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<front>
<journal-meta>
<journal-id journal-id-type="publisher-id">Front. Bioeng. Biotechnol.</journal-id>
<journal-title-group>
<journal-title>Frontiers in Bioengineering and Biotechnology</journal-title>
<abbrev-journal-title abbrev-type="pubmed">Front. Bioeng. Biotechnol.</abbrev-journal-title>
</journal-title-group>
<issn pub-type="epub">2296-4185</issn>
<publisher>
<publisher-name>Frontiers Media S.A.</publisher-name>
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</journal-meta>
<article-meta>
<article-id pub-id-type="publisher-id">1754875</article-id>
<article-id pub-id-type="doi">10.3389/fbioe.2026.1754875</article-id>
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<article-categories>
<subj-group subj-group-type="heading">
<subject>Brief Research Report</subject>
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</article-categories>
<title-group>
<article-title>Prediction of non-intuitive metabolic targets with bayesian metabolic control analysis to improve 3-hydroxypropionic acid production in <italic>Aspergillus niger</italic>
</article-title>
<alt-title alt-title-type="left-running-head">Dai 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.2026.1754875">10.3389/fbioe.2026.1754875</ext-link>
</alt-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname>Dai</surname>
<given-names>Ziyu</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
</xref>
<xref ref-type="aff" rid="aff2">
<sup>2</sup>
</xref>
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</contrib>
<contrib contrib-type="author">
<name>
<surname>Zucker</surname>
<given-names>Jeremy D.</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
</xref>
<xref ref-type="aff" rid="aff3">
<sup>3</sup>
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<contrib contrib-type="author">
<name>
<surname>Han</surname>
<given-names>Yichao</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
</xref>
<xref ref-type="aff" rid="aff2">
<sup>2</sup>
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<contrib contrib-type="author">
<name>
<surname>Mahserejian</surname>
<given-names>Shant</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
</xref>
<xref ref-type="aff" rid="aff3">
<sup>3</sup>
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<name>
<surname>Cottam</surname>
<given-names>Joseph</given-names>
</name>
<xref ref-type="aff" rid="aff3">
<sup>3</sup>
</xref>
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<surname>Munoz</surname>
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</name>
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<sup>1</sup>
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<xref ref-type="aff" rid="aff3">
<sup>3</sup>
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<name>
<surname>Gao</surname>
<given-names>Yuqian</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
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<xref ref-type="aff" rid="aff3">
<sup>3</sup>
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<contrib contrib-type="author">
<name>
<surname>Yuan</surname>
<given-names>Guoliang</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
</xref>
<xref ref-type="aff" rid="aff2">
<sup>2</sup>
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</contrib>
<contrib contrib-type="author">
<name>
<surname>Hofstad</surname>
<given-names>Beth A.</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
</xref>
<xref ref-type="aff" rid="aff2">
<sup>2</sup>
</xref>
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</contrib>
<contrib contrib-type="author">
<name>
<surname>Magnuson</surname>
<given-names>Jon K.</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
</xref>
<xref ref-type="aff" rid="aff2">
<sup>2</sup>
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</contrib>
<contrib contrib-type="author">
<name>
<surname>Kim</surname>
<given-names>Joonhoon</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
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<xref ref-type="aff" rid="aff2">
<sup>2</sup>
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<contrib contrib-type="author">
<name>
<surname>Kim</surname>
<given-names>Young-Mo</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
</xref>
<xref ref-type="aff" rid="aff3">
<sup>3</sup>
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<contrib contrib-type="author">
<name>
<surname>Burnum-Johnson</surname>
<given-names>Kristin E.</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
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<xref ref-type="aff" rid="aff3">
<sup>3</sup>
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<contrib contrib-type="author" corresp="yes">
<name>
<surname>Pomraning</surname>
<given-names>Kyle R.</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
</xref>
<xref ref-type="aff" rid="aff2">
<sup>2</sup>
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<aff id="aff1">
<label>1</label>
<institution>DOE Agile BioFoundry</institution>, <city>Emeryville</city>, <state>CA</state>, <country country="US">United States</country>
</aff>
<aff id="aff2">
<label>2</label>
<institution>Energy and Environment Directorate, Pacific Northwest National Laboratory</institution>, <city>Richland</city>, <state>WA</state>, <country country="US">United States</country>
</aff>
<aff id="aff3">
<label>3</label>
<institution>Earth and Biological Sciences Directorate, Pacific Northwest National Laboratory</institution>, <city>Richland</city>, <state>WA</state>, <country country="US">United States</country>
</aff>
<author-notes>
<corresp id="c001">
<label>&#x2a;</label>Correspondence: Kyle R. Pomraning, <email xlink:href="mailto:kyle.pomraning@pnnl.gov">kyle.pomraning@pnnl.gov</email>
</corresp>
</author-notes>
<pub-date publication-format="electronic" date-type="pub" iso-8601-date="2026-02-17">
<day>17</day>
<month>02</month>
<year>2026</year>
</pub-date>
<pub-date publication-format="electronic" date-type="collection">
<year>2026</year>
</pub-date>
<volume>14</volume>
<elocation-id>1754875</elocation-id>
<history>
<date date-type="received">
<day>26</day>
<month>11</month>
<year>2025</year>
</date>
<date date-type="rev-recd">
<day>22</day>
<month>01</month>
<year>2026</year>
</date>
<date date-type="accepted">
<day>02</day>
<month>02</month>
<year>2026</year>
</date>
</history>
<permissions>
<copyright-statement>Copyright &#xa9; 2026 Dai, Zucker, Han, Mahserejian, Cottam, Munoz, Gao, Yuan, Hofstad, Magnuson, Kim, Kim, Burnum-Johnson and Pomraning.</copyright-statement>
<copyright-year>2026</copyright-year>
<copyright-holder>Dai, Zucker, Han, Mahserejian, Cottam, Munoz, Gao, Yuan, Hofstad, Magnuson, Kim, Kim, Burnum-Johnson and Pomraning</copyright-holder>
<license>
<ali:license_ref start_date="2026-02-17">https://creativecommons.org/licenses/by/4.0/</ali:license_ref>
<license-p>This is an open-access article distributed under the terms of the <ext-link ext-link-type="uri" xlink:href="https://creativecommons.org/licenses/by/4.0/">Creative Commons Attribution License (CC BY)</ext-link>. 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.</license-p>
</license>
</permissions>
<abstract>
<p>Development of efficient bioconversion processes is limited by the ability to predictably improve metabolic flux. Here we deployed Bayesian Metabolic Control Analysis as a platform to integrate multi-omics data with metabolic modeling and evaluated its ability to predict genetic interventions that improve metabolic flux. Global Metabolomics and proteomics data was collected from 17 <italic>Aspergillus niger</italic> strains engineered to produce the platform biochemical 3-hydroxypropionic acid from which seven actional genetic interventions were predicted from significant flux control coefficients. Of the suggested genetic interventions, two were present within the intuitively designed strains used for training (malonic semialdehyde dehydrogenase and pyruvate carboxylase) while five predicted targets were present within non-intuitive areas of the metabolic network including 5-formyltetrahydrofolate deformylase and four mitochondrial enzymes, alcohol dehydrogenase, succinyl-CoA ligase, aspartate aminotransferase, and malate dehydrogenase. Six of the targets were validated in the highest performing 3-HP strain used for multi-omics data generation which contained a prior disruption of the highest scoring target malonic semialdehyde dehydrogenase. Predicted directional perturbation of five of the six tested targets significantly improved titer and rate of 3-HP production and two significantly improved yield. The greatest improvements were observed following disruption of the non-intuitive target succinyl-CoA ligase which increased titer by 39% and yield by 29% (to 20.4&#xa0;g/L 3-HP and 0.31&#xa0;g 3-HP/g glucose) over the strains used for training. This study demonstrates the utility of Bayesian Metabolic Control Analysis and highlights the ability to predict meaningful genetic targets in unexpected areas of metabolism to improve engineered strains for bioconversion.</p>
</abstract>
<kwd-group>
<kwd>3HP</kwd>
<kwd>3-hydroxypropionic acid</kwd>
<kwd>Aspergillus niger</kwd>
<kwd>bayesian metabolic control analysis</kwd>
<kwd>non-intuitive</kwd>
<kwd>prediction</kwd>
</kwd-group>
<funding-group>
<award-group id="gs1">
<funding-source id="sp1">
<institution-wrap>
<institution>Bioenergy Technologies Office</institution>
<institution-id institution-id-type="doi" vocab="open-funder-registry" vocab-identifier="10.13039/open_funder_registry">10.13039/100011735</institution-id>
</institution-wrap>
</funding-source>
</award-group>
<funding-statement>The author(s) declared that financial support was received for this work and/or its publication. The work described herein was performed at the Agile Biofoundry, funded by the Bioenergy Technologies Office in the Office of Critical Minerals and Energy Innovation of the U.S. Department of Energy under Agreement 30038&#xa0;at Pacific Northwest National Laboratory, operated by Battelle for the US Department of Energy under contract DE-AC05-76RL01830. The views expressed herein do not necessarily represent the views of the U.S. Department of Energy or the United States Government.</funding-statement>
</funding-group>
<counts>
<fig-count count="3"/>
<table-count count="1"/>
<equation-count count="1"/>
<ref-count count="24"/>
<page-count count="8"/>
</counts>
<custom-meta-group>
<custom-meta>
<meta-name>section-at-acceptance</meta-name>
<meta-value>Synthetic Biology</meta-value>
</custom-meta>
</custom-meta-group>
</article-meta>
</front>
<body>
<sec sec-type="intro" id="s1">
<label>1</label>
<title>Introduction</title>
<p>Biological production of 3-hydroxypropionic acid (3-HP) from CO<sub>2</sub> derived feedstocks including lignocellulosic material is a promising route to reduce emissions during commodity scale chemical production (<xref ref-type="bibr" rid="B1">Bhagwat et al., 2021</xref>; <xref ref-type="bibr" rid="B8">Karp et al., 2017</xref>). 3-HP is a 3-carbon building block that can be used as a chemical precursor for production of a variety of valuable polymers through catalytic dehydration to acrylic acid (<xref ref-type="bibr" rid="B12">Li et al., 2018</xref>), or acrylonitrile through nitrilation (<xref ref-type="bibr" rid="B8">Karp et al., 2017</xref>) or other commodity scale chemicals including acrylamide, 1,3-propanediol, and methyl acrylates (<xref ref-type="bibr" rid="B20">Werpy and Petersen, 2004</xref>). The total market size for commodity scale chemical products that can be derived from 3-HP is well in excess of a million metric tons per year and offers a substantial opportunity to reduce emissions by transitioning from petrochemical to biologically derived feedstocks for polymer markets (<xref ref-type="bibr" rid="B19">Wang et al., 2023</xref>). Reducing emissions during production of 3C polymers will require low-carbon-intensity 3-HP at or near cost-parity to petroleum derived propylene from which acrylic acid is derived by oxidation. To achieve this will require production of 3-HP from inexpensive feedstocks at near theoretical yield while minimizing fermentation and downstream costs by using an acidic bioconversion host (<xref ref-type="bibr" rid="B1">Bhagwat et al., 2021</xref>; <xref ref-type="bibr" rid="B20">Werpy and Petersen, 2004</xref>).</p>
<p>Commercial interest in production of 3-HP as a platform chemical is long-standing with a well-developed patent landscape around the efficient production of 3-HP from sugars. Significant efforts have been focused on development of 3-HP pathways in model hosts including the yeast <italic>Saccharomyces cerevisiae</italic> and the bacterium <italic>Escherichia coli</italic>, which have achieved yields of 0.31 and 0.30&#xa0;g/g from glucose in neutral to mildly acidic conditions (<xref ref-type="bibr" rid="B21">Yu et al., 2022</xref>; <xref ref-type="bibr" rid="B23">Zhang et al., 2023</xref>). To reduce the cost of biomanufacturing via 3-HP as a platform biomolecule basic process requirements include (1) use of inexpensive readily existing feedstocks, (2) establishment of an acidic fermentation to minimize contamination, gypsum formation, and down-stream separation costs, (3) use of an industrial fungal host to enable a low pH fermentation, avoid phage induced process failure, and minimize feedstock nutrient additives, and (4) high titer, rate, and yield metrics. To accommodate all of the necessary process constraints we have focused on development of a theoretically high yield pathway in the acidophilic fungus <italic>A. niger</italic> which is capable of converting wide ranging lignocellulosic and waste feedstocks to 3-HP via the &#x3b2;-alanine bioconversion pathway, selected because it exhibits less dependency on oxygen uptake at high yields (<xref ref-type="bibr" rid="B2">Borodina et al., 2015</xref>) and operates in <italic>Aspergillus niger</italic> at acidic pH (<xref ref-type="bibr" rid="B5">Dai et al., 2023</xref>).</p>
<p>To increase the yield of 3-HP from sugars in <italic>A. niger</italic> fermentation we sought to adopt an approach that would generate predictions of reactions that control metabolic flux. To accomplish this, we leveraged Bayesian Metabolic Control Analysis (BMCA) to infer metabolic kinetics from genome-scale multi-omics data (<xref ref-type="bibr" rid="B14">McNaughton et al., 2021</xref>; <xref ref-type="bibr" rid="B18">St John et al., 2019</xref>). BMCA is a probabilistic framework for calculating metabolite and flux control coefficients from experimental data. Unlike traditional Metabolic Control Analysis (MCA), which provides point estimates, BMCA yields a posterior distribution for control coefficients, allowing for the quantification of uncertainty and the integration of diverse omics datasets (e.g., proteomics, metabolomics, fluxomics) to constrain the model. The BMCA framework employs the lin-log approximation of enzyme kinetics. This assumption linearizes the non-linear relationship between reaction rates (fluxes) and metabolite concentrations in logarithmic space, making the elasticities locally constant. This approach allows the system to be described by linear equations involving these coefficients, simplifying the calculation of steady-state to a single linear solve, while remaining accurate for small perturbations around a reference steady state. Here, we applied the BMCA framework with proteomics and metabolomics datasets to predict genes that control yield of 3-HP from sugars in engineered <italic>A. niger</italic> strains.</p>
</sec>
<sec sec-type="materials|methods" id="s2">
<label>2</label>
<title>Materials and methods</title>
<sec id="s2-1">
<label>2.1</label>
<title>Strain maintenance and cultivation</title>
<p>
<italic>Escherichia coli</italic> strain Top10 was used for routine plasmid DNA preparation. <italic>Aspergillus niger</italic> strains are all derived from ATCC11414 from the American Type Culture Collection (Rockville, MD, United States) and were grown on complete medium (CM) or potato dextrose agar (PDA) plates (<xref ref-type="bibr" rid="B7">JW and LL, 1991</xref>) at 30&#xa0;&#xb0;C for culture maintenance and spore preparation. About 5 &#xd7; 10<sup>4</sup> to 5 &#xd7; 10<sup>5</sup> spores were inoculated on CM agar (Petri dish) plates and incubated for 4&#xa0;days at 30&#xa0;&#xb0;C. Spores were harvested by washing with 5&#x2013;10&#xa0;mL sterile 0.4% Tween H<sub>2</sub>O and pelleted by centrifugation at 2,500&#xa0;<italic>g</italic> for 5&#xa0;min. The spores were re-suspended in the sterile 0.4% Tween H<sub>2</sub>O and enumerated with a hemocytometer. The spore suspensions were used for agar-plate or liquid cultures. The shake flask cultures were performed at 30&#xa0;&#xb0;C, 200 RPM in a New Brunswick Innova 44R stackable incubator shaker (Eppendorf, Endfield, CT, United States) with Pyrex 125&#xa0;mL or 250&#xa0;mL glass Erlenmeyer flasks which were prepared by filling with 5% Contrad 70 (Decon Labs, Inc., King of Prussia, PA, United States) and soaked overnight to remove any potential residues on the inside surface of flasks prior to general dishwashing. Silicon sponge closures were used for all flask cultures. For 3-HP production, sterile modified production medium B (mRDM; 100&#xa0;g/L glucose, 5&#xa0;g/L (NH<sub>4</sub>)<sub>2</sub>SO<sub>4</sub>, 0.11&#xa0;g/L KH<sub>2</sub>PO<sub>4</sub>, 2.08&#xa0;g/L MgSO<sub>4</sub>.7H<sub>2</sub>O, 0.13&#xa0;g/L CaCl<sub>2</sub>.2H<sub>2</sub>O, 0.074 g/L NaCl, 4&#xa0;mg/L CuSO<sub>4</sub>.5H<sub>2</sub>O, 110&#xa0;mg/L FeSO<sub>4</sub>.7H<sub>2</sub>O, 14&#xa0;mg/L MnCl<sub>2</sub>.4H<sub>2</sub>O, 26&#xa0;mg/L ZnSO<sub>4</sub>.7H<sub>2</sub>O) (<xref ref-type="bibr" rid="B5">Dai et al., 2023</xref>) was used for cultivations.</p>
</sec>
<sec id="s2-2">
<label>2.2</label>
<title>Strain construction</title>
<p>Strains were constructed as described previously (<xref ref-type="bibr" rid="B5">Dai et al., 2023</xref>; <xref ref-type="bibr" rid="B17">Pomraning et al., 2021</xref>) with additional strains containing intermediatory or combinatorial expression of transgene vectors included here to provide diversity in expression of 3-HP pathway components. In this study, all transgene expression cassettes were prepared with Gibson assembly master mix (NEB, Ipswich, MA, United States) and the DNA fragments were isolated by PCR with Phusion high-fidelity DNA polymerase (Thermo Fisher Scientific, Waltham, MA, United States). Strain ABF_008348, the highest performing strain in the reference dataset was used as the host for validation of target genes. In this background, targets for overexpression (purU, mdhA, pyc2, and aat1) were constructed using the several strong constitutive promoters (<italic>cox1</italic>, <italic>mbfA</italic>, <italic>tef1</italic>, and <italic>ubi4</italic>) and integrated into the genome. Strains containing deletions of <italic>adhD</italic>, <italic>suclg1</italic>, and <italic>suclg2</italic> were constructed using CRISPR-Cas9 system for single gene editing in <italic>A. niger</italic> (<xref ref-type="bibr" rid="B22">Yuan et al., 2024</xref>) to create large indels in the genes targeted for deletion. Protoplast preparation and chemical-mediated transformation followed the method described previously (<xref ref-type="bibr" rid="B4">Dai et al., 2013</xref>). All strains used in this study are shown in <xref ref-type="table" rid="T1">Table 1</xref>. Plasmid and strain construction is described in further detail in Additional File 1.</p>
<table-wrap id="T1" position="float">
<label>TABLE 1</label>
<caption>
<p>Strains used in this study.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th align="left">Strain</th>
<th align="left">Genotype</th>
<th align="left">Purpose</th>
<th align="left">References</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="left">ABF_008340</td>
<td align="left">wild-type</td>
<td align="left">Omics Data</td>
<td align="left">
<xref ref-type="bibr" rid="B16">Perlman et al. (1946)</xref>
</td>
</tr>
<tr>
<td align="left">ABF_008343</td>
<td align="left">[&#x3b2;AI-3HP]&#x2b;</td>
<td align="left">Omics Data</td>
<td align="left">
<xref ref-type="bibr" rid="B5">Dai et al. (2023)</xref>
</td>
</tr>
<tr>
<td align="left">ABF_008344</td>
<td align="left">[&#x3b2;AI-3HP]&#x2b;, aat1&#x2b;</td>
<td align="left">Omics Data</td>
<td align="left">
<xref ref-type="bibr" rid="B5">Dai et al. (2023)</xref>
</td>
</tr>
<tr>
<td align="left">ABF_008345</td>
<td align="left">[&#x3b2;AI-3HP]&#x2b;, pyc2&#x2b;</td>
<td align="left">Omics Data</td>
<td align="left">
<xref ref-type="bibr" rid="B5">Dai et al. (2023)</xref>
</td>
</tr>
<tr>
<td align="left">ABF_008346</td>
<td align="left">[&#x3b2;AI-3HP]&#x2b;&#x2b;, pyc2&#x2b;</td>
<td align="left">Omics Data</td>
<td align="left">this work</td>
</tr>
<tr>
<td align="left">ABF_008347</td>
<td align="left">[&#x3b2;AI-3HP]&#x2b;, pyc2&#x2b;, &#x394;oahA</td>
<td align="left">Omics Data</td>
<td align="left">
<xref ref-type="bibr" rid="B5">Dai et al. (2023)</xref>
</td>
</tr>
<tr>
<td align="left">ABF_008348</td>
<td align="left">[&#x3b2;AI-3HP]&#x2b;, pyc2&#x2b;, &#x394;ald6a</td>
<td align="left">Omics Data</td>
<td align="left">
<xref ref-type="bibr" rid="B5">Dai et al. (2023)</xref>
</td>
</tr>
<tr>
<td align="left">ABF_008349</td>
<td align="left">[&#x3b2;AI-3HP]&#x2b;, pyc2&#x2b;, &#x394;ald6b</td>
<td align="left">Omics Data</td>
<td align="left">
<xref ref-type="bibr" rid="B5">Dai et al. (2023)</xref>
</td>
</tr>
<tr>
<td align="left">ABF_008351</td>
<td align="left">[&#x3b2;AI-3HP]&#x2b;, pyc2&#x2b;, &#x394;uga2</td>
<td align="left">Omics Data</td>
<td align="left">
<xref ref-type="bibr" rid="B5">Dai et al. (2023)</xref>
</td>
</tr>
<tr>
<td align="left">ABF_008354</td>
<td align="left">[&#x3b2;AI-3HP]&#x2b;, pyc2&#x2b;, aat2&#x2b;</td>
<td align="left">Omics Data</td>
<td align="left">this work</td>
</tr>
<tr>
<td align="left">ABF_008355</td>
<td align="left">[&#x3b2;AI-3HP]&#x2b;&#x2b;, pyc2&#x2b;, aat2&#x2b;</td>
<td align="left">Omics Data</td>
<td align="left">this work</td>
</tr>
<tr>
<td align="left">ABF_008356</td>
<td align="left">[&#x3b2;AI-3HP]&#x2b;, pyc2&#x2b;, &#x394;ald6a, aat2&#x2b;</td>
<td align="left">Omics Data</td>
<td align="left">this work</td>
</tr>
<tr>
<td align="left">ABF_008897</td>
<td align="left">[&#x3b2;AI-3HP]&#x2b;&#x2b;, pyc2&#x2b;, mct1&#x2b;</td>
<td align="left">Omics Data</td>
<td align="left">this work</td>
</tr>
<tr>
<td align="left">ABF_008898</td>
<td align="left">[&#x3b2;AI-3HP]&#x2b;, pyc2&#x2b;, mct1&#x2b;</td>
<td align="left">Omics Data</td>
<td align="left">
<xref ref-type="bibr" rid="B5">Dai et al. (2023)</xref>
</td>
</tr>
<tr>
<td align="left">ABF_008899</td>
<td align="left">[&#x3b2;AI-3HP]&#x2b;&#x2b;, pyc2&#x2b;, &#x394;oahA</td>
<td align="left">Omics Data</td>
<td align="left">this work</td>
</tr>
<tr>
<td align="left">ABF_015658</td>
<td align="left">[&#x3b2;AI-3HP]&#x2b;&#x2b;, pyc2&#x2b;, uga2&#x2b;</td>
<td align="left">Omics Data</td>
<td align="left">this work</td>
</tr>
<tr>
<td align="left">ABF_009101</td>
<td align="left">[&#x3b2;AI-3HP]&#x2b;, pyc2&#x2b;, aat2&#x2b;</td>
<td align="left">Omics Data</td>
<td align="left">this work</td>
</tr>
<tr>
<td align="left">ABF_011231</td>
<td align="left">[&#x3b2;AI-3HP]&#x2b;, pyc2&#x2b;, &#x394;ald6a, aat2&#x2b;</td>
<td align="left">Validation</td>
<td align="left">this work</td>
</tr>
<tr>
<td align="left">ABF_011232</td>
<td align="left">[&#x3b2;AI-3HP]&#x2b;, pyc2&#x2b;, &#x394;ald6a, aat1&#x2b;</td>
<td align="left">Validation</td>
<td align="left">this work</td>
</tr>
<tr>
<td align="left">ABF_011234</td>
<td align="left">[&#x3b2;AI-3HP]&#x2b;, pyc2&#x2b;, &#x394;ald6a, mdhA&#x2b;</td>
<td align="left">Validation</td>
<td align="left">this work</td>
</tr>
<tr>
<td align="left">ABF_011236</td>
<td align="left">[&#x3b2;AI-3HP]&#x2b;, pyc2&#x2b;, &#x394;ald6a, purU&#x2b;</td>
<td align="left">Validation</td>
<td align="left">this work</td>
</tr>
<tr>
<td align="left">ABF_011233</td>
<td align="left">[&#x3b2;AI-3HP]&#x2b;, pyc2&#x2b;, &#x394;ald6a, pyc2&#x2b;</td>
<td align="left">Validation</td>
<td align="left">this work</td>
</tr>
<tr>
<td align="left">ABF_011239</td>
<td align="left">[&#x3b2;AI-3HP]&#x2b;, pyc2&#x2b;, &#x394;ald6a, &#x394;adhD</td>
<td align="left">Validation</td>
<td align="left">this work</td>
</tr>
<tr>
<td align="left">ABF_011240</td>
<td align="left">[&#x3b2;AI-3HP]&#x2b;, pyc2&#x2b;, &#x394;ald6a, &#x394;iscA</td>
<td align="left">Validation</td>
<td align="left">this work</td>
</tr>
<tr>
<td align="left">ABF_011241</td>
<td align="left">[&#x3b2;AI-3HP]&#x2b;, pyc2&#x2b;, &#x394;ald6a, &#x394;iscB</td>
<td align="left">Validation</td>
<td align="left">this work</td>
</tr>
</tbody>
</table>
</table-wrap>
</sec>
<sec id="s2-3">
<label>2.3</label>
<title>Metabolome and proteome analysis</title>
<p>For quantification of extracellular metabolites in the spent medium samples were analyzed using high performance liquid chromatography (HPLC) equipped with a Waters 2,414 refractive index detector. A Bio-Rad Aminex HPX-87H ion exclusion column (300&#xa0;mm &#xd7; 7.8&#xa0;mm), heated to 65C was used for analyte separation. Sulfuric acid (0.0045&#xa0;M) was used as eluent at a flow rate of 0.55&#xa0;mL/min. Intracellular metabolite extracts were completely dried under vacuum to remove moisture and chemically derivatized. Briefly, the extracted metabolites were derivatized by methoxyamination and trimethylsilyation (TMS), then the samples were analyzed by GC-MS. Sample preparation, instrument acquisition and data analysis was performed as previously reported (<xref ref-type="bibr" rid="B17">Pomraning et al., 2021</xref>; <xref ref-type="bibr" rid="B10">Kim et al., 2015</xref>). Global and targeted proteomics was performed as in previously established LC-MS/MS methods and data analysis workflows (<xref ref-type="bibr" rid="B17">Pomraning et al., 2021</xref>), except slight adjustments to the mass spectrometry acquisition settings in global proteomics. In global proteomics, peptide digests were analyzed using a Q Exactive Plus mass spectrometer (Thermo Fisher Scientific) in data-dependent acquisition mode. Mass spectrometer settings were as following: full MS (AGC, 3 &#xd7; 10<sup>6</sup>; resolution, 70,000; m/z range, 300&#x2013;1800; maximum ion time, 20&#xa0;m); MS/MS (AGC, 1 &#xd7; 10<sup>5</sup>; resolution, 17,500; m/z range, 200&#x2013;2000; maximum ion time, 50&#xa0;m; TopN, 12; isolation width, 1.5 Da; dynamic exclusion, 30.0 s; collision energy, NCE 30).</p>
</sec>
<sec id="s2-4">
<label>2.4</label>
<title>Bayesian inference for kinetic parameter estimation</title>
<p>BMCA was performed following established protocols (<xref ref-type="bibr" rid="B14">McNaughton et al., 2021</xref>; <xref ref-type="bibr" rid="B18">St John et al., 2019</xref>). A reduced metabolic model of <italic>A. niger</italic> was constructed by integrating the central metabolism of iJB1325 (<xref ref-type="bibr" rid="B3">Brandl et al., 2018</xref>) and beta-alanine pathway for 3-HP production and removing reactions with zero flux at the reference state. The resulting model comprised 172 reactions and 171 metabolites. Proteomics and metabolomics measurements from 51 samples representing 17 distinct strains were used as the observed data. Strain-specific uptake and excretion rates were calculated for measured extracellular metabolites. These rates were further used to calculate internal fluxes with global proteomics as constraints with a proton export objective using E-Flux2 (<xref ref-type="bibr" rid="B11">Kim et al., 2016</xref>). At steady state, the metabolic reaction rate (<inline-formula id="inf1">
<mml:math id="m1">
<mml:mrow>
<mml:mi>v</mml:mi>
</mml:mrow>
</mml:math>
</inline-formula>) can be expressed as a function of enzyme concentrations (<inline-formula id="inf2">
<mml:math id="m2">
<mml:mrow>
<mml:mi>e</mml:mi>
</mml:mrow>
</mml:math>
</inline-formula>), internal and external metabolite concentrations (<inline-formula id="inf3">
<mml:math id="m3">
<mml:mrow>
<mml:mi>x</mml:mi>
</mml:mrow>
</mml:math>
</inline-formula> and <inline-formula id="inf4">
<mml:math id="m4">
<mml:mrow>
<mml:mi>y</mml:mi>
</mml:mrow>
</mml:math>
</inline-formula>) as follows:<disp-formula id="equ1">
<mml:math id="m5">
<mml:mrow>
<mml:mi>v</mml:mi>
<mml:mo>&#x3d;</mml:mo>
<mml:mtext>diag</mml:mtext>
<mml:mrow>
<mml:mfenced open="(" close=")" separators="|">
<mml:mrow>
<mml:msup>
<mml:mi>v</mml:mi>
<mml:mo>&#x2a;</mml:mo>
</mml:msup>
<mml:mfrac>
<mml:mrow>
<mml:mi>e</mml:mi>
</mml:mrow>
<mml:mrow>
<mml:msup>
<mml:mi>e</mml:mi>
<mml:mo>&#x2a;</mml:mo>
</mml:msup>
</mml:mrow>
</mml:mfrac>
</mml:mrow>
</mml:mfenced>
</mml:mrow>
<mml:mrow>
<mml:mfenced open="(" close=")" separators="|">
<mml:mrow>
<mml:msub>
<mml:mn>1</mml:mn>
<mml:mi>n</mml:mi>
</mml:msub>
<mml:mo>&#x2b;</mml:mo>
<mml:msubsup>
<mml:mi>&#x3b5;</mml:mi>
<mml:mi>x</mml:mi>
<mml:mo>&#x2a;</mml:mo>
</mml:msubsup>
<mml:mo>&#x2061;</mml:mo>
<mml:mi>log</mml:mi>
<mml:mfrac>
<mml:mrow>
<mml:mi>x</mml:mi>
</mml:mrow>
<mml:mrow>
<mml:msup>
<mml:mi>x</mml:mi>
<mml:mo>&#x2a;</mml:mo>
</mml:msup>
</mml:mrow>
</mml:mfrac>
<mml:mo>&#x2b;</mml:mo>
<mml:msubsup>
<mml:mi>&#x3b5;</mml:mi>
<mml:mi>y</mml:mi>
<mml:mo>&#x2a;</mml:mo>
</mml:msubsup>
<mml:mo>&#x2061;</mml:mo>
<mml:mi mathvariant="italic">log</mml:mi>
<mml:mfrac>
<mml:mrow>
<mml:mi>y</mml:mi>
</mml:mrow>
<mml:mrow>
<mml:msup>
<mml:mi>y</mml:mi>
<mml:mo>&#x2a;</mml:mo>
</mml:msup>
</mml:mrow>
</mml:mfrac>
</mml:mrow>
</mml:mfenced>
</mml:mrow>
</mml:mrow>
</mml:math>
</disp-formula>where the asterisks (<inline-formula id="inf5">
<mml:math id="m6">
<mml:mrow>
<mml:mo>&#x2a;</mml:mo>
</mml:mrow>
</mml:math>
</inline-formula>) denote quantities at a defined reference state, <inline-formula id="inf6">
<mml:math id="m7">
<mml:mrow>
<mml:msubsup>
<mml:mi>&#x3b5;</mml:mi>
<mml:mi>x</mml:mi>
<mml:mo>&#x2a;</mml:mo>
</mml:msubsup>
</mml:mrow>
</mml:math>
</inline-formula> and <inline-formula id="inf7">
<mml:math id="m8">
<mml:mrow>
<mml:msubsup>
<mml:mi>&#x3b5;</mml:mi>
<mml:mi>y</mml:mi>
<mml:mo>&#x2a;</mml:mo>
</mml:msubsup>
</mml:mrow>
</mml:math>
</inline-formula> are kinetic parameters called metabolite elasticity matrixes, which respectively quantify the sensitivity of reaction rates to changes in internal and external metabolite concentrations. This lin-log approximation is valid near the reference state and enables efficient parameter estimation (<xref ref-type="bibr" rid="B18">St John et al., 2019</xref>).</p>
<p>Posterior distributions of the model parameters were inferred using automatic differentiation variational inference (ADVI), as implemented in the PyMC3 Python library. The model was optimized using the Adagrad optimizer until convergence of the negative evidence lower bound score. Using the resulting parameterized kinetic model, we computed flux control coefficients (FCCs), which quantify the sensitivity of steady-state fluxes to perturbations in enzyme levels at the reference state. FCCs were considered significantly different from zero if their 95% highest posterior density intervals from the posterior distribution do not overlap with zero. Github repositories for the <italic>Aspergillus</italic>-specific analysis are available at <ext-link ext-link-type="uri" xlink:href="https://github.com/agilebiofoundry/aspergillusq4milestone">https://github.com/agilebiofoundry/aspergillusq4milestone</ext-link> and for the BMCA at <ext-link ext-link-type="uri" xlink:href="https://github.com/agilebiofoundry/bayesian-metabolic-control-analysis">https://github.com/agilebiofoundry/bayesian-metabolic-control-analysis</ext-link>.</p>
</sec>
</sec>
<sec sec-type="results" id="s3">
<label>3</label>
<title>Results</title>
<sec id="s3-1">
<label>3.1</label>
<title>Multi-omic analysis of <italic>Aspergillus niger</italic> strains engineered to produce 3-HP</title>
<p>Metabolomic and Proteomic analysis was conducted to identify reactions controlling flux in <italic>A</italic>. <italic>niger</italic> strains engineered to produce 3-HP. Strains were constructed or selected from a previous studies (<xref ref-type="bibr" rid="B5">Dai et al., 2023</xref>) to perturb flux through the beta-alanine 3-HP biosynthetic pathway enabled by overexpression of three heterologous enzymes, <italic>Tc</italic>PAND, <italic>Bc</italic>BAPAT, and <italic>Ec</italic>HPDH (<xref ref-type="bibr" rid="B2">Borodina et al., 2015</xref>). Previously identified genetic targets including <italic>oahA</italic>, <italic>uga2</italic>, <italic>ald6a</italic>, <italic>ald6b</italic>, <italic>pyc1</italic>, <italic>aat1</italic>, <italic>mct1</italic>, and the heterologous beta-alanine pathway genes (<xref ref-type="bibr" rid="B5">Dai et al., 2023</xref>; <xref ref-type="bibr" rid="B17">Pomraning et al., 2021</xref>) were disrupted and overexpressed to establish a dataset spanning a wide range of 3-HP productivity levels amenable to learn from (<xref ref-type="table" rid="T1">Table 1</xref>). All strains were cultivated in mRDM for 7&#xa0;days with extracellular metabolites and biomass collected at days 3, 5, and 7 to provide boundary constraints for flux balance analysis (<xref ref-type="fig" rid="F1">Figure 1</xref>). Cell pellets collected on day 5 were extracted using MPLEx (<xref ref-type="bibr" rid="B15">Nakayasu et al., 2016</xref>) for mass-spec based multi-omics assays. Data from 17 strains in triplicate was collected for 55 intracellular metabolites (<xref ref-type="bibr" rid="B9">Kim and Heyman, 2018</xref>) and 3,814 proteins using global untargeted methods and 59 proteins selected for quantitatively precise measurement by selected reaction monitoring (SRM) based targeted proteomics (<xref ref-type="bibr" rid="B6">Gao et al., 2020</xref>) (Additional file 2).</p>
<fig id="F1" position="float">
<label>FIGURE 1</label>
<caption>
<p>Metabolic analysis of 3-HP production in <italic>Aspergillus niger</italic>. <bold>(A)</bold> Time-series production of 3-HP from glucose in diverse strains. <bold>(B)</bold> Samples for multi-omics analysis were collected in triplicate on day 5 and metabolic fluxes predicted with consumption, production, and growth as constraints. Abbreviations: &#x03B2;Ala-3HP, beta-alanine heterologous pathway consisting of <italic>Tc</italic>PAND, <italic>Bc</italic>BAPAT, and <italic>Ec</italic>HPDH; AAT1, aspartate aminotransferase; ALD6, malonic semialdehyde dehydrogenase; <italic>Bc</italic>BAPAT, beta-alanine pyruvate aminotransferase; <italic>Ec</italic>HPDH, 3-hydroxypropanoate dehydrogenase; MCT1, monocarboxylate transporter; OAHA, oxaloacetate hydrolase; PYC2, pyruvate carboxylase; UGA2, succinate semialdehyde dehydrogenase; <italic>Tc</italic>PAND, aspartate decarboxylase.</p>
</caption>
<graphic xlink:href="fbioe-14-1754875-g001.tif">
<alt-text content-type="machine-generated">Panel A displays two heatmaps showing glucose consumption and 3-hydroxypropionic acid (3-HP) production over days three, five, and seven for various yeast genotypes. Panel B presents four three-dimensional scatter plots depicting global proteomics, targeted proteomics, intracellular metabolomics, and predicted metabolic fluxes, with each point representing a sample colored by genotype or condition.</alt-text>
</graphic>
</fig>
<p>Intracellular reactions fluxes were predicted using a reduced metabolic model (172 reactions, 171 metabolites) adapted from a genome-scale metabolic model of <italic>A. niger</italic> (<xref ref-type="bibr" rid="B3">Brandl et al., 2018</xref>) that contained only non-zero fluxes at the reference state. The spent media, time, and biomass at collection were used to construct a simple exponential growth model of the organism and estimate strain-specific uptake and excretion rates for key measured extracellular metabolites. These rates were further used to calculate internal fluxes with global proteomics as constraints using E-Flux2 (<xref ref-type="bibr" rid="B11">Kim et al., 2016</xref>).</p>
</sec>
<sec id="s3-2">
<label>3.2</label>
<title>Bayesian metabolic control analysis to predict reactions controlling metabolic flux</title>
<p>We next employed the BMCA methodology developed to predict how cellular kinetics respond to genetic changes (<xref ref-type="bibr" rid="B14">McNaughton et al., 2021</xref>; <xref ref-type="bibr" rid="B18">St John et al., 2019</xref>). In BMCA, a low-fidelity kinetic model of microbial metabolism is constructed leveraging linear-logarithmic kinetics. With known kinetic parameters, a kinetic model enables the expected steady-state internal metabolite concentrations and metabolic fluxes to be estimated as a function of enzyme expression and media conditions. With measurements of both the input variables (extracellular metabolite concentrations and enzyme expression) and the output variables (steady-state fluxes and internal metabolite concentrations), posterior distributions in the kinetic parameters that are consistent with the observed data can then be estimated.</p>
<p>Due to the size of the kinetic model considered, posterior distributions in kinetic parameters as a function of the observed data was estimated using automatic differentiation variational inference as implemented in the PyMC3 Python library. The model was optimized until convergence of the evidence lower bound score using the Adagrad optimizer. The posterior predictive distribution (PPD) of the model shows the ability of the model to reproduce the measured experimental data across different strains. The PPD of the fitted model closely reproduces the measured targeted proteomics, metabolite concentrations, and global proteomics-based Eflux2-predicted intracellular fluxes within the unclipped shaded region (<xref ref-type="fig" rid="F2">Figure 2A</xref>). Outside this region, predicted metabolomics, proteins and fluxes were based on clipped measurements, hence the horizontal cluster of sample points.</p>
<fig id="F2" position="float">
<label>FIGURE 2</label>
<caption>
<p>Bayesian metabolic control analysis. <bold>(A)</bold> Posterior predictive distribution of the fitted model. The metabolomics (left), intracellular and extracellular fluxes (center) and proteomics (right) closely match the experimentally measured values. Fluxes are in units of mmol/gDCW&#x2a;hr, while metabolomics and proteomics data are in log-transformed, dimensionless units relative to the reference strain. Shaded boxes indicate the unclipped region where measured data is near the reference state. <bold>(B)</bold> Posterior distributions in 3-HP flux control coefficients (FCC). The dotted lines are provided as a qualitative aid for selecting candidate targets. FCC&#x2019;s whose credible interval crosses the dashed line are not considered a target. <bold>(C)</bold> Gene included in multi-omics analysis dataset (perturbed) and with significant FCCs (predicted). Abbreviations: 10-FTH, 10-formyltetrahydrofolate; 3HP, 3-hydroxyproptionic acid; ACAL, acetaldehyde; AKG, alpha-ketoglutarate; ACCA, acetyl-CoA; ALA, alanine; ASP, aspartate; BAL, beta-alanine; ETOH, ethanol; FMT, formate; GABA, gamma-aminobutyrate; GLC, glucose; GLU, Glutamate; MAL, malate; MSA, malonic semialdehyde; OAA, oxaloacetate; OXA, oxalate; PYR, pyruvate; SUC, succinate; SUCA, succinyl-CoA; SUCS, succinate semialdehyde.</p>
</caption>
<graphic xlink:href="fbioe-14-1754875-g002.tif">
<alt-text content-type="machine-generated">Panel A displays histograms and scatter plots comparing measured versus predicted values for metabolomics, fluxomics, and proteomics datasets. Panel B presents a dot plot of FCC values for gene deletions and overexpressions, showing error bars and a marked division between conditions. Panel C is a metabolic pathway diagram separated into extracellular, cytosolic, and mitochondrial compartments, illustrating carbon metabolism with highlighted reactions for perturbed (orange) and predicted (green) states, and various transporters and metabolites labeled throughout.</alt-text>
</graphic>
</fig>
<p>With a kinetic model and estimated probability distributions in kinetic parameters, we then conducted the Metabolic Control Analysis portion of the BMCA framework. Here, the uncertainty in the estimated kinetic parameters is propagated to the metabolic design strategies suggested by Metabolic Control Analysis. In <xref ref-type="fig" rid="F2">Figure 2B</xref>, we show a subset of the highest posterior density regions of flux control coefficients (FCCs) on 3-HP export calculated from the posterior distribution. A positive FCC indicates that an increase in the corresponding enzyme concentration will increase 3-HP flux, while a negative FCC indicates that a decrease in enzyme concentration will increase 3-HP flux, thus FCCs capture the systems-level regulation of changing enzyme concentration on steady-state metabolic flux.</p>
</sec>
<sec id="s3-3">
<label>3.3</label>
<title>Validation of reaction targets with metabolic engineering to increase 3-HP production</title>
<p>To evaluate use of the BMCA framework as a predictive modeling tool for synthetic biology applications we selected reactions to modify based on their associated FCC in the training data. We predicted that reactions with negative FCCs will increase flux through the 3-HP pathway when downregulated or deleted and reactions with positive FCCs will increase flux through the 3-HP pathway when enzymes associated with the reaction are over-expressed (<xref ref-type="fig" rid="F2">Figure 2</xref>). The largest positive flux control coefficients include plasmas membrane nitrate transport (r1086, ProteinID 1189116), 5-formyltetrahydrofolate deformylase (r95, ProteinID 1182700), malate dehydrogenase (r44, ProteinID 1144118), pyruvate carboxylase (r19, ProteinID 1031996), and mitochondrial aspartate aminotransferase (r258&#xa0;m, ProteinID 1184650). The most negative FCC&#x2019;s include the putative reaction catalyzed by ALD6 (malonate semialdehyde &#x2b; CoA &#x2b; NAD(P)<sup>&#x2b;</sup> &#x2192; Acetyl-CoA &#x2b; CO<sub>2</sub> &#x2b; NAD(P)H, ProteinID 1182225) (<xref ref-type="bibr" rid="B5">Dai et al., 2023</xref>; <xref ref-type="bibr" rid="B17">Pomraning et al., 2021</xref>), mitochondrial alcohol dehydrogenase (r118a, ProteinID 1145368) and succinyl-CoA ligase (r38a, ProteinIDs 1145655 and 1141712).</p>
<p>We sought to delete or overexpress each predicted gene target in the highest performing 3-HP strain evaluated in the training set (strain ABF_008348). This strain has a preexisting <italic>ald</italic>6a disruption, the most strongly suggested deletion target, which we previously defined as a critical modification in 3-HP producing <italic>Aspergilli</italic> as well as <italic>Rhodosporidium toruloides</italic> (<xref ref-type="bibr" rid="B5">Dai et al., 2023</xref>; <xref ref-type="bibr" rid="B17">Pomraning et al., 2021</xref>; <xref ref-type="bibr" rid="B13">Liu et al., 2023</xref>). To evaluate alcohol dehydrogenase we selected a high-quality mitochondrial target, <italic>adh</italic>D (Protein ID 1145368) and assessed both subunits of the succinyl-CoA ligase enzyme. All the single gene overexpression targets were selected for evaluation except plasma membrane transport of nitrate as we had previously established that increasing the concentration of extracellular nitrogen promotes significantly higher yield and titer of 3-HP (<xref ref-type="bibr" rid="B5">Dai et al., 2023</xref>). Overexpression of mitochondrial aspartate aminotransferase AAT1 unexpectedly dramatically reduced 3-HP productivity, however, overexpression of a cytosolic variant (AAT2; ProteinID 1176455) improved both titer and yield of 3-HP. In total, six reactions with significant FCCs were evaluated for their impact on flux toward 3-HP. Predicted directional perturbation of five of the six reactions significantly improved titer and rate of 3-HP production and two significantly improved yield (<xref ref-type="fig" rid="F3">Figure 3</xref>). Notably, disruption of the nonintuitive target succinyl-CoA ligase resulted in a 39% increase in titer (14.7&#x2013;20.4&#xa0;g/L 3-HP) and 29% increase in yield (0.24&#x2013;0.31&#xa0;g 3-HP/g glucose), highlighting the ability to predict meaningful genetic targets in unexpected areas of metabolism by integrating systems-level proteome and metabolome data with metabolic modeling and flux-omics.</p>
<fig id="F3" position="float">
<label>FIGURE 3</label>
<caption>
<p>Validation of flux control predictions by genetic intervention. <bold>(A)</bold> 3-HP titer and yield metrics from glucose after 7&#xa0;days of cultivation in selected transformants of high performing parent strain ABF_008348 (n &#x3d; 3). Asterisks indicate significant improvements (p &#x3c; 0.05). <bold>(B)</bold> 3-HP titer and yield in the training data and in strains produced to test for improvements in 3-HP production. The parent strain ABF_008348 used for testing is indicated as darkened squares in each dataset. Abbreviations: 3-HP, 3-hydroxyproptionic acid; aat1/2, aspartate aminotransferase; adhD, alcohol dehydrogenase; ald6, malonic semialdehyde dehydrogenase; iscA/B, succinyl-CoA ligase; mdhA, malate dehydrogenase; purU, 5-formyltetrahydrofolate deformylase; pyc2, pyruvate carboxylase.</p>
</caption>
<graphic xlink:href="fbioe-14-1754875-g003.tif">
<alt-text content-type="machine-generated">Panel A presents two bar charts showing 3-HP titers and yields for genetic modifications compared to parent strain, with several modifications significantly increasing both metrics. Panel B displays a scatterplot comparing predicted genetic improvements and training data, plotting 3-HP titers versus yield with error bars for each point.</alt-text>
</graphic>
</fig>
</sec>
</sec>
<sec sec-type="discussion" id="s4">
<label>4</label>
<title>Discussion</title>
<p>In conclusion, we developed the computational infrastructure to deploy BMCA to enable integration of systems-level multi-omics datasets with prior knowledge in the form of a genome-scale metabolic model, and metabolic flux predictions constrained by growth, consumption, and production rates. This approach enables the generation of small numbers of high-quality predictions to improve metabolic flux in organisms engineered to produce biochemicals at high yield. BMCA also requires less data collection than machine learning approaches due to the integration of a mechanistic model (<xref ref-type="bibr" rid="B24">Shin et al., 2026</xref>). While machine learning and artificial intelligence may expediate development of model microbes amenable to high-throughput genetic manipulation and rapid data-sparse phenotyping, data-rich approaches that globally characterize engineered microbes are needed for industrial hosts that are limited by genetic engineering or phenotyping rates, particularly when assessing bioprocesses at industrially relevant scales where even modest throughput is impractical.</p>
</sec>
</body>
<back>
<sec sec-type="data-availability" 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="s11">Supplementary Material</xref>, further inquiries can be directed to the corresponding author.</p>
</sec>
<sec sec-type="author-contributions" id="s6">
<title>Author contributions</title>
<p>ZD: Conceptualization, Investigation, Writing &#x2013; original draft, Writing &#x2013; review and editing. JZ: Conceptualization, Investigation, Writing &#x2013; original draft, Writing &#x2013; review and editing. YH: Investigation, Writing &#x2013; review and editing. SM: Investigation, Writing &#x2013; review and editing. JC: Investigation, Writing &#x2013; review and editing. NM: Investigation, Writing &#x2013; review and editing. YG: Investigation, Writing &#x2013; review and editing. GY: Investigation, Writing &#x2013; review and editing. BH: Investigation, Writing &#x2013; review and editing. JM: Conceptualization, Funding acquisition, Writing &#x2013; review and editing. JK: Conceptualization, Investigation, Writing &#x2013; review and editing. Y-MK: Conceptualization, Investigation, Writing &#x2013; review and editing. KB-J: Conceptualization, Writing &#x2013; review and editing. KP: Conceptualization, Funding acquisition, Investigation, Writing &#x2013; original draft, Writing &#x2013; review and editing.</p>
</sec>
<sec sec-type="COI-statement" id="s8">
<title>Conflict of interest</title>
<p>The author(s) declared that this work 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="ai-statement" id="s9">
<title>Generative AI statement</title>
<p>The author(s) declared that generative AI was not 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="s10">
<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 sec-type="supplementary-material" id="s11">
<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/fbioe.2026.1754875/full#supplementary-material">https://www.frontiersin.org/articles/10.3389/fbioe.2026.1754875/full&#x23;supplementary-material</ext-link>
</p>
<supplementary-material xlink:href="DataSheet1.pdf" id="SM1" mimetype="application/pdf" xmlns:xlink="http://www.w3.org/1999/xlink"/>
<supplementary-material xlink:href="Table1.xlsx" id="SM2" mimetype="application/xlsx" xmlns:xlink="http://www.w3.org/1999/xlink"/>
</sec>
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<ext-link ext-link-type="uri" xlink:href="https://loop.frontiersin.org/people/3316995/overview">Blaise Manga Enuh</ext-link>, University of Wisconsin-Madison, United States</p>
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