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<front>
<journal-meta>
<journal-id journal-id-type="publisher-id">Front. Mater.</journal-id>
<journal-title>Frontiers in Materials</journal-title>
<abbrev-journal-title abbrev-type="pubmed">Front. Mater.</abbrev-journal-title>
<issn pub-type="epub">2296-8016</issn>
<publisher>
<publisher-name>Frontiers Media S.A.</publisher-name>
</publisher>
</journal-meta>
<article-meta>
<article-id pub-id-type="publisher-id">1407655</article-id>
<article-id pub-id-type="doi">10.3389/fmats.2024.1407655</article-id>
<article-categories>
<subj-group subj-group-type="heading">
<subject>Materials</subject>
<subj-group>
<subject>Original Research</subject>
</subj-group>
</subj-group>
</article-categories>
<title-group>
<article-title>Prevention of severe pitting corrosion of 13Cr pipeline steel by a sulfate reducing bacterium using a green biocide cocktail</article-title>
<alt-title alt-title-type="left-running-head">Xu 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/fmats.2024.1407655">10.3389/fmats.2024.1407655</ext-link>
</alt-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname>Xu</surname>
<given-names>Lingjun</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
</xref>
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<contrib contrib-type="author">
<name>
<surname>Khan</surname>
<given-names>Adnan</given-names>
</name>
<xref ref-type="aff" rid="aff2">
<sup>2</sup>
</xref>
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<contrib contrib-type="author">
<name>
<surname>Kijkla</surname>
<given-names>Pruch</given-names>
</name>
<xref ref-type="aff" rid="aff3">
<sup>3</sup>
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<contrib contrib-type="author">
<name>
<surname>Kumseranee</surname>
<given-names>Sith</given-names>
</name>
<xref ref-type="aff" rid="aff3">
<sup>3</sup>
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<contrib contrib-type="author">
<name>
<surname>Punpruk</surname>
<given-names>Suchada</given-names>
</name>
<xref ref-type="aff" rid="aff3">
<sup>3</sup>
</xref>
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<contrib contrib-type="author" corresp="yes">
<name>
<surname>Gu</surname>
<given-names>Tingyue</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
</xref>
<xref ref-type="aff" rid="aff2">
<sup>2</sup>
</xref>
<xref ref-type="corresp" rid="c001">&#x2a;</xref>
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<aff id="aff1">
<sup>1</sup>
<institution>Department of Chemical and Biomolecular Engineering</institution>, <institution>Institute for Corrosion and Multiphase Technology</institution>, <institution>Ohio University</institution>, <addr-line>Athens</addr-line>, <addr-line>OH</addr-line>, <country>United States</country>
</aff>
<aff id="aff2">
<sup>2</sup>
<institution>Department of Biological Sciences</institution>, <institution>Molecular and Cellular Biology Program</institution>, <institution>Ohio University</institution>, <addr-line>Athens</addr-line>, <addr-line>OH</addr-line>, <country>United States</country>
</aff>
<aff id="aff3">
<sup>3</sup>
<institution>PTT Exploration and Production</institution>, <addr-line>Bangkok</addr-line>, <country>Thailand</country>
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<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/1954834/overview">Wenwen Dou</ext-link>, Shandong University, China</p>
</fn>
<fn fn-type="edited-by">
<p>
<bold>Reviewed by:</bold> <ext-link ext-link-type="uri" xlink:href="https://loop.frontiersin.org/people/1554752/overview">Weichen Xu</ext-link>, Chinese Academy of Sciences (CAS), China</p>
<p>
<ext-link ext-link-type="uri" xlink:href="https://loop.frontiersin.org/people/2631763/overview">Enze Zhou</ext-link>, Northeastern University, China</p>
</fn>
<corresp id="c001">&#x2a;Correspondence: Tingyue Gu, <email>gu@ohio.edu</email>
</corresp>
</author-notes>
<pub-date pub-type="epub">
<day>30</day>
<month>05</month>
<year>2024</year>
</pub-date>
<pub-date pub-type="collection">
<year>2024</year>
</pub-date>
<volume>11</volume>
<elocation-id>1407655</elocation-id>
<history>
<date date-type="received">
<day>27</day>
<month>03</month>
<year>2024</year>
</date>
<date date-type="accepted">
<day>10</day>
<month>05</month>
<year>2024</year>
</date>
</history>
<permissions>
<copyright-statement>Copyright &#xa9; 2024 Xu, Khan, Kijkla, Kumseranee, Punpruk and Gu.</copyright-statement>
<copyright-year>2024</copyright-year>
<copyright-holder>Xu, Khan, Kijkla, Kumseranee, Punpruk and Gu</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>To combat abiotic CO<sub>2</sub> corrosion of pipelines, chromium steels (CrSs) are used to replace carbon steels, but CrSs can suffer very severe pitting corrosion caused by microbiologically influenced corrosion (MIC) because their passive films are not as good as those on high-grade stainless steels, and their MIC often involves (semi-)conductive corrosion product films. In this study, severe pitting corrosion (2.0 cm/a pitting corrosion rate) with a 7-day weight loss of 3.8 &#xb1; 0.5 mg/cm<sup>2</sup> (0.26 mm/a uniform corrosion rate) was observed on 13Cr coupons incubated anaerobically with a highly corrosive pure-strain sulfate reducing bacterium (SRB) <italic>Desulfovibrio ferrophilus</italic> IS5 in 125 mL anaerobic vials filled with 50 mL enriched artificial seawater at 28&#xb0;C. A popular green biocide, namely tetrakis hydroxymethyl phosphonium sulfate (THPS), was enhanced by biofilm dispersing Peptide A (a 14-mer) to mitigate SRB MIC against 13Cr. The 7-day weight losses for coupons with 50 ppm (w/w) THPS, 50 ppm THPS &#x2b; 100 nM (180 ppb) Peptide A and 100 ppm THPS were reduced to 2.2 &#xb1; 0.2 mg/cm<sup>2</sup>, 1.5 &#xb1; 0.5 mg/cm<sup>2</sup>, and 0.3 &#xb1; 0.2 mg/cm<sup>2</sup>, respectively. The pitting rates also decreased from 20 mm/a to 12 mm/a, 8.6 mm/a, and 1.5 mm/a, respectively based on the maximum pit depth data for the 7-day incubation. Electrochemical tests using a miniature electrochemical glass cell design supported the weight loss trend with additional transient corrosion rate information. THPS was found to be effective in mitigating severe pitting corrosion on 13Cr, and the enhancement effect of Peptide A for THPS was manifested. This work has significant implications in field applications when CrSs are considered as metal choices to replace carbon steels to combat abiotic CO<sub>2</sub> corrosion in pipelines. When SRB MIC is a possible threat, a mitigation plan needs to be implemented to prevent potentially very severe pitting that can lead to pinhole leaks.</p>
</abstract>
<kwd-group>
<kwd>microbiologically influenced corrosion</kwd>
<kwd>sulfate reducing bacterium</kwd>
<kwd>13Cr</kwd>
<kwd>pitting corrosion</kwd>
<kwd>biocide mitigation</kwd>
</kwd-group>
<custom-meta-wrap>
<custom-meta>
<meta-name>section-at-acceptance</meta-name>
<meta-value>Environmental Degradation of Materials</meta-value>
</custom-meta>
</custom-meta-wrap>
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</front>
<body>
<sec id="s1">
<title>1 Introduction</title>
<p>It is known that microbiologically influenced corrosion (MIC) is a serious menace to various assets in the oil and gas industry (D. <xref ref-type="bibr" rid="B56">Xu et al., 2023</xref>; <xref ref-type="bibr" rid="B60">Yazdi et al., 2021</xref>). It has been reported to be responsible for nearly 20% of the total corrosion costs (<xref ref-type="bibr" rid="B28">Kermani and Harrop, 1996</xref>; <xref ref-type="bibr" rid="B43">Skovhus et al., 2017</xref>). Different types of microorganisms including bacteria, archaea, fungi, and microalgae have been documented to cause deterioration of various metals directly and indirectly (<xref ref-type="bibr" rid="B10">Chugh et al., 2020</xref>; <xref ref-type="bibr" rid="B17">El-Shamy, 2020</xref>; <xref ref-type="bibr" rid="B61">You et al., 2021</xref>). Sulfate reducing bacteria (SRB) have been extensively studied in MIC research since they are ubiquitous in the environment, especially anaerobic environment, and very aggressive to metals (<xref ref-type="bibr" rid="B48">Videla and Characklis, 1992</xref>; <xref ref-type="bibr" rid="B38">Sand and Gehrke, 2003</xref>; <xref ref-type="bibr" rid="B3">Abdullah et al., 2014</xref>; <xref ref-type="bibr" rid="B18">Enning and Garrelfs, 2014</xref>; <xref ref-type="bibr" rid="B59">Yang et al., 2020</xref>). They typically utilize sulfate as the terminal electron acceptors through the respiration process to obtain energy from organic compounds or H<sub>2</sub> (<xref ref-type="bibr" rid="B8">&#x10c;ernou&#x161;ek et al., 2020</xref>). The corrosion mechanisms of SRB are mainly categorized into extracellular electron transfer-MIC (EET-MIC) and metabolite-MIC (M-MIC) (<xref ref-type="bibr" rid="B52">Wang et al., 2020</xref>; <xref ref-type="bibr" rid="B36">Pu et al., 2023</xref>).</p>
<p>EET-MIC occurs when a metal such as Fe<sup>0</sup> is energetic enough to serve as the electron donor for sulfate reduction. During this process, electrons released from iron oxidation Eq. <xref ref-type="disp-formula" rid="e1">1</xref> are transported across cell walls and finally used for enzyme-catalyzed sulfate reduction Eq. <xref ref-type="disp-formula" rid="e2">2</xref> to in the SRB cytoplasm (<xref ref-type="bibr" rid="B24">Gu et al., 2019</xref>).<disp-formula id="e1">
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<p>The apostrophe in <italic>E</italic>&#xb0;&#x2019; indicates pH 7 physiological condition in bioenergetics (<xref ref-type="bibr" rid="B46">Thauer et al., 2007</xref>). Another major type of MIC happens to metals (e.g., Cu) that are not energetic enough to donate electrons to facilitate sulfate reduction. In this case, M-MIC is the mechanism for SRB MIC of Cu.<disp-formula id="e3">
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<p>Due to the extremely low solubility of Cu<sub>2</sub>S, the reaction in Eq. <xref ref-type="disp-formula" rid="e3">3</xref> has a rather negative Gibbs free energy change. This corrosion reaction is thermodynamically favorable and H<sup>&#x2b;</sup> becomes a feasible electron acceptor in M-MIC (<xref ref-type="bibr" rid="B7">Blais et al., 2008</xref>; <xref ref-type="bibr" rid="B24">Gu et al., 2019</xref>).</p>
<p>Active metals such as Al and Zn can be easily corroded by water hydrolysis when their oxide passive films are damaged. These mineral films can be damaged by biofilms which lead to FD-MIC (film-damage MIC) (<xref ref-type="bibr" rid="B47">Unsal et al., 2021</xref>).</p>
<p>SRB MIC of metals containing Fe<sup>0</sup> is known to be EET-MIC because it can be accelerated by an electron mediator such as riboflavin and conductive magnetite nanoparticles (MNPs) (<xref ref-type="bibr" rid="B53">Wang et al., 2022b</xref>). Furthermore, starved sessile cells were found to be far more corrosive (<xref ref-type="bibr" rid="B55">Xu and Gu, 2014</xref>). In EET-MIC, more sessile cells harvest more electrons to harvest energy in their respiration (<xref ref-type="bibr" rid="B26">Jia et al., 2018</xref>). Thus, mitigation of EET-MIC needs to reduce the sessile cell count.</p>
<p>Different materials such as carbon steels (CSs), chromium steels (CrSs) and stainless steels (SSs) are used in the oil and gas industry (<xref ref-type="bibr" rid="B25">Hinds et al., 2005</xref>; <xref ref-type="bibr" rid="B30">Mesquita et al., 2014</xref>; <xref ref-type="bibr" rid="B33">Obot et al., 2020</xref>; <xref ref-type="bibr" rid="B12">Costa et al., 2023</xref>). Their corrosion behaviors under different conditions have been widely studied (<xref ref-type="bibr" rid="B14">Dorcheh et al., 2016</xref>; <xref ref-type="bibr" rid="B4">Alc&#xe1;ntara et al., 2017</xref>; <xref ref-type="bibr" rid="B16">Dwivedi et al., 2017</xref>; <xref ref-type="bibr" rid="B21">Fahim et al., 2019</xref>; <xref ref-type="bibr" rid="B13">Dong et al., 2020</xref>; <xref ref-type="bibr" rid="B20">Ettefagh et al., 2021</xref>). Compared with CSs, SSs provide higher corrosion resistance to CO<sub>2</sub> due to the Cr-rich passive film on the surface (<xref ref-type="bibr" rid="B54">Wu et al., 2013</xref>; <xref ref-type="bibr" rid="B29">Lin et al., 2015</xref>; <xref ref-type="bibr" rid="B49">Wang et al., 2016</xref>). CrSs are the economical alternative to expensive SSs in combating abiotic CO<sub>2</sub> corrosion, which usually appears as uniform corrosion. However, in SRB MIC, CrSs or low grade SSs were found to suffer severe pitting corrosion despite their high uniform corrosion resistance (<xref ref-type="bibr" rid="B58">Xu et al., 2023b</xref>). Unlike the non-conductive siderite film in CO<sub>2</sub> corrosion, the semi-conductive FeS film in SRB MIC allows electrons to be harvested across it. The occasionally damaged spots on the Cr-rich layer will serve as anodic sites where iron oxidation will occur. The much larger undamaged surface becomes a large cathode, and the small anode-large cathode area ratio situation amplifies pitting. In a previous study, 13Cr [also known as API 5CT L80-13Cr, 13Cr or 420 SS (<xref ref-type="bibr" rid="B39">Scheuer et al., 2019</xref>)] incubated with <italic>Desulfovibrio ferrophilus</italic> (IS5 strain) for 7 days had a much lower weight loss of 4.4 mg/cm<sup>2</sup> (0.30 mm/a uniform corrosion rate) compared with N80 carbon steel (15.2 mg/cm<sup>2</sup> and 1.01 mm/a uniform corrosion rate). However, 13Cr suffered very severe pitting corrosion (15 mm/a) compared with N80 (0.38 mm/a), with 7-day pits visible even to the naked eyes (L. <xref ref-type="bibr" rid="B58">Xu et al., 2023b</xref>).</p>
<p>The relative pitting severity (<italic>RPS</italic>) was defined by Eq. <xref ref-type="disp-formula" rid="e4">4</xref> to quantify the pitting corrosion severity vs. uniform corrosion severity (<xref ref-type="bibr" rid="B15">Dou et al., 2018</xref>),<disp-formula id="e4">
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<mml:mtext>maximum</mml:mtext>
<mml:mtext>&#x2009;</mml:mtext>
<mml:mtext>pitting</mml:mtext>
<mml:mtext>&#x2009;</mml:mtext>
<mml:mtext>rate</mml:mtext>
</mml:mrow>
<mml:mrow>
<mml:mtext>uniform</mml:mtext>
<mml:mtext>&#x2009;</mml:mtext>
<mml:mtext>corrosion</mml:mtext>
<mml:mtext>&#x2009;</mml:mtext>
<mml:mtext>rate</mml:mtext>
<mml:mtext>&#x2009;</mml:mtext>
<mml:mtext>based</mml:mtext>
<mml:mtext>&#x2009;</mml:mtext>
<mml:mtext>on</mml:mtext>
<mml:mtext>&#x2009;</mml:mtext>
<mml:mrow>
<mml:mfenced open="(" close=")" separators="|">
<mml:mrow>
<mml:mtext>specific</mml:mtext>
</mml:mrow>
</mml:mfenced>
</mml:mrow>
<mml:mtext>&#x2009;</mml:mtext>
<mml:mtext>weight</mml:mtext>
<mml:mtext>&#x2009;</mml:mtext>
<mml:mtext>loss</mml:mtext>
</mml:mrow>
</mml:mfrac>
</mml:mrow>
</mml:math>
<label>(4)</label>
</disp-formula>
</p>
<p>When <italic>RPS</italic> is around unity, both pitting corrosion and uniform corrosion are important. When <italic>RPS</italic> is much greater than unity, pitting corrosion is deemed much more aggressive than uniform corrosion. The <italic>RPS</italic> of 13Cr in <italic>D. ferrophilus</italic> IS5 MIC was found to be 50 in SRB MIC which is far greater than unity, indicating very high pitting corrosion relatively to uniform corrosion (L. <xref ref-type="bibr" rid="B58">Xu et al., 2023b</xref>). Pitting corrosion is more dangerous than uniform corrosion since deep pits can easily lead to pipeline failures due to pinhole leaks (<xref ref-type="bibr" rid="B9">Chouchaoui and Pick, 1996</xref>; <xref ref-type="bibr" rid="B2">Abdalla Filho et al., 2014</xref>). Even a single deep pit can penetrate the material and cause equipment failure and even catastrophic accidents (<xref ref-type="bibr" rid="B6">Bhandari et al., 2015</xref>). Therefore, a mitigation plan should be in place to minimize pitting risks of 13Cr.</p>
<p>Biocide mitigation is a common strategy to treat biofilms which are responsible for MIC (<xref ref-type="bibr" rid="B23">Grande Burgos et al., 2013</xref>; <xref ref-type="bibr" rid="B5">Astuti et al., 2018</xref>; <xref ref-type="bibr" rid="B1">Abbas et al., 2021</xref>). Tetrakis hydroxymethyl phosphonium sulfate (THPS) is a popular green biocide in oilfields which has been found to be effective in mitigating SRB MIC in different systems (<xref ref-type="bibr" rid="B22">Gana et al., 2011</xref>; <xref ref-type="bibr" rid="B11">Conlette, 2014</xref>; <xref ref-type="bibr" rid="B42">Silva et al., 2021</xref>). Biocide enhancers at a small dosage can considerably improve biocide efficacy when used together with biocides (<xref ref-type="bibr" rid="B32">Mukherjee and Ahn, 2022</xref>; <xref ref-type="bibr" rid="B57">Xu et al., 2023a</xref>; <xref ref-type="bibr" rid="B41">Shi et al., 2023</xref>). Peptide A, a chemically synthesized 14-mer circular peptide (cys-ser-val-pro-tyr-asp-tyr-asn-trp-tyr-ser-asn-trp-cys) was reported to be an effective biocide enhancer at a sub-ppm (w/w) dosage for THPS in mitigating MIC. It is a nature-mimicking peptide that shows a biofilm dispersing effect in the presence of biocides. Its core 12-mer sequence was inspired by nature with its origin from a protein in a sea anemone that has a biofilm-free exterior (<xref ref-type="bibr" rid="B27">Jia et al., 2019</xref>). A biocide such as THPS at a low concentration may achieve the same inhibition result as a high concentration with the help of Peptide A at a sub-ppm dosage.</p>
<p>Because of the potential severe pitting on 13Cr caused by SRB MIC, for field applications it is necessary to have mitigation strategies such as biocide treatment in place. Thus, it is desired to study if deep pits would disappear with biocide treatment. In this work, 13Cr coupons were incubated with <italic>D. ferrophilus</italic> IS5, a highly corrosive SRB strain. Different biocide dosages were tested to investigate the mitigation effect of THPS and enhancement performance of Peptide A. The coupon tests were complimented by electrochemical tests.</p>
</sec>
<sec id="s2">
<title>2 Experimental</title>
<sec id="s2-1">
<title>2.1 Bacterium, metal, and culture medium</title>
<p>
<xref ref-type="table" rid="T1">Table 1</xref> shows a test matrix for this investigation. <italic>D. ferrophilus</italic> (strain IS5) was cultured anaerobically in enriched artificial seawater (EASW) culture medium at 28&#xb0;C (optimal temperature for growth) (<xref ref-type="bibr" rid="B19">Enning et al., 2012</xref>). The composition of EASW is listed in <xref ref-type="table" rid="T2">Table 2</xref>. The test coupon was 13Cr, and its elemental composition is summarized in <xref ref-type="table" rid="T3">Table 3</xref>.</p>
<table-wrap id="T1" position="float">
<label>TABLE 1</label>
<caption>
<p>Test matrix to evaluate biocide mitigation of <italic>D. ferrophilus</italic> MIC against 13Cr.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th align="left">Parameter</th>
<th align="left">Condition</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="left">Microbe</td>
<td align="left">
<italic>D. ferrophilus</italic> (IS5 strain)</td>
</tr>
<tr>
<td align="left">Cultural medium</td>
<td align="left">Enriched artificial seawater (EASW)</td>
</tr>
<tr>
<td align="left">Coupon material</td>
<td align="left">13Cr</td>
</tr>
<tr>
<td align="left">Liquid volume</td>
<td align="left">50 mL in 125 mL anaerobic vials, 5 mL in 10 mL glass cells</td>
</tr>
<tr>
<td align="left">Inoculum size</td>
<td align="left">0.5 mL in anaerobic vials, 0.05 mL in glass cells</td>
</tr>
<tr>
<td align="left">Temperature</td>
<td align="left">28&#xb0;C</td>
</tr>
<tr>
<td align="left">Initial pH</td>
<td align="left">7.0 &#xb1; 0.2</td>
</tr>
<tr>
<td align="left">Incubation time</td>
<td align="left">7 days</td>
</tr>
<tr>
<td align="left">Treatment</td>
<td align="left">No treatment (control), 50 ppm THPS, 50 ppm THPS &#x2b; 100 nM (180 ppb) Peptide A, 100 ppm THPS</td>
</tr>
<tr>
<td align="left">Assay</td>
<td align="left">Sessile cell count, weight loss, pit depth using 125 mL anaerobic vials; electrochemical tests using 10 mL glass cells</td>
</tr>
</tbody>
</table>
</table-wrap>
<table-wrap id="T2" position="float">
<label>TABLE 2</label>
<caption>
<p>Composition of EASW culture medium (<xref ref-type="bibr" rid="B40">Sheng et al., 2007</xref>).</p>
</caption>
<table>
<thead valign="top">
<tr>
<th align="left">Chemical</th>
<th align="left">Amount</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="left">NaCl</td>
<td align="left">23.476 g</td>
</tr>
<tr>
<td align="left">Na<sub>2</sub>SO<sub>4</sub>
</td>
<td align="left">3.917 g</td>
</tr>
<tr>
<td align="left">NaHCO<sub>3</sub>
</td>
<td align="left">0.192 g</td>
</tr>
<tr>
<td align="left">KCl</td>
<td align="left">0.664 g</td>
</tr>
<tr>
<td align="left">KBr</td>
<td align="left">0.096 g</td>
</tr>
<tr>
<td align="left">H<sub>3</sub>BO<sub>3</sub>
</td>
<td align="left">0.026 g</td>
</tr>
<tr>
<td align="left">MgCl<sub>2</sub>
</td>
<td align="left">4.965 g</td>
</tr>
<tr>
<td align="left">SrCl<sub>2</sub>&#xb7;6H<sub>2</sub>O</td>
<td align="left">0.04 g</td>
</tr>
<tr>
<td align="left">CaCl<sub>2</sub>&#xb7;2H<sub>2</sub>O</td>
<td align="left">1.469 g</td>
</tr>
<tr>
<td align="left">Sodium lactate</td>
<td align="left">3.5 g</td>
</tr>
<tr>
<td align="left">Yeast extract</td>
<td align="left">1.0 g</td>
</tr>
<tr>
<td align="left">Sodium citrate</td>
<td align="left">0.5 g</td>
</tr>
<tr>
<td align="left">MgSO<sub>4</sub>&#xb7;7H<sub>2</sub>O</td>
<td align="left">0.71 g</td>
</tr>
<tr>
<td align="left">CaSO<sub>4</sub>&#xb7;2H<sub>2</sub>O</td>
<td align="left">0.1 g</td>
</tr>
<tr>
<td align="left">NH<sub>4</sub>Cl</td>
<td align="left">0.1 g</td>
</tr>
<tr>
<td align="left">K<sub>2</sub>HPO<sub>4</sub>
</td>
<td align="left">0.05 g</td>
</tr>
<tr>
<td align="left">Fe(NH<sub>4</sub>)<sub>2</sub>(SO<sub>4</sub>)<sub>2</sub>&#xb7;6H<sub>2</sub>O</td>
<td align="left">1.37 g</td>
</tr>
<tr>
<td align="left">DI water</td>
<td align="left">1 L</td>
</tr>
</tbody>
</table>
</table-wrap>
<table-wrap id="T3" position="float">
<label>TABLE 3</label>
<caption>
<p>Elemental compositions (wt%) of 13Cr (Fe balance).</p>
</caption>
<table>
<thead valign="top">
<tr>
<th align="center">C</th>
<th align="center">Mn</th>
<th align="center">Cr</th>
<th align="center">Ni</th>
<th align="center">Cu</th>
<th align="center">P</th>
<th align="center">S</th>
<th align="center">Si</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="center">0.15&#x2013;0.22</td>
<td align="center">0.25&#x2013;1.00</td>
<td align="center">12.0&#x2013;14.0</td>
<td align="center">&#x2264;0.50</td>
<td align="center">&#x2264;0.25</td>
<td align="center">&#x2264;0.020</td>
<td align="center">&#x2264;0.010</td>
<td align="center">&#x2264;1.00</td>
</tr>
</tbody>
</table>
</table-wrap>
<p>The EASW culture medium was adjusted to an initial pH of 7.0 using 5% (w/w) NaOH. Before inoculation, the medium was autoclave-sterilized and deoxygenated by purging filter-sterilized N<sub>2</sub> gas for 1 h. The addition of 100 ppm (w/w) L-cysteine into EASW was conducted in an anaerobic chamber filled with N<sub>2</sub> to further remove dissolved oxygen, following its use in the ATCC 1249 culture medium. THPS (Sigma-Aldrich, St. Louis, MO, USA) was dissolved into a 5,000 ppm (w/w) stock solution for biocide treatment.</p>
<p>The pre-cut 13Cr coupons all had an exposed top surface area of 1 cm<sup>2</sup> (1 cm &#xd7; 1 cm). The top test surfaces were polished progressively to a 600 grit final finish. All other coupon surfaces were painted with inert Epoxy coating (3M Product 323). The coupons were sanitized using absolute isopropanol before testing.</p>
</sec>
<sec id="s2-2">
<title>2.2 Enumeration of sessile cells</title>
<p>Three replicate 13Cr coupons were put into each anaerobic vial for different treatment conditions. The initial <italic>D. ferrophilus</italic> planktonic cell concentration in each vial upon inoculation was 10<sup>6</sup> cells/mL. After incubation for 7 days, all coupons were taken out from the anaerobic vials. Deoxygenated phosphate buffered saline (PBS) solution (pH 7.4) was then used to rinse the coupons. Sessile cells on each coupon surface were transferred into a 10 mL (or 1 mL if cell count too low for counting in a 10 mL cell suspension) PBS solution (total) using a sterile brush applicator. The brush, the coupon, and the PBS solution were vortexed for 30 s in a 50 mL centrifuge tube. The evenly distributed cell suspension in the tube was used for cell counting. A hemocytometer was employed in which (viable motile) cells can be counted under an optical microscope at &#xd7;400 magnification.</p>
</sec>
<sec id="s2-3">
<title>2.3 Biofilm visualization</title>
<p>Biofilms on coupon surfaces after 7-day incubation were observed under CLSM (confocal laser scanning microscopy) (Model LSM 510, Carl Zeiss, Jena, Germany). Coupons were first rinsed in pH 7.4 PBS solution to wash away planktonic cells and culture medium. Then the coupon surfaces were stained with Live/Dead<sup>&#xae;</sup> BacLight&#x2122; Bacterial Viability Kit L7012 (Life Technologies, Grand Island, NY, United States) before observation. Under CLSM, live cells were seen as green dots at 488 nm wavelength laser and dead cells as red dots at a wavelength of 559 nm.</p>
</sec>
<sec id="s2-4">
<title>2.4 Weight loss and pit depth</title>
<p>Three replicate 13Cr coupons were used for each treatment condition in the weight loss test. After the 7-day incubation in 125 mL anaerobic vials, the biofilm and corrosion products on each coupon were removed with a freshly prepared Clarke&#x2019;s solution for 30 s before weight measurement following ASTM G1&#x2013;03. Coupon surfaces were scanned using an infinite focus microscope (IFM) profilometer (Model ALC13, Alicona Imaging GmbH, Graz, Austria) to obtain pit depth and surface profiles.</p>
</sec>
<sec id="s2-5">
<title>2.5 Electrochemical measurements</title>
<p>Electrochemical tests were executed in 10 mL electrochemical glass cells, each filled with 5 mL EASW inoculated with 0.05 mL seed culture. Each glass cell consisted of a 13Cr WE (working electrode) (1 cm &#xd7; 1 cm) and a graphite rod (0.64 cm diameter and 1 cm height) counter electrode, which also served as reference electrode. Electrochemical scans were performed using a PCI4/750 potentiostat (Gamry Instruments, Inc., Warminster, PA, United States). Linear polarization resistance (LPR) and Tafel were scanned daily during the 7-day incubation period. LPR measurement was performed within the range of &#x2212;10 to 10 mV vs. OCP (open circuit potential) with a rate of 0.167 mV/s. Tafel curves were scanned at a scan rate of 0.167 mV/s from OCP to &#x2212;200 mV vs. OCP, and then after a 20 min gap, from OCP to &#x2b;200 mV vs. OCP on the same working electrode (<xref ref-type="bibr" rid="B50">Wang et al., 2021a</xref>; <xref ref-type="bibr" rid="B58">Xu et al., 2023b</xref>). It was shown that this dual half-scan scheme with the voltage range did not alter the working electrode in repeated scans on the same working electrode (<xref ref-type="bibr" rid="B51">Wang et al., 2022a</xref>).</p>
</sec>
</sec>
<sec sec-type="results|discussion" id="s3">
<title>3 Results and discussion</title>
<sec id="s3-1">
<title>3.1 Sessile cell count</title>
<p>
<xref ref-type="fig" rid="F1">Figure 1</xref> shows images of 125 mL anaerobic vials before and after the 7-day incubation. <italic>D. ferrophilus</italic> growth was seen in vials with no treatment, 50 ppm THPS and 50 ppm THPS &#x2b; 100 nM Peptide A. With 100 ppm THPS, no apparent planktonic growth was observed (not turbid), suggesting strong inhibition effect. <xref ref-type="table" rid="T4">Table 4</xref> summarizes sessile cell counts on coupons with different treatment.</p>
<fig id="F1" position="float">
<label>FIGURE 1</label>
<caption>
<p>Anaerobic vials containing 13Cr coupons before <bold>(A)</bold> and after <bold>(B)</bold> 7-day incubation with <italic>D. ferrophilus</italic> (strain IS5) in EASW (left to right): abiotic control, no treatment, 50 ppm THPS, 50 ppm THPS &#x2b; 100 nM Peptide A, and 100 ppm THPS.</p>
</caption>
<graphic xlink:href="fmats-11-1407655-g001.tif"/>
</fig>
<table-wrap id="T4" position="float">
<label>TABLE 4</label>
<caption>
<p>Sessile cell count and reduction in biofilms on 13Cr coupon surfaces.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th align="center">Treatment</th>
<th align="center">Sessile cell count (&#xd7;10<sup>6</sup> cells/cm<sup>2</sup>)</th>
<th align="center">Reduction</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="center">No treatment</td>
<td align="center">39 &#xb1; 8</td>
<td align="center">-</td>
</tr>
<tr>
<td align="center">50 ppm THPS</td>
<td align="center">8.0 &#xb1; 0.4</td>
<td align="center">0.7-log</td>
</tr>
<tr>
<td align="center">50 ppm THPS &#x2b; 100 nM Peptide A</td>
<td align="center">2.4 &#xb1; 0.4</td>
<td align="center">1.2-log</td>
</tr>
<tr>
<td align="center">100 ppm THPS</td>
<td align="center">Undetectable</td>
<td align="center">(&#x3e;2.9-log)</td>
</tr>
</tbody>
</table>
</table-wrap>
<p>Without biocide treatment, sessile cells on 13Cr coupons were found to be (3.9 &#xb1; 0.8) &#xd7; 10<sup>7</sup> cells/cm<sup>2</sup>. With treatment of 50 ppm THPS and 50 ppm THPS &#x2b; 100 nM Peptide A, sessile cell counts reduced to (8.0 &#xb1; 0.4) &#xd7; 10<sup>6</sup> cells/cm<sup>2</sup> and (2.4 &#xb1; 0.4) &#xd7; 10<sup>6</sup> cells/cm<sup>2</sup>. A 0.7-log reduction was seen in sessile cells with 50 ppm THPS alone, and the addition of 100 nM Peptide A achieved an extra 0.5-log reduction, showing its obvious enhancement effect. Sessile cells were not detected (detection threshold of 5 &#xd7; 10<sup>4</sup> planktonic cells/mL translating into 5 &#xd7; 10<sup>4</sup> sessile cells/cm<sup>2</sup>) on coupons treated with 100 ppm THPS.</p>
</sec>
<sec id="s3-2">
<title>3.2 Biofilm CLSM images</title>
<p>CLSM images of <italic>D. ferrophilus</italic> biofilms on 13Cr coupon surfaces with different treatments are presented in <xref ref-type="fig" rid="F2">Figure 2</xref>. Healthy biofilms were seen on the coupon surface without treatment (<xref ref-type="fig" rid="F2">Figure 2A</xref>) with densely populated green dots (live cells). With 50 ppm THPS and 50 ppm THPS &#x2b; 100 nM Peptide A (<xref ref-type="fig" rid="F2">Figures 2B, C</xref>), live cells became fewer and more dead cells (red dots) appeared. It is hard to see any live cells in <xref ref-type="fig" rid="F2">Figure 2D</xref> on the 13Cr coupon surface treated with 100 ppm THPS. Here, these CLSM biofilm observations are consistent with the sessile cell count results.</p>
<fig id="F2" position="float">
<label>FIGURE 2</label>
<caption>
<p>CLSM images of biofilms on 13Cr coupons after 7-day incubation <italic>D. ferrophilus</italic> in EASW: <bold>(A)</bold> no treatment, <bold>(B)</bold> 50 ppm THPS, <bold>(C)</bold> 50 ppm THPS &#x2b; 100 nM Peptide A, and <bold>(D)</bold> 100 ppm THPS.</p>
</caption>
<graphic xlink:href="fmats-11-1407655-g002.tif"/>
</fig>
</sec>
<sec id="s3-3">
<title>3.3 Weight loss</title>
<p>The weight loss results of 13Cr coupons with different treatment are listed in <xref ref-type="table" rid="T5">Table 5</xref>. For the abiotic control, no weight loss was detected. The weight losses for coupons with no treatment, 50 ppm THPS, 50 ppm THPS &#x2b; 100 nM Peptide A and 100 ppm THPS were 3.8 &#xb1; 0.5 mg/cm<sup>2</sup> (equivalent to uniform corrosion rate 0.26 &#xb1; 0.03 mm/a), 2.2 &#xb1; 0.2 mg/cm<sup>2</sup> (0.15 &#xb1; 0.01 mm/a), 1.5 &#xb1; 0.5 mg/cm<sup>2</sup> (0.10 &#xb1; 0.03 mm/a) and 0.3 &#xb1; 0.2 mg/cm<sup>2</sup> (0.02 &#xb1; 0.01 mm/a), respectively. THPS at 50 ppm reduced weight loss by 42%, while 50 ppm THPS &#x2b; 100 nM Peptide A achieved an extra 18% weight loss reduction, suggesting considerable enhancement effect. With 100 ppm THPS, the uniform corrosion inhibition efficiency reached 92% which was very effective. In EET-MIC by SRB, sessile cells in biofilms are directly involved in iron oxidation. The weight loss sequence matches the sessile cell count sequence. Thus, the greatly reduced weight loss here can be attributed to the effectiveness of THPS in inhibiting the growth of <italic>D. ferrophilus</italic> biofilms and the biofilm dispersing effect of Peptide A.</p>
<table-wrap id="T5" position="float">
<label>TABLE 5</label>
<caption>
<p>Weight loss of 13Cr after 7-day incubation with <italic>D. ferrophilus</italic>.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th align="center">Treatment</th>
<th align="center">Weight loss (mg/cm<sup>2</sup>)</th>
<th align="center">Uniform corrosion rate (mm/a)</th>
<th align="center">Inhibition efficiency (%)</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="center">Abiotic</td>
<td align="center">&#x2212;0.1 &#xb1; 0.1</td>
<td align="center">&#x2212;0.01 &#xb1; 0.01</td>
<td align="center">-</td>
</tr>
<tr>
<td align="center">No treatment</td>
<td align="center">3.8 &#xb1; 0.5</td>
<td align="center">0.26 &#xb1; 0.03</td>
<td align="center">(basis)</td>
</tr>
<tr>
<td align="center">50 ppm THPS</td>
<td align="center">2.2 &#xb1; 0.2</td>
<td align="center">0.15 &#xb1; 0.01</td>
<td align="center">42</td>
</tr>
<tr>
<td align="center">50 ppm THPS &#x2b; 100 nM Peptide A</td>
<td align="center">1.5 &#xb1; 0.5</td>
<td align="center">0.10 &#xb1; 0.03</td>
<td align="center">60</td>
</tr>
<tr>
<td align="center">100 ppm THPS</td>
<td align="center">0.3 &#xb1; 0.2</td>
<td align="center">0.02 &#xb1; 0.01</td>
<td align="center">92</td>
</tr>
</tbody>
</table>
</table-wrap>
<p>The outstanding performance of THPS in mitigating SRB MIC was because the degradation of THPS forms trihydroxymethyl phosphine which can destroy microbial cell walls by reducing disulfide bonds within cell wall disulfide amino acids (<xref ref-type="bibr" rid="B35">Parker and Kharasch, 1959</xref>; <xref ref-type="bibr" rid="B37">R&#xfc;egg and Rudinger, 1977</xref>). THPS also inhibits SRB growth through its selective action which affects the hNRB (heterotrophic nitrate-reducing bacteria) and so-NRB (sulfide-oxidizing-NRB) activities (<xref ref-type="bibr" rid="B34">Okoro, 2015</xref>). Besides, as an H<sub>2</sub>S scavenger, THPS can mitigate corrosion caused by souring (<xref ref-type="bibr" rid="B45">Talbot et al., 2000</xref>). The biofilm dispersing effect of Peptide A enhanced the THPS treatment effect as some sessile cells were detached without biocide kill. The exact mechanism for Peptide A&#x2019;s superior biofilm dispersing ability remains unknown, but it likely functions as a signal molecule. Thus, its effective dosage is extremely small, much lower than the 10s of ppm dosage required for a typical corrosion inhibitor that needs to have a monolayer coverage on a metal surface.</p>
</sec>
<sec id="s3-4">
<title>3.4 Pitting analysis</title>
<p>Coupons with biofilms and corrosion products removed are shown in <xref ref-type="fig" rid="F3">Figures 3A&#x2013;E</xref>. Some corrosion pits on the coupons are visible to the naked eyes, especially for coupons without treatment in <xref ref-type="fig" rid="F3">Figure 3B</xref>. <xref ref-type="fig" rid="F4">Figure 4</xref> presents pits with maximum depth and pit profiles scanned using IFM. No well-defined pits were found on the abiotic coupon surface. The maximum pit depth for coupons with no treatment, 50 ppm THPS, 50 ppm THPS &#x2b; 100 nM Peptide A and 100 ppm THPS were 375 &#x3bc;m (equivalent to 20 mm/a pitting rate), 232 &#x3bc;m (12 mm/a), 163 &#x3bc;m (8.6 mm/a) and 28 &#x3bc;m (1.5 mm/a), respectively. The single deepest pit on the coupon without treatment alone results in a weigh loss of 1.95 mg, accounting for 42% of the entire coupon weight loss. The addition of 50 ppm THPS, 50 ppm THPS &#x2b; 100 nM Peptide A and 100 ppm THPS reduced pitting rates by 38%, 57%, and 93%, respectively. Thus, 100 ppm THPS mitigated pitting corrosion greatly.</p>
<fig id="F3" position="float">
<label>FIGURE 3</label>
<caption>
<p>13Cr coupons after Clarke&#x2019;s solution cleaning treatment following 7-day <italic>D. ferrophilus</italic> incubation in EASW: <bold>(A)</bold> abiotic control, <bold>(B)</bold> no treatment, <bold>(C)</bold> 50 ppm THPS, <bold>(D)</bold> 50 ppm THPS &#x2b; 100 nM Peptide A, and <bold>(E)</bold> 100 ppm THPS.</p>
</caption>
<graphic xlink:href="fmats-11-1407655-g003.tif"/>
</fig>
<fig id="F4" position="float">
<label>FIGURE 4</label>
<caption>
<p>Pit images and profiles from IFM for 13Cr coupons after 7-day <italic>D. ferrophilus</italic> incubation in EASW in anaerobic vials. (Red lines indicate IFM pit profile scan paths.)</p>
</caption>
<graphic xlink:href="fmats-11-1407655-g004.tif"/>
</fig>
<p>Based on the uniform corrosion rates from weight loss data and pitting corrosion rates, <italic>RPS</italic> were calculated and summarized in <xref ref-type="table" rid="T6">Table 6</xref>. The <italic>RPS</italic> for 13Cr in all conditions were all considerably high but similar with an average value of 80. In comparison, <italic>RPS</italic> of C1018 carbon steel MIC by <italic>D. ferrophilus</italic> in EASW was only 1.36 (<xref ref-type="bibr" rid="B50">Wang et al., 2021a</xref>). This phenomenon supported the fact that pitting corrosion is the major issue for low grade stainless steels just like 13Cr. Even with biocide treatment, the <italic>RPS</italic> values showed no apparent changes, which were still almost two orders of magnitude of that for C1018 carbon steel. With 100 ppm THPS, the uniform corrosion rate declined to a very small number of 0.02 mm/a. However, its pitting rate was still as high as 1.5 mm/a, which is greater than pitting rates of some carbon steels in the same system without any biocide treatment (<xref ref-type="bibr" rid="B50">Wang et al., 2021a</xref>; <xref ref-type="bibr" rid="B58">Xu et al., 2023b</xref>). Thus, a higher THPS dosage may be needed for better biocide mitigation to prevent pinhole leaks due to SRB MIC pitting.</p>
<table-wrap id="T6" position="float">
<label>TABLE 6</label>
<caption>
<p>Calculated <italic>RPS</italic> values for different treatment.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th align="center"/>
<th align="center">No treatment</th>
<th align="center">50 ppm THPS</th>
<th align="center">50 ppm THPS &#x2b; 100 nM peptide A</th>
<th align="center">100 ppm THPS</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="center">Uniform corrosion rate (mm/a)</td>
<td align="center">0.26</td>
<td align="center">0.15</td>
<td align="center">0.10</td>
<td align="center">0.02</td>
</tr>
<tr>
<td align="center">Pitting rate (mm/a)</td>
<td align="center">20</td>
<td align="center">12</td>
<td align="center">8.6</td>
<td align="center">1.5</td>
</tr>
<tr>
<td align="center">
<italic>RPS</italic>
</td>
<td align="center">77</td>
<td align="center">80</td>
<td align="center">86</td>
<td align="center">75</td>
</tr>
</tbody>
</table>
</table-wrap>
<p>The high <italic>PRS</italic> values in <xref ref-type="table" rid="T6">Table 6</xref> for 13Cr shows that it is particularly prone to pitting corrosion. 13Cr is a low-grade stainless steel (420 SS) with a PREN (pitting resistance equivalent number) value of 13. It has a passive film that is relatively easy to be damaged in some spots compared to higher grade stainless steels such as 304 SS with a PREN value of 20 (L. <xref ref-type="bibr" rid="B58">Xu et al., 2023b</xref>). CrSs have Cr oxide/hydroxide passive films that are (semi-)conductive (<xref ref-type="bibr" rid="B44">Sun et al., 2016</xref>). In SRB MIC, the iron sulfide corrosion product film is also (semi-)conductive (<xref ref-type="bibr" rid="B24">Gu et al., 2019</xref>). Thus, 13Cr MIC by SRB satisfies the two essential requirements for classical pitting, i.e., a passive film that can be damaged and the passive film is (semi-)conductive (L. <xref ref-type="bibr" rid="B58">Xu et al., 2023b</xref>). This leads to a large cathode to small anode area ratio situation, which amplifies the pitting effect as illustrated in <xref ref-type="fig" rid="F5">Figure 5</xref>. In carbon steel MIC by SRB, the corrosion products (iron sulfides) form a conductive film that can reach 10&#x2013;30 &#x3bc;m in thickness (<xref ref-type="bibr" rid="B26">Jia et al., 2018</xref>). In stainless steel MIC by SRB, the iron sulfides film will be on top of the metal&#x2019;s own passive film (chromium oxides/chromium hydroxide) that is only several nm in thickness (<xref ref-type="bibr" rid="B31">Mohammadi et al., 2011</xref>). Sessile cells in the biofilm can harvest electrons across both (semi-)conductive films.</p>
<fig id="F5" position="float">
<label>FIGURE 5</label>
<caption>
<p>Schematic illustration showing small anode-large cathode with semi-conductive passive film(s) scenario leading to severe pitting with an isolated large pit.</p>
</caption>
<graphic xlink:href="fmats-11-1407655-g005.tif"/>
</fig>
</sec>
<sec id="s3-5">
<title>3.5 Electrochemical measurements</title>
<p>Electrochemical tests can provide extra evidence, especially transient information, to support one-shoot weight loss data. <xref ref-type="fig" rid="F6">Figure 6</xref> demonstrates <italic>R</italic>
<sub>p</sub> (polarization resistance) variations of 13Cr with different treatment from LPR measurements. The abiotic control exhibited a stable curve over the 7-day incubation. Without treatment, <italic>R</italic>
<sub>p</sub> declined considerably from 1 day to 3 days and remained stable for the remaining time. This suggests that mature biofilm formed at 3 days and corrosion rate generally increased during the first 3 days and stabilized from 3 days to 7 days. With 50 ppm THPS, the <italic>R</italic>
<sub>p</sub> curve was consistently higher than that of no treatment. Compared with 50 ppm THPS alone, <italic>R</italic>
<sub>p</sub> values of 50 ppm THPS &#x2b; 100 nM Peptide A were generally higher, especially from 5 days to 7 days. Thus, the enhancement effect of Peptide A for THPS was clearly manifested. The <italic>R</italic>
<sub>p</sub> values of 100 ppm THPS did not drop considerably compared to the abiotic control and remained high during the 7-d incubation period, indicating effective corrosion inhibition through biofilm inhibition. The 1/<italic>R</italic>
<sub>p</sub> sequence of different treatments matches the corrosion rate sequence based on weight loss results. Based on the 1/<italic>R</italic>
<sub>p</sub> data at 7 days, 100 ppm THPS achieved a corrosion inhibition efficiency of 97%.</p>
<fig id="F6" position="float">
<label>FIGURE 6</label>
<caption>
<p>
<italic>R</italic>
<sub>p</sub> curves from LPR measurements during 7-day <italic>D. ferrophilus</italic> incubation in 10 mL electrochemical glass cell.</p>
</caption>
<graphic xlink:href="fmats-11-1407655-g006.tif"/>
</fig>
<p>Corrosion current density (<italic>i</italic>
<sub>corr</sub>) results fitted from 7-day Tafel scans are displayed in <xref ref-type="fig" rid="F7">Figure 7</xref>. Without treatment, <italic>i</italic>
<sub>corr</sub> gradually increased and remained higher than the treated conditions. With 100 nM Peptide A, <italic>i</italic>
<sub>corr</sub> values of 100 ppm THPS were generally lower than those without over the entire 7-day incubation period. The 100 ppm THPS <italic>i</italic>
<sub>corr</sub> kept at a low level which was close to the abiotic control, proving that 100 ppm THPS was effective in biofilm inhibition. The <italic>i</italic>
<sub>corr</sub> sequence of different treatments again matches the weight loss sequence. Based on the <italic>i</italic>
<sub>corr</sub> data at 7 days, 100 ppm THPS achieved a corrosion inhibition efficiency of 93%. It should be noted that daily Tafel scans of the same WE were permitted using the dual-scan method with cathodic scan and cathodic scan commencing at OCP according to our previous Tafel scan scheme study (<xref ref-type="bibr" rid="B51">Wang et al., 2022a</xref>). Both LPR and Tafel findings confirmed the effective mitigation of <italic>D. ferrophilus</italic> MIC on 13Cr and the obvious enhancement effect of Peptide A for THPS. They provide extra evidence to support weight loss or uniform corrosion results. The overall corrosion rates were substantially reduced with biocide addition which also resulted in much lower pitting rates as reflected by the pitting analysis.</p>
<fig id="F7" position="float">
<label>FIGURE 7</label>
<caption>
<p>
<italic>i</italic>
<sub>corr</sub> vs. time during 7-day <italic>D. ferrophilus</italic> incubation in 10 mL electrochemical glass cell.</p>
</caption>
<graphic xlink:href="fmats-11-1407655-g007.tif"/>
</fig>
<p>Injection tests were conducted in a 10 mL electrochemical cell at 3 days when mature <italic>D. ferrophilus</italic> biofilms formed on the 13Cr WE surface. In <xref ref-type="fig" rid="F8">Figure 8</xref>, stable <italic>R</italic>
<sub>p</sub> readings were obtained for 40 min before injections. After 20 ppm (final concentration in the broth) MNPs injection, a generally decreasing <italic>R</italic>
<sub>p</sub> trend was observed and <italic>R</italic>
<sub>p</sub> was reduced by 16% in 40 min after the injection, which means the corrosion rate became higher. This shows that MNPs successfully enhanced MIC of <italic>D. ferrophilus</italic> against 13Cr. THPS was subsequently injected to reach 100 ppm in broth and led to an increase in <italic>R</italic>
<sub>p</sub>. The final <italic>R</italic>
<sub>p</sub> value was increased by 37% due to the THPS injection, indicating mitigation effect of THPS.</p>
<fig id="F8" position="float">
<label>FIGURE 8</label>
<caption>
<p>
<italic>R</italic>
<sub>p</sub> responses of 13Cr to tandem injections of MNPs and THPS in 10 mL electrochemical glass cell containing 3-day old <italic>D. ferrophilus</italic>. (Time zero indicates injection at 3 days of incubation.)</p>
</caption>
<graphic xlink:href="fmats-11-1407655-g008.tif"/>
</fig>
<p>The 16% <italic>R</italic>
<sub>p</sub> decreased after the injection of MNPs was because MIC of 13Cr by <italic>D. ferrophilus</italic> belongs to EET-MIC where the electron transfer between sessile cell walls and Fe surface is an important rate-limiting process, and the MNPs can serve as electron conduits to accelerate this process (<xref ref-type="bibr" rid="B53">Wang et al., 2022b</xref>). Thus, the SRB MIC of 13Cr is proven to be EET-MIC here. The followed THPS injection proved its biocidal effect in treating SRB biofilms and showed that electrochemical injection tests were sensitive enough to provide both accelerated and decelerated MIC information. It should be noted that treating a pre-established biofilm is far more difficult than preventing the biofilm from establishing. Thus, 37% was much smaller than the 93% based on the <italic>i</italic>
<sub>corr</sub> data at 7 days in <xref ref-type="fig" rid="F7">Figure 7</xref>.</p>
</sec>
</sec>
<sec sec-type="conclusion" id="s4">
<title>4 Conclusion</title>
<p>Severe pitting corrosion was found on 13Cr after the 7-day incubation. THPS was effective in mitigating <italic>D. ferrophilus</italic> MIC against 13Cr. The enhancement effect of Peptide A for THPS was manifested. The macroscopic pits on 13Cr coupon surfaces visible to the naked eyes disappeared with effective biocide treatment. However, to reduce pitting corrosion completely, a THPS dosage higher than 100 ppm will be needed.</p>
<p>The electrochemical results in this work indicate that electrochemical measurements qualitatively described biocide treatment efficacy consistent with sessile cell count and weight loss data trends.</p>
<p>This lab investigation demonstrated an alarming SRB pitting risk for 13Cr. If 13Cr is used to combat CO<sub>2</sub> (uniform) corrosion in the presence of SRB, a biocide mitigation plan should be in place to prevent pinhole leaks caused by potentially very fast SRB pitting.</p>
</sec>
</body>
<back>
<sec sec-type="data-availability" id="s5">
<title>Data availability statement</title>
<p>The raw data supporting the conclusion of this article will be made available by the authors, without undue reservation.</p>
</sec>
<sec id="s6">
<title>Author contributions</title>
<p>LX: Data curation, Formal Analysis, Investigation, Methodology, Validation, Visualization, Writing&#x2013;original draft. AK: Data curation, Investigation, Methodology, Writing&#x2013;original draft. PK: Conceptualization, Resources, Writing&#x2013;review and editing. SK: Conceptualization, Resources, Writing&#x2013;review and editing. SP: Conceptualization, Resources, Writing&#x2013;review and editing. TG: Funding acquisition, Methodology, Project administration, Supervision, Validation, Writing&#x2013;review and editing.</p>
</sec>
<sec sec-type="funding-information" id="s7">
<title>Funding</title>
<p>The author(s) declare that financial support was received for the research, authorship, and/or publication of this article. This work was financially supported by PTT Exploration and Production, and Petrobras.</p>
</sec>
<ack>
<p>We thank Flavia Maciel Fernandes Guedes, Vinicius de Abreu Waldow, Maira Paula de Sousa, Rubens Nobumoto Akamine, and Gustavo Leitao Vaz for their expertise and input throughout this study.</p>
</ack>
<sec sec-type="COI-statement" id="s8">
<title>Conflict of interest</title>
<p>Authors PK, SK, and SP were employed by PTT Exploration and Production.</p>
<p>The remaining 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="disclaimer" id="s9">
<title>Publisher&#x2019;s note</title>
<p>All claims expressed in this article are solely those of the authors and do not necessarily represent those of their affiliated organizations, or those of the publisher, the editors and the reviewers. Any product that may be evaluated in this article, or claim that may be made by its manufacturer, is not guaranteed or endorsed by the publisher.</p>
</sec>
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