>2025</year>
</pub-date>
<volume>13</volume>
<elocation-id>1650600</elocation-id>
<history>
<date date-type="received">
<day>20</day>
<month>06</month>
<year>2025</year>
</date>
<date date-type="accepted">
<day>21</day>
<month>08</month>
<year>2025</year>
</date>
</history>
<permissions>
<copyright-statement>Copyright &#xa9; 2025 Zhou, Long, Huan, Wu and Zhang.</copyright-statement>
<copyright-year>2025</copyright-year>
<copyright-holder>Zhou, Long, Huan, Wu and Zhang</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>Nicotinamide adenine dinucleotide (phosphate) oxidases are the enzymes that catalyze the oxidation of NAD(P)H to produce NAD(P)<sup>&#x2b;</sup>, which is the cofactor of many dehydrogenases. To reduce costs, cofactor regeneration of NAD(P)&#x2b; is essential for both enzymatic and whole-cell biotransformations. In the present review, the enzymatic or microbial production of rare sugars like L-tagatose, L-xylulose, L-gulose, and L-sorbose with cofactor regeneration was summarized. And the cofactor regeneration in some value-added chemicals, including acetoin, 1,3-dihydroacetone, vanillic acid, chlorolactone, acetophenone, and kinetic resolution of racemic phenylethanol by employing NADH/NADPH oxidase was also reviewed. The engineering of these enzymes by modifying the enzyme surface, reshaping the catalytic pocket, and mutating the substrate-binding domain of NADH oxidase to improve the catalytic performance for potential industrial applications was discussed in the future outlook.</p>
</abstract>
<kwd-group>
<kwd>NADH oxidase</kwd>
<kwd>cofactor regeneration</kwd>
<kwd>biocatalysis</kwd>
<kwd>cascade enzymatic reactions</kwd>
<kwd>pharmaceuticals</kwd>
</kwd-group>
<contract-sponsor id="cn001">Jiangsu Commission of Health<named-content content-type="fundref-id">10.13039/100017962</named-content>
</contract-sponsor>
<counts>
<page-count count="10"/>
</counts>
</article-meta>
</front>
<body>
<sec id="s1">
<title>1 Introduction</title>
<p>Nicotinamide adenine dinucleotide (NAD), as the most important coenzyme, could help other NAD-dependent enzymes to catalyze chemical reactions by switching between the reduced and oxidized form (NAD<sup>&#x2b;</sup>/NADH). In eukaryotic cells, the energy could be produced using NADH in cellular metabolism. The process from NADH to NAD<sup>&#x2b;</sup> is generally catalyzed by NADH oxidase (NOX) and produces reactive oxygen species (ROS) in eukaryotic cells, and another main source of ROS <italic>in vivo</italic> is NADPH oxidase. These two categories of enzymes catalyze the NAD(P)H to produce NAD(P)<sup>&#x2b;</sup> for coupling with the dehydrogenases catalyzed oxidoreduction reactions for the production of enantiopure chemicals or pharmaceuticals. The increasing attention on these enzymes is due to their potential capacity to regenerate the expensive cofactor NAD(P)<sup>&#x2b;</sup> in industrial enzymatic preparation of value-added products with NAD(P)<sup>&#x2b;</sup>-dependent dehydrogenases.</p>
<p>Most NOXs have a highly conserved catalytic residue -cysteine, located in the active site. They catalyze the oxidation reactions of NADH to NAD<sup>&#x2b;</sup> coupled with the four-electron transfer mode by consumption of O<sub>2</sub> or the two-electron transfer mode by reducing H<sub>2</sub>O<sub>2</sub> (<xref ref-type="bibr" rid="B14">Li et al., 2018</xref>). Compared with the H<sub>2</sub>O<sub>2</sub>-forming NOX, the H<sub>2</sub>O-forming NOX is more interesting because of its good compatibility in enzymatic reactions in aqueous solution. Similarly, the oxidized NADP<sup>&#x2b;</sup> could also be recycled by NADPH oxidase and follows a similar reaction mechanism.</p>
<p>Oxidoreductase is the largest class of enzymes, and NAD(P)<sup>&#x2b;</sup> is the most common cofactor of the oxidoreductase. Now, the chemical synthesis route in chemical, paper, cosmetic, and other industries is undergoing a change to biocatalytic, especially enzymatic methods. In this review, we summarized the potential industrial production of value-added chemicals with cofactor regeneration of NAD<sup>&#x2b;</sup>/NADP<sup>&#x2b;</sup>. In the enzymatic reactions by using coupled or combined enzymes, the strategy of protein engineering for remodeling the enzyme is also included to improve the catalytic efficiency.</p>
</sec>
<sec id="s2">
<title>2 Enzymatic production of rare sugars with dehydrogenase and NOX</title>
<p>Rare sugars are highly valued mono- or disaccharides with beneficial health effects. However, most synthetic chemical routes are both limited and economically unfeasible due to the expensive raw materials, harsh reaction conditions, and severe environmental pollution. Enzymatic transformation has become a powerful tool in the field. Many NAD-dependent enzymes are hydrogenases, which oxidize alcohols or sugars (<xref ref-type="bibr" rid="B31">Stolarczyk et al., 2020</xref>) to produce rare sugars. The cofactors are bound weakly to the enzyme and could be easily released from the protein. Thus, the regeneration of the cofactors is essential for the combined or cascade enzymatic reactions, which will significantly lower the cost. In the past decade, several L-form rare sugars have been successfully synthesized with dehydrogenase coupled with NAD(P)H oxidases as shown in <xref ref-type="table" rid="T1">Table 1</xref>.</p>
<table-wrap id="T1" position="float">
<label>TABLE 1</label>
<caption>
<p>Enzymatic synthesis of the rare sugars and their applications.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th align="left">Rare sugar</th>
<th align="left">Enzymes</th>
<th align="left">Production yield</th>
<th align="left">Applications</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="left">L-tagatose</td>
<td align="left">GatDH and NOX</td>
<td align="left">Up to 90%</td>
<td align="left">Food additive, low-calorie sweetener</td>
</tr>
<tr>
<td align="left">L-xylulose</td>
<td align="left">ArDH and NOX</td>
<td align="left">Up to 93%</td>
<td align="left">Pharmaceuticals</td>
</tr>
<tr>
<td align="left">L-gulose</td>
<td align="left">MDH and NOX</td>
<td align="left">5.5&#xa0;g/L</td>
<td align="left">Anticancer drug precursor</td>
</tr>
<tr>
<td align="left">L-sorbose</td>
<td align="left">SlDH and NOX</td>
<td align="left">Up to 92%</td>
<td align="left">Pharmaceutical intermediate</td>
</tr>
</tbody>
</table>
</table-wrap>
<sec id="s2-1">
<title>2.1 Production of L-tagatose with galactitol dehydrogenase</title>
<p>As a rare sugar, L-tagatose has great potential applications in the therapy of diabetes, food additives, and cosmetics because of its low-calorie value (<xref ref-type="bibr" rid="B22">Mahmood et al., 2021</xref>). Considering the increasing diabetes and obesity, low- or zero-caloric sweeteners are gaining attention in the food industry (<xref ref-type="bibr" rid="B28">Ravikumar et al., 2022</xref>; <xref ref-type="bibr" rid="B27">Ravikumar et al., 2021</xref>). The biological production method has drawn obvious achievements for L-tagatose production (<xref ref-type="bibr" rid="B21">Lu et al., 2024</xref>; <xref ref-type="bibr" rid="B41">Yuan et al., 2021</xref>). However, chemical synthesis of L-tagatose leads to low yield and by-products (<xref ref-type="bibr" rid="B33">Tang et al., 2022</xref>). Su et al. used galactitol dehydrogenase (<italic>Gat</italic>DH) and H<sub>2</sub>O-forming NOX (<italic>Sm</italic>Nox) for efficient enzymatic synthesis of L-tagatose (<xref ref-type="bibr" rid="B32">Su et al., 2021</xref>). The yield of 90% after 12&#xa0;h reaction was obtained when the substrate concentration of 100&#xa0;mM and 3&#xa0;mM NAD<sup>&#x2b;</sup> was supplied. There was no by-product formation and a high yield of L-tagatose with low costs using this enzymatic route (<xref ref-type="fig" rid="F1">Figure 1</xref>). Later, they prepared the combined cross-linked enzyme aggregates containing <italic>Gat</italic>DH and <italic>Sm</italic>Nox for the synthesis of L-tagatose (<xref ref-type="bibr" rid="B17">Li et al., 2022b</xref>). The combined cross-linked enzyme aggregates exhibited high thermal stability and industrial potential for the L-tagatose preparation.</p>
<fig id="F1" position="float">
<label>FIGURE 1</label>
<caption>
<p>Enzymatic production of L-tagatose from D-galactitol with NOX and GatDH.</p>
</caption>
<graphic xlink:href="fbioe-13-1650600-g001.tif">
<alt-text content-type="machine-generated">Chemical reaction scheme showing the conversion of D-Galactitol to L-Tagatose. D-Galactitol has a blue hydroxyl group and L-Tagatose features a red carbonyl group. The reaction involves GatDH enzyme and coenzymes NAD&#x207A; converting to NADH, with water and oxygen involved via NOX.</alt-text>
</graphic>
</fig>
</sec>
<sec id="s2-2">
<title>2.2 Enzymatic production of L-xylulose with arabinitol dehydrogenase</title>
<p>L-Xylulose, as another important rare sugar, is usually used as an anticancer and cardioprotective agent or as a precursor for the preparation of antiviral drugs. The chemical synthesis of the L-xylulose method has disadvantages of low yield, environmental pollution, and low purity because it is difficult to separate from other isomers. The substrate for the biological preparation of L-xylulose could be L-arabinitol or xylitol.</p>
<p>Gao et al. reported the biotransformation of L-arabinitol to L-xylulose with immobilized whole <italic>Escherichia coli</italic> cells expressed L-arabinitol dehydrogenase and NOX (<xref ref-type="bibr" rid="B5">Gao et al., 2015</xref>). By coupling two enzymes in the cells, a molar conversion of 96% from L-arabinitol to L-xylulose was achieved. It was reported later that a product titer of 48.45&#xa0;g/L for L-xylulose was reached by co-expressing the two enzymes in <italic>E. coli</italic> with pETDuet-xdh-smnox (<xref ref-type="bibr" rid="B34">Tesfay et al., 2021</xref>). They immobilized the <italic>E. coli</italic> cells expressing the two enzymes with entrapment, and a yield of 96% was obtained when the substrate concentration was 150&#xa0;mM (<xref ref-type="bibr" rid="B6">Gao et al., 2016a</xref>). The group then developed a cell-free system containing the two enzymes for the synthesis of L-xylulose from arabinitol, and a final yield of 78.4% was achieved when the substrate concentration was 250&#xa0;mM (<xref ref-type="bibr" rid="B7">Gao et al., 2016b</xref>). Then they immobilized the two enzymes onto inorganic hybrid nanoflowers to enhance the L-xylulose production, and a maximum yield of 91% was observed, which was 2.9-fold higher than the free enzymes (<xref ref-type="bibr" rid="B24">Patel et al., 2017</xref>). They demonstrated a sequential co-immobilization of L-arabinitol dehydrogenase and NADH oxidase for the conversion of L-arabinitol to L-xylulose recently (<xref ref-type="bibr" rid="B25">Patel et al., 2024</xref>). The results indicated that the co-immobilized enzymes exhibited 6.5-fold higher activity than that of free enzymes, and the maximum conversion of 93.6% was obtained.</p>
<p>Generally, xylitol could be enzymatically converted into xylulose with xylitol dehydrogenase. Another possible enzymatic route is using arabinitol dehydrogenase, which is an NAD-dependent short-chain dehydrogenase that can convert xylitol to L-xylulose. <xref ref-type="bibr" rid="B46">Zhu et al. (2022)</xref> cloned arabinitol dehydrogenase (ArDH) from <italic>Aspergillus nidulans</italic> for the preparation of L-xylulose from xylitol and coupled NOX for the cofactor NAD<sup>&#x2b;</sup> regeneration (<xref ref-type="fig" rid="F2">Figure 2</xref>). It was found that the high substrate concentration of xylitol inhibits the enzymatic reaction. A yield of 92.7% was achieved when the substrate concentration was 10&#xa0;mM, but the conversion was only 18.4% when the substrate concentration was 80&#xa0;mM.</p>
<fig id="F2" position="float">
<label>FIGURE 2</label>
<caption>
<p>Enzymatic preparation of L-xylulose with ArDH coupled with NOX.</p>
</caption>
<graphic xlink:href="fbioe-13-1650600-g002.tif">
<alt-text content-type="machine-generated">Chemical reaction diagram showing the conversion of xylitol to L-xylulose. Xylitol, with a blue hydroxyl group, is oxidized to L-xylulose, with a red carbonyl group. The reaction involves NAD+, NADH, and enzymes ArDH and NOX, with arrows indicating the flow and involvement of water (H2O) and oxygen (O2).</alt-text>
</graphic>
</fig>
</sec>
<sec id="s2-3">
<title>2.3 Enzymatic synthesis of L-gulose with mannitol dehydrogenase</title>
<p>L-Gulose is a building block for the preparation of the anticancer drug bleomycin and antiviral agents. The chemical synthesis routes require complex protections and deprotections of the hydroxyl groups, resulting in inconvenience, high cost, and inefficiency. Woodyer et al. constructed recombinant <italic>Escherichia coli</italic> harboring mannitol dehydrogenase for the production of L-gulose and L-tagatose (<xref ref-type="bibr" rid="B36">Woodyer et al., 2010</xref>). The productivities were only 4.6 and 0.9&#xa0;g/L for L-tagatose and L-gulose, respectively. Later, mannitol dehydrogenase and NADH oxidase were co-expressed in <italic>E. coli</italic> by using the pACYDuet-1 vector, and the whole cell expressing mannitol dehydrogenase and NADH oxidase was employed to convert D-sorbitol to L-gulose (<xref ref-type="fig" rid="F3">Figure 3</xref>). With the highly efficient cofactor regeneration, a volumetric product titer of 5.5&#xa0;g/L for L-gulose was obtained after the optimization of the reaction conditions, including pH, temperature, substrate concentration, and metal ions.</p>
<fig id="F3" position="float">
<label>FIGURE 3</label>
<caption>
<p>Enzymatic synthesis of L-gulose with mannitol dehydrogenase (MDH) and NOX.</p>
</caption>
<graphic xlink:href="fbioe-13-1650600-g003.tif">
<alt-text content-type="machine-generated">Chemical reaction converting D-Sorbitol to L-Gulose using MDH. NAD+ is reduced to NADH, while NADH is oxidized back to NAD+ by NOX with oxygen and water as coproducts.</alt-text>
</graphic>
</fig>
</sec>
<sec id="s2-4">
<title>2.4 Production of L-sorbose with sorbitol dehydrogenase</title>
<p>L-Sorbose is an intermediate for the synthesis of L-ascorbic acid, and could be used as the starting material to synthesize the glycosidase inhibitor 1-deoxygalactonojirim and other rare sugars like L--tagatose and L-iditol. <xref ref-type="bibr" rid="B12">Kim et al. (2016)</xref> cloned, characterized, and immobilized a highly efficient sorbitol dehydrogenase from <italic>Gluconobacter oxydans</italic> G624, which showed higher activity toward D-sorbitol. However, the sorbitol dehydrogenase was inhibited by NADPH; thus, it is necessary to lower the cofactor concentration in the reaction system. They then co-expressed sorbitol dehydrogenase and NADPH oxidase in <italic>E. coli</italic> for the production of L-sorbose (<xref ref-type="bibr" rid="B13">Kim et al., 2019</xref>). After optimization of the reaction conditions, a high yield of 92% was achieved by using the whole-cell catalysts (<xref ref-type="fig" rid="F4">Figure 4</xref>). The L-sorbose production was 4.1&#xa0;g/L, which was 20.5-fold higher than that of <italic>E. coli</italic> without NADPH oxidase for the cofactor regeneration. Later, they discovered a novel NADPH oxidase which could oxidize both NADH and NADPH (<xref ref-type="bibr" rid="B8">Gao et al., 2019</xref>), and the L-sorbose production could be improved 53-fold with this enzyme. One drawback of the sorbitol dehydrogenase is that the working pH range (9.0&#x2013;10.5) is much higher than the optimal pH of NADPH oxidase.</p>
<fig id="F4" position="float">
<label>FIGURE 4</label>
<caption>
<p>Enzymatic conversion of D-sorbitol to produce L-sorbose with sorbitol dehydrogenase (SlDH) and NOX.</p>
</caption>
<graphic xlink:href="fbioe-13-1650600-g004.tif">
<alt-text content-type="machine-generated">Chemical reaction diagram showing the conversion of D-sorbitol to L-sorbose. The process involves the enzymes SIDH and NOX, with arrows indicating the direction of the reaction. NADP&#x207A; is reduced to NADPH in the cycle.</alt-text>
</graphic>
</fig>
</sec>
</sec>
<sec id="s3">
<title>3 Enzymatic production of ketone with dehydrogenase coupled cofactor regeneration</title>
<p>Alcohol dehydrogenase (ADH) is the main enzyme catalyzing the oxidation of alcohol substrate to ketone product. The typical dehydrogenation reaction involves the oxidation of alcohol with the oxidized NAD(P)<sup>&#x2b;</sup> as the electron acceptor. A practical challenge in applying the ADHs for the oxidation of alcohol is the consumption of NAD(P)<sup>&#x2b;</sup>. Therefore, it is feasible to recycle the cofactor NAD(P)<sup>&#x2b;</sup> in the ADH-catalyzed oxidation of alcohol to the synthesis of ketone.</p>
<sec id="s3-1">
<title>3.1 Enzymatic synthesis of acetoin with acetaldehyde lyase (FLS)</title>
<p>Acetoin has been used in the food and pharmaceutical industries as a flavor enhancer and precursor for alkaloid ligustrazine (<xref ref-type="bibr" rid="B26">Peng et al., 2020</xref>). It could be produced with chemical reduction of diacetyl, fermentation from microbial cells, or enzymatic production from ethanol (<xref ref-type="bibr" rid="B16">Li et al., 2022a</xref>). Although some strains, including <italic>Enterobacter, Klebsiella, Serratia, Saccharomyces cerevisiae,</italic> and <italic>Bacillus</italic> could be utilized for the production of acetoin (<xref ref-type="bibr" rid="B16">Li et al., 2022a</xref>), the yield was low because acetoin is an intermediate in the 2,3-butanediol metabolic pathway. By deleting the butanediol dehydrogenase encoding gene, which converts acetoin to 2,3-butanediol, and overexpressing NADH oxidase (NOX) to enhance the cofactor regeneration, the final yield of 100.1&#xa0;g/L was achieved (<xref ref-type="bibr" rid="B2">Bae et al., 2016</xref>). Later, Guo et al. co-expressed butanediol dehydrogenase, hemoglobin, and NADH oxidase in <italic>E. coli</italic> for the production of acetoin, and a product titer of 86.74&#xa0;g/L was obtained. To overcome the complex regulation of cell growth and purification of acetoin from the fermentation medium, <xref ref-type="bibr" rid="B16">Li et al. (2022a)</xref> developed an enzymatic cascade reaction for the production of acetoin. They immobilized ethanol dehydrogenase (EtDH), NOX, and formolase (FLS) onto epoxy-modified magnetic nanoparticles for the synthesis of acetoin (<xref ref-type="fig" rid="F5">Figure 5</xref>). In the cascade enzymatic reactions, EtDH catalyzes the conversion of ethanol to acetaldehyde, which is subsequently transferred to acetoin with the catalysis of formolase. NADH oxidase is responsible for the regeneration of NAD<sup>&#x2b;</sup> in the first enzymatic step. A high conversion of 90% was achieved by using the three immobilized enzymes for one-pot biosynthesis of acetoin, suggesting that this is a promising way to produce value-added acetoin from ethanol.</p>
<fig id="F5" position="float">
<label>FIGURE 5</label>
<caption>
<p>Cascade enzymatic synthesis of acetoin from ethanol with ethanol dehydrogenase (EtDH), NOX, and Formolase (FLS).</p>
</caption>
<graphic xlink:href="fbioe-13-1650600-g005.tif">
<alt-text content-type="machine-generated">Chemical reaction diagram showing the conversion of ethanol to acetaldehyde using EtDH. Ethanol is depicted with a carbon atom bonded to hydrogen and an OH group. Acetaldehyde, with its carbon-oxygen double bond, is formed. The process involves NAD&#x207A; and NADH cycle, H&#x2082;O, O&#x2082;, and NOX. The acetaldehyde further reacts with FLS to form (3R)-acetoin and (3S)-acetoin.</alt-text>
</graphic>
</fig>
</sec>
<sec id="s3-2">
<title>3.2 Synthesis of 1,3-dihydroacetone from glycerol with glycerol dehydrogenase</title>
<p>Glycerol is the byproduct of biodiesel and a cheap raw material, and it is economical to convert it to value-added chemicals (<xref ref-type="bibr" rid="B4">Fokum et al., 2021</xref>; <xref ref-type="bibr" rid="B18">Li et al., 2023</xref>). Fan et al. immobilized whole cells harboring glycerol dehydrogenase (GDH) and NADH oxidase genes through a click reaction (<xref ref-type="bibr" rid="B3">Fan et al., 2021</xref>). By employing the immobilized whole cell, glycerol could be converted into 1,3-dihydroxyacetone, around 400 times higher in price. The same group immobilized GDH and Nox for bioconversion of glycerol to 1,3-dihydroxyacetone, and the final product concentration of 3.5&#xa0;mM was obtained, which was four times higher than that without cofactor regeneration (<xref ref-type="fig" rid="F6">Figure 6</xref>). Then they combined immobilized GDH and NOX with cross-linking to form aggregates for efficient regeneration of NAD<sup>&#x2b;</sup>; there was about a 1.5 times improvement compared with the free enzyme system (<xref ref-type="bibr" rid="B39">Xu et al., 2020</xref>). By using the combined cross-linked enzyme aggregate, about 4.6% glycerol was converted into 1,3-dihydroxyacetone with a final concentration of 9.4&#xa0;mM. The combined cross-linked enzyme aggregate could regenerate NADH with a high speed of a turnover number of 2137 in the production of 1,3-dihydroxyacetone.</p>
<fig id="F6" position="float">
<label>FIGURE 6</label>
<caption>
<p>Bioconversion of glycerol with GDH and NOX mixed with NAD<sup>&#x2b;</sup> regeneration.</p>
</caption>
<graphic xlink:href="fbioe-13-1650600-g006.tif">
<alt-text content-type="machine-generated">Chemical reaction diagram showing glycerol converting to 1,3-dihydroxyacetone. The reaction involves the enzyme GDH, with NAD&#x207A; reduced to NADH. Oxygen (O&#x2082;) and water (H&#x2082;O) participate, with NOX cycling NADH back to NAD&#x207A;. Glycerol&#x27;s hydroxyl group is blue, and the ketone group on 1,3-dihydroxyacetone is red.</alt-text>
</graphic>
</fig>
</sec>
<sec id="s3-3">
<title>3.3 Enzymatic production of statin precursor with alcohol dehydrogenase and NADPH oxidase</title>
<p>Generally, an excess of reactive oxygen species will lead to plenty of devastating diseases (<xref ref-type="bibr" rid="B23">Panday et al., 2015</xref>). Among these diseases, cardiovascular diseases are the main leading cause of death worldwide. The treatments of the diseases are focused on using drugs such as statins to decrease low-density lipoprotein cholesterol. One attractive approach for the synthesis of statins is the enzymatic route, in which the oxidation of chlorolactol to chlorolactone is the key step. The whole cell co-expressing alcohol dehydrogenase and NADPH oxidase could help to produce chlorolactone (<xref ref-type="fig" rid="F7">Figure 7</xref>), which was performed by co-expressing the two enzymes by <xref ref-type="bibr" rid="B11">Jiao et al. (2016)</xref>. Another group immobilized alcohol dehydrogenase and NADPH oxidase onto Eupergit CM, Amino-agarose, and epoxy agarose-UAB, and used the immobilized enzymes to catalyze the conversion of chlorolactol, and a yield of 94.7% for chlorolactone was obtained (<xref ref-type="bibr" rid="B9">Garcia-Bofill et al., 2021</xref>).</p>
<fig id="F7" position="float">
<label>FIGURE 7</label>
<caption>
<p>Enzymatic oxidation of chlorolactol to chlorolactone with alcohol dehydrogenase (ADH) and NOX.</p>
</caption>
<graphic xlink:href="fbioe-13-1650600-g007.tif">
<alt-text content-type="machine-generated">Chemical reaction diagram showing the conversion of chlorolactol to chlorolactone. The reaction involves ADH with NADP&#x207A; and NADPH as cofactors, and NOX involved with H&#x2082;O and O&#x2082;. Chlorolactol has an OH group, while chlorolactone has a double-bonded oxygen.</alt-text>
</graphic>
</fig>
</sec>
<sec id="s3-4">
<title>3.4 Biosynthesis of 2,5-dimethylpyrazine with L-threonine dehydrogenase</title>
<p>L-Threonine is widely distributed in nature and could be prepared through microbial fermentation, making it a relatively cheap raw material. Thus, the conversion of L-threonine to a more valuable chemical is attractive and engaging for the chemical or pharmaceutical industry. <xref ref-type="bibr" rid="B20">Liu et al. (2023)</xref> reconfigured the L-threonine metabolic pathway in <italic>Escherichia coli</italic> by overexpressing NADH oxidase and L-threonine dehydrogenase (TDH) using the pACYCDuet-1 vector. The whole cell can effectively catalyze L-threonine to L-2-aminoacetoacetic acid, which could be further converted into 2,5-dimethylpyrazine. And the recombinant <italic>E. coli</italic> overexpressing the two enzymes can convert L-threonine to produce 2,5-dimethylpyrazine (<xref ref-type="fig" rid="F8">Figure 8</xref>), which is a flavor compound and the precursor for some drugs, and a yield of 2.0&#xa0;g/L was obtained with a molar conversion of 22.2%.</p>
<fig id="F8" position="float">
<label>FIGURE 8</label>
<caption>
<p>Synthesis of 2,5-dimethylpyrazine using L-threonine as a substrate with TDH.</p>
</caption>
<graphic xlink:href="fbioe-13-1650600-g008.tif">
<alt-text content-type="machine-generated">Chemical pathway depicting the conversion of L-threonine to L-2-aminoacetoacetic acid via TDH, with interaction of NAD plus and NADH through NOX. The pathway continues with the release of CO2 to form aminoacetone, then water interacts to form 3,6-dihydro-2,5-dimethylpyrazine, finally resulting in 2,5-dimethylpyrazine with the release of water.</alt-text>
</graphic>
</fig>
</sec>
</sec>
<sec id="s4">
<title>4 Enzymatic synthesis of vanillic acid with vanillin dehydrogenase</title>
<p>Vanillic acid has been widely used in the pharmaceutical, food, cosmetic, and flavor industries because of its biological activities (<xref ref-type="bibr" rid="B19">Liaqat et al., 2023</xref>). Chemical synthesis of vanillic acid has some disadvantages, including low yield and environmental pollution (<xref ref-type="bibr" rid="B10">Ji et al., 2024</xref>). The alternative route for vanillic acid is the enzymatic transformation of lignin, which is a greener production method. <xref ref-type="bibr" rid="B40">Xu et al. (2024)</xref> cloned and expressed vanillin dehydrogenase (VDH) from <italic>Bacillus ligniniphilus</italic> L1 and NADH oxidase (NOX) from <italic>Streptococcus pyogenes</italic> for the biotransformation of vanillin into vanillic acid. They immobilized VDH and NOX to form cross-linked enzyme aggregates (Combi-CLVNAs). The Combi-CLVAs were used to produce vanillic acid (<xref ref-type="fig" rid="F9">Figure 9</xref>). With fed-batch addition of vanillin to the reaction mixture, the production of 44.21&#xa0;mM vanillic acid was obtained, which was 22.5-fold higher than without NOX in the presence of 2&#xa0;mM NAD<sup>&#x2b;</sup>. After 4 cycles, a total of 149.98&#xa0;mM vanillic acid was harvested using Combi-CLVNAs. Finally, 38.69&#xa0;mM vanillic acid was prepared from vanillin-rich extracts derived from lignin depolymerization with combi-CLVNAs. In the whole process using combi-CLVNAs, there were no by-products, which provides a green way for vanillic acid production.</p>
<fig id="F9" position="float">
<label>FIGURE 9</label>
<caption>
<p>Enzymatic synthesis of vanillic acid with VDH and NOX.</p>
</caption>
<graphic xlink:href="fbioe-13-1650600-g009.tif">
<alt-text content-type="machine-generated">Chemical reaction diagram showing the conversion of vanillin to vanillic acid. Vanillin&#x27;s structure includes a methoxy and hydroxyl group with a blue carbonyl group. The reaction pathway involves VDH enzyme, NAD, NADH, NOX, H2O, and O2. Vanillic acid features a carboxyl group highlighted in red.</alt-text>
</graphic>
</fig>
</sec>
<sec id="s5">
<title>5 Kinetic resolution of racemic phenylethanol with alcohol dehydrogenase</title>
<p>Optically active alcohols are important pharmaceutical or chemical intermediates and could be biosynthesized with alcohol dehydrogenase. However, these enzymes are highly dependent on the oxidized NAD cofactors, which are too expensive to be used stoichiometrically. So, scientists tried to use NADH oxidase to regenerate the cofactor. (<italic>R</italic>)-alcohol dehydrogenase from <italic>Lactobacillus brevis</italic> (<italic>Lb</italic>ADH) was used to enantioselectively oxidize racemic phenylethanol to produce acetophenone, and another product is (S)-phenylethanol, and NADH oxidase from <italic>Lactobacillus sanfranciscensis</italic> was employed to reduce O<sub>2</sub> to H<sub>2</sub>O, coupling with the regeneration of cofactor NAD<sup>&#x2b;</sup> (<xref ref-type="bibr" rid="B29">Riebel et al., 2003</xref>). The mutant of <italic>Lb</italic>ADH G37D prefers NAD<sup>&#x2b;</sup> as the cofactor and is coupled with LsNox to yield 50% conversion of racemic phenylethanol to (<italic>S</italic>)-phenylethanol and acetophenone. It was found that more than 100 turnovers were obtained depending on the relative concentration of alcohol to cofactor. The regeneration system can also recycle NADP<sup>&#x2b;</sup> with the same NADH oxidase.</p>
<p>
<xref ref-type="bibr" rid="B37">Wu et al. (2022)</xref> designed and constructed fusion proteins containing alcohol dehydrogenase (ADH) and NADH oxidase for the production of chiral alcohols (<xref ref-type="fig" rid="F10">Figure 10</xref>). The NOX in the fusion proteins exhibited much higher specific activities than that of the individual enzyme, which could regenerate NAD<sup>&#x2b;</sup> in the enantioselective oxidation of racemic 1-phenylethanol. The fusion proteins linked NOX at the N-terminus showed higher turnover numbers than the individual enzyme, especially at low cofactor concentrations.</p>
<fig id="F10" position="float">
<label>FIGURE 10</label>
<caption>
<p>Enantioselective oxidation of racemic phenylethanol with alcohol dehydrogenase (ADH) and NOX.</p>
</caption>
<graphic xlink:href="fbioe-13-1650600-g010.tif">
<alt-text content-type="machine-generated">Chemical reaction scheme showing the oxidation of racemic alcohol to a ketone and an enantiomer. Alcohol dehydrogenase (ADH) converts the racemic alcohol to a ketone and an (R)-alcohol. Nicotinamide adenine dinucleotide (NAD+) is reduced to NADH and regenerated by nicotinamide oxidase (NOX) using oxygen to form hydrogen peroxide.</alt-text>
</graphic>
</fig>
<p>To expand the application of alcohol dehydrogenase for alcohol oxidation, the cofactor must be recycled to make the process economical because of the stoichiometric consumption of the expensive NADP. <xref ref-type="bibr" rid="B1">Aalbers and Fraaije (2019)</xref> designed an artificial alcohol oxidase by fusion of alcohol dehydrogenase and NADPH oxidase for continuous oxidation of alcohol (<xref ref-type="fig" rid="F11">Figure 11</xref>). In this system, a catalytic amount of NADP<sup>&#x2b;</sup> was required, and the purified enzymes could perform a good catalytic efficiency of 69%&#x2013;99% conversion and 99% ee with racemic phenylethanol as the substrate. Compared with other fusion proteins, the NADH oxidase fusion partner has some advantages and could be a valuable tool for the development of robust catalysts. The NADH oxidase was immobilized for the regeneration of NAD<sup>&#x2b;</sup> in the kinetic resolution of racemic phenylethanol (<xref ref-type="bibr" rid="B30">Rocha-Mart&#xed;n et al., 2011</xref>).</p>
<fig id="F11" position="float">
<label>FIGURE 11</label>
<caption>
<p>Kinetic resolution of racemic phenylethanol with fused NOX and ADH.</p>
</caption>
<graphic xlink:href="fbioe-13-1650600-g011.tif">
<alt-text content-type="machine-generated">Chemical reaction diagram showing the oxidation of 1-phenylethanol to acetophenone and S-1-phenylethanol. The reaction involves alcohol dehydrogenase (ADH) and involves NADP+, NADPH, hydrogen peroxide, and oxygen facilitated by NADPH oxidase (NOX).</alt-text>
</graphic>
</fig>
</sec>
<sec id="s6">
<title>6 Conclusion and future outlook</title>
<p>Now, all the chemical synthesis and transformations are undergoing the shift from chemical methods to biological routes. With the advances of synthetic biology, important enzymes and whole cells are engineered and have great potential applications in pharmaceutical, food, cosmetic, petrochemical, and other industries. Oxidoreductases, as the largest enzyme class, have essential biological functions in life, and will have a huge future market in the industry. However, although the cofactor is expensive, most oxidoreductases need cofactors to transfer electrons, atoms, or chemical groups in a stoichiometric amount. From the industrial aspects, the regeneration of the cofactor will lower the cost and make the preparation of valuable chemicals economical. NAD(P)H oxidases have wide applications in biotechnology and are used as genetic tools to regulate physiological roles of compartment-specific changes in NAD(P)<sup>&#x2b;</sup>/NAD(P)H equilibrium in living cells.</p>
<p>Much research work has been done on the discovery, catalytic mechanism, biochemical characterization, and deciphering the structure of NAD(P)H oxidase. It is easy to conclude that value-added chemicals could be prepared with NAD(P)-dependent dehydrogenases, which need the cofactor regeneration with NAD(P)H oxidases. However, there are some biocompatibility issues for the enzymes. It is known that most dehydrogenases have a pH optimum around 8.0&#x2013;10.0, and some NAD(P)H oxidases are not active in the pH range. For example, the optimal pH of NOX from <italic>Lactobacillus rhamnosus</italic> is 5.5, which cannot work together with most dehydrogenases (<xref ref-type="bibr" rid="B42">Zhang et al., 2012</xref>). To overcome the pH incompatibility, the enzyme was engineered to shift the pH optimum and working pH range by mutation of Asp251 to Arg, and the activity was improved 1.44-fold than the wild-type at pH 7.5 (<xref ref-type="bibr" rid="B44">Zhou et al., 2021</xref>). NADPH is more difficult to recycle, and the price of NADPH is higher than that of NADH; So, the NAD(P)H oxidases that could regenerate both NAD<sup>&#x2b;</sup> and NADP<sup>&#x2b;</sup> are more interesting for industrial production. Generally, engineering the surface, catalytic pocket, and the substrate binding domain is a practical approach for enhancing the production of value-added products (<xref ref-type="fig" rid="F12">Figure 12</xref>). These enzymes have achieved notable enhancements in catalytic efficiency, substrate specificity, and operational stability through site-directed evolution and rational design. The dual-substrate NOXs with the ability to switch substrate from NADH to NADPH open new avenues for their industrial applications in the biosynthesis of high-value chemicals. Furthermore, the adaptation of these enzymes to varying pH and temperature conditions is crucial for their integration into industrial processes, ensuring compatibility and efficiency. Discovering new enzymes with high specific activity on both substrates would benefit the applications (<xref ref-type="bibr" rid="B8">Gao et al., 2019</xref>; <xref ref-type="bibr" rid="B14">Li et al., 2018</xref>), or engineering the enzyme protein to switch the substrate specificity by mutation of Leu179 to Ser (<xref ref-type="bibr" rid="B15">Li et al., 2019</xref>). There was a report that engineered NADH oxidase for the regeneration of oxidized non-natural cofactor nicotinamide cytosine dinucleotide (NCD), which could expand the development of NCD-linked redox system (<xref ref-type="bibr" rid="B35">Wang et al., 2025</xref>). There is no doubt that more and more NAD(P)-dependent dehydrogenases will be applied in industry with the regeneration of NAD(P)<sup>&#x2b;</sup> by NAD(P)H oxidase. The synergy achieved by coupling engineered NADH oxidase with other enzymes in biocatalytic systems has demonstrated remarkable improvements in product yield and reaction efficiency.</p>
<fig id="F12" position="float">
<label>FIGURE 12</label>
<caption>
<p>Protein engineering of the surface, catalytic pocket, and substrate binding domain to improve the catalytic activity of NOX to enhance the production of value-added chemicals.</p>
</caption>
<graphic xlink:href="fbioe-13-1650600-g012.tif">
<alt-text content-type="machine-generated">Diagram illustrating enzymatic transformation. A substrate undergoes engineering within a catalytic pocket to enhance substrate specificity. This process involves NOX enzymes, resulting in value-added products. Visual elements include surface and molecular structures.</alt-text>
</graphic>
</fig>
<p>NAD(P)H oxidases catalyze the oxidation of NAD(P)H to regenerate NAD(P)<sup>&#x2b;</sup>, in which the product is the oxidized form of the chemicals. The contrary reaction for the production of reduced forms of chemicals to form a chiral center is attracting more attention because of the sharply increasing demand for enzymatic transformations. To regenerate the reduced form NAD(P)H, many enzymes, including glucose dehydrogenase (<xref ref-type="bibr" rid="B45">Zhu et al., 2019</xref>), formate dehydrogenase (<xref ref-type="bibr" rid="B38">Wu et al., 2025</xref>), and phosphite dehydrogenase (<xref ref-type="bibr" rid="B43">Zhang et al., 2022</xref>) have been employed. However, to drive the reaction to the product, a second substrate and product must be introduced for the regeneration enzyme, which will complicate the separation and purification of the products. Recycling or regenerating the reduced form NAD(P)H of the cofactor without introducing by-products is a challenge for enzymologists and chemists.</p>
</sec>
</body>
<back>
<sec sec-type="author-contributions" id="s7">
<title>Author contributions</title>
<p>L-JZ: Writing &#x2013; review and editing, Conceptualization. S-XL: Writing &#x2013; original draft. TH: Writing &#x2013; original draft. YW: Writing &#x2013; original draft. Y-WZ: Writing &#x2013; review and editing, Conceptualization, Supervision.</p>
</sec>
<sec sec-type="funding-information" id="s8">
<title>Funding</title>
<p>The author(s) declare that financial support was received for the research and/or publication of this article. The authors appreciated the financial support from the Elderly Health Research Project of Jiangsu Provincial Health Commission (No. LKM2022083).</p>
</sec>
<sec sec-type="COI-statement" id="s9">
<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>
<p>The author(s) declared that they were an editorial board member of Frontiers, at the time of submission. This had no impact on the peer review process and the final decision.</p>
</sec>
<sec sec-type="ai-statement" id="s10">
<title>Generative AI statement</title>
<p>The author(s) declare that no Generative AI was used in the creation of this manuscript.</p>
<p>Any alternative text (alt text) provided alongside figures in this article has been generated by Frontiers with the support of artificial intelligence and reasonable efforts have been made to ensure accuracy, including review by the authors wherever possible. If you identify any issues, please contact us.</p>
</sec>
<sec sec-type="disclaimer" id="s11">
<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="s12">
<title>Abbreviations</title>
<p>ADH, alcohol dehydrogenase; ArDH, arabinitol dehydrogenase; EtDH, ethanol dehydrogenase; FLS, formolase; GDH, glycerol dehydrogenase; <italic>Gat</italic>DH, Galactitol dehydrogenase; MDH, mannitol dehydrogenase; <italic>Sl</italic>DH, sorbitol dehydrogenase; TDH-L-threonine dehydrogenase; NAD, Nicotinamide adenine dinucleotide; NOX, NADH oxidase/NADPH oxidase; ROS, reactive oxygen species; VDH, vanillin dehydrogenase.</p>
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