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<front>
<journal-meta>
<journal-id journal-id-type="publisher-id">Front. Earth Sci.</journal-id>
<journal-title>Frontiers in Earth Science</journal-title>
<abbrev-journal-title abbrev-type="pubmed">Front. Earth Sci.</abbrev-journal-title>
<issn pub-type="epub">2296-6463</issn>
<publisher>
<publisher-name>Frontiers Media S.A.</publisher-name>
</publisher>
</journal-meta>
<article-meta>
<article-id pub-id-type="publisher-id">869917</article-id>
<article-id pub-id-type="doi">10.3389/feart.2022.869917</article-id>
<article-categories>
<subj-group subj-group-type="heading">
<subject>Earth Science</subject>
<subj-group>
<subject>Original Research</subject>
</subj-group>
</subj-group>
</article-categories>
<title-group>
<article-title>Impact of Microbially Enhanced Coalbed Methane on the Pore Structure of Coal</article-title>
<alt-title alt-title-type="left-running-head">Gao et al.</alt-title>
<alt-title alt-title-type="right-running-head">Microbially on Coal Pore Structure</alt-title>
</title-group>
<contrib-group>
<contrib contrib-type="author" corresp="yes">
<name>
<surname>Gao</surname>
<given-names>Di</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
</xref>
<xref ref-type="aff" rid="aff2">
<sup>2</sup>
</xref>
<xref ref-type="aff" rid="aff3">
<sup>3</sup>
</xref>
<xref ref-type="corresp" rid="c001">&#x2a;</xref>
<uri xlink:href="https://loop.frontiersin.org/people/1413465/overview"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Guo</surname>
<given-names>Huiling</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
</xref>
</contrib>
<contrib contrib-type="author" corresp="yes">
<name>
<surname>Guo</surname>
<given-names>Bianqing</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
</xref>
<xref ref-type="corresp" rid="c001">&#x2a;</xref>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Tan</surname>
<given-names>Kaili</given-names>
</name>
<xref ref-type="aff" rid="aff2">
<sup>2</sup>
</xref>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Ren</surname>
<given-names>Hengxing</given-names>
</name>
<xref ref-type="aff" rid="aff2">
<sup>2</sup>
</xref>
</contrib>
</contrib-group>
<aff id="aff1">
<sup>1</sup>
<institution>School of Resources and Environment</institution>, <institution>Henan Polytechnic University</institution>, <addr-line>Jiaozuo</addr-line>, <country>China</country>
</aff>
<aff id="aff2">
<sup>2</sup>
<institution>State Key Laboratory of Coal and Coalbed Methane Co-mining</institution>, <addr-line>Jincheng</addr-line>, <country>China</country>
</aff>
<aff id="aff3">
<sup>3</sup>
<institution>Collaborative Innovation Center of Coal Work Safety and Clean High Efficiency Utilization</institution>, <addr-line>Jiaozuo</addr-line>, <country>China</country>
</aff>
<author-notes>
<fn fn-type="edited-by">
<p>
<bold>Edited by:</bold> <ext-link ext-link-type="uri" xlink:href="https://loop.frontiersin.org/people/1310688/overview">Yiwen Ju</ext-link>, University of Chinese Academy of Sciences, 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/1676215/overview">Haihai Hou</ext-link>, Liaoning Technical University, China</p>
<p>
<ext-link ext-link-type="uri" xlink:href="https://loop.frontiersin.org/people/1677899/overview">Run Chen</ext-link>, China University of Mining and Technology, China</p>
</fn>
<corresp id="c001">&#x2a;Correspondence: Di Gao, <email>gaodi1119@163.com</email>; Bianqing Guo, <email>guobianqing@hpu.edu.cn</email>
</corresp>
<fn fn-type="other">
<p>This article was submitted to Economic Geology, a section of the journal Frontiers in Earth Science</p>
</fn>
</author-notes>
<pub-date pub-type="epub">
<day>30</day>
<month>03</month>
<year>2022</year>
</pub-date>
<pub-date pub-type="collection">
<year>2022</year>
</pub-date>
<volume>10</volume>
<elocation-id>869917</elocation-id>
<history>
<date date-type="received">
<day>05</day>
<month>02</month>
<year>2022</year>
</date>
<date date-type="accepted">
<day>14</day>
<month>03</month>
<year>2022</year>
</date>
</history>
<permissions>
<copyright-statement>Copyright &#xa9; 2022 Gao, Guo, Guo, Tan and Ren.</copyright-statement>
<copyright-year>2022</copyright-year>
<copyright-holder>Gao, Guo, Guo, Tan and Ren</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>Microbially enhanced coalbed methane (MECBM) has important theoretical and practical significance for reforming coal reservoir structure, alleviating greenhouse effects and energy crises and developing new sources of clean energy. In this study, No. 3 coal seams in Qinshui Basin were taken as research objects to analyze the pore structure characteristics after microbial treatment by means of low-temperature nitrogen adsorption (LTNA), mercury porosimetry (MP), and isothermal adsorption/desorption experiments. The results showed that after bioconversion, the specific surface area and pore volume increased from 1.79&#xa0;m<sup>2</sup>/g and 0.0018&#xa0;cm<sup>3</sup>/g to 4.01&#xa0;m<sup>2</sup>/g and 0.0051&#xa0;cm<sup>3</sup>/g respectively under liquid nitrogen testing; however, the specific surface area was reduced from 5.398&#xa0;m<sup>2</sup>/g to 5.246&#xa0;m<sup>2</sup>/g and the pore volume was increased from 0.053&#xa0;cm<sup>3</sup>/g to 0.0626&#xa0;cm<sup>3</sup>/g under MP. The fractal dimension based on the LTNA data indicated that the fractal dimension of micropores and minipores was increased from 2.73 to 2.60 to 2.89 and 2.81, however the fractal dimension of meso-macropores was decreased from 2.90 to 2.85. The volatile matter and fixed carbon were both reduced from 6.68% to 78.63%&#x2013;5.09% to 75.63%, and the Langmuir volume and Langmuir pressure were increased from 34.84&#xa0;cm<sup>3</sup>/g and 2.73&#xa0;MPa to 36.34&#xa0;cm<sup>3</sup>/g and 3.28&#xa0;MPa, respectively. This result indicated that microorganism participated in the degradation of coal reservoir and promoted the production of methane gas, the meso-macropores were more obviously modified by microorganism, so that the pore diameter stabilized, the pores became smoother, the specific surface area decreased, and the pore volume increased. These are more beneficial to the adsorption and production of coalbed methane (CBM) after microbial treatment.</p>
</abstract>
<kwd-group>
<kwd>microbially enhanced coalbed methane (MECBM)</kwd>
<kwd>pore structure</kwd>
<kwd>fractal theory</kwd>
<kwd>coalbed methane</kwd>
<kwd>qinshui basin</kwd>
</kwd-group>
</article-meta>
</front>
<body>
<sec id="s1">
<title>Introduction</title>
<p>Coal, as an important energy resource, has been widely used since the industrial revolution. Approximately 71.4% of global fossil fuel reserves are in the form of coal (<xref ref-type="bibr" rid="B9">Faison, 1991</xref>; <xref ref-type="bibr" rid="B23">Park and Liang, 2016</xref>). However, a series of severe environmental problems have resulted, such as global climate change, extreme weather and land desertification. These problems have seriously affected and restricted the sustainable development of humankind with the development and utilization of coal resources (<xref ref-type="bibr" rid="B11">Fakoussa and Hofrichter, 1999</xref>; <xref ref-type="bibr" rid="B12">Formolo et al., 2008</xref>; <xref ref-type="bibr" rid="B4">Byamba-Ochir et al., 2017</xref>; <xref ref-type="bibr" rid="B26">Su et al., 2021</xref>). Exploitation and utilization of coalbed methane (CBM) is of great significance to alleviate these problems. CBM is developed by way of two processes: thermogenic gasification and biogenetic gasification, so it is possible to obtain CBM in artificial conditions through microbial degradation (<xref ref-type="bibr" rid="B11">Fakoussa and Hofrichter, 1999</xref>; <xref ref-type="bibr" rid="B23">Park and Liang, 2016</xref>). Microbially enhanced coalbed methane (MECBM) has important theoretical and practical significance for reforming coal reservoir structure, alleviating greenhouse effect and energy crises and developing new sources of clean energy (<xref ref-type="bibr" rid="B30">Zhang et al., 2017</xref>; <xref ref-type="bibr" rid="B20">Lu et al., 2020</xref>; <xref ref-type="bibr" rid="B16">Hou et al., 2021</xref>). Meanwhile, the permeability of coal reservoir can be improved by using MECBM. This technique is believed to be related to low metamorphic coal, which is more conducive to microbial degradation (<xref ref-type="bibr" rid="B15">Harris et al., 2008</xref>; <xref ref-type="bibr" rid="B25">Robbins et al., 2016</xref>; <xref ref-type="bibr" rid="B20">Lu et al., 2020</xref>), but the bituminous-coal contents in some countries (such as the United States, Russia, and China) exceed 50% (<xref ref-type="bibr" rid="B21">Mcglade and Ekins, 2015</xref>; <xref ref-type="bibr" rid="B20">Lu et al., 2020</xref>). Especially in China, commercial CBM gas fields are mainly concentrated in anthracite coal mining areas. Therefore, MECBM research should not only focus on lignite, and but also highly metamorphosed bituminous coal, or even anthracite (<xref ref-type="bibr" rid="B20">Lu et al., 2020</xref>), many scholars have investigated this topic (<xref ref-type="bibr" rid="B10">Faiz and Hendry, 2006</xref>; <xref ref-type="bibr" rid="B12">Formolo et al., 2008</xref>; <xref ref-type="bibr" rid="B28">Boris et al., 2012</xref>; <xref ref-type="bibr" rid="B3">Bao et al., 2020</xref>; <xref ref-type="bibr" rid="B32">Zhao et al., 2020</xref>; <xref ref-type="bibr" rid="B1">Ashley et al., 2021</xref>; <xref ref-type="bibr" rid="B14">Guo et al., 2021</xref>). As a porous medium, the pores of coal are the main accumulation space and migration channels of CBM, and the pore structure not only affects the state of occurrence, adsorption/desorption, diffusion, seepage flow, gas content, but also restricts the ability to exploit CBM (<xref ref-type="bibr" rid="B17">Hudot, 1966</xref>; <xref ref-type="bibr" rid="B7">Clarkson et al., 2011</xref>; <xref ref-type="bibr" rid="B22">Moore, 2012</xref>; <xref ref-type="bibr" rid="B13">Gao et al., 2017</xref>; <xref ref-type="bibr" rid="B5">Chen et al., 2018</xref>), making it necessary to study the modification of coal pore structures by microorganisms.</p>
</sec>
<sec sec-type="materials|methods" id="s2">
<title>Materials and Methods</title>
<sec id="s2-1">
<title>Coal Samples</title>
<p>The No. 3 coal seams of Early Permian Shanxi formation in Sihe mine, in the southern Qinshui basin of China were taken as research objects to study the pore structure characteristics after microbial treatment. These are typical primary mineable coal beds found in northern China. The study area lies in the southeast of Shanxi Province and forms a part to the western margin of North China Platform. The average thickness of No. 3 coal seam is about 6&#xa0;m and <italic>R</italic>
<sub>o, Max.</sub> is 2.54%. The research area is a focus of CBM research in China, and is the earliest and most successful commercialization area of the CBM industry in China. To maintain the contact between the coal and microorganisms as much as possible, while avoiding the channels becoming blocked by pulverized coal, the particle size of the granular coal specimens was about 20 &#xd7; 20&#xa0;mm and a coal sample of 18&#xa0;kg was loaded into each experimental device. Proximate analysis, low-temperature nitrogen adsorption (LTNA), mercury porosimetry (MP) and isothermal adsorption measurements, and field emission scanning electron microscopy (FESEM) were applied to pre-test/post-test samples. Two sets of experimental devices were designed (<xref ref-type="fig" rid="F1">Figure 1</xref>). The test data are summarized in <xref ref-type="table" rid="T1">Table 1</xref>.</p>
<fig id="F1" position="float">
<label>FIGURE 1</label>
<caption>
<p>Experimental devices used to test MECBM.</p>
</caption>
<graphic xlink:href="feart-10-869917-g001.tif"/>
</fig>
<table-wrap id="T1" position="float">
<label>TABLE 1</label>
<caption>
<p>Coal sample data.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th align="left">Sample ID</th>
<th align="center">M<sub>ad</sub> (%)</th>
<th align="center">A<sub>d</sub> (%)</th>
<th align="center">V<sub>daf</sub> (%)</th>
<th align="center">FC<sub>ad</sub> (%)</th>
<th align="center">Clay minerals</th>
<th align="center">BET surface area m<sup>2</sup>/g, LTNA)</th>
<th align="center">Pore volume cm<sup>3</sup>/g, LTNA)</th>
<th align="center">Total pore area m<sup>2</sup>/g, MP)</th>
<th align="center">Total intrusion volume cm<sup>3</sup>/g, MP)</th>
<th align="center">Langmuir volume V<sub>L</sub>/(cm<sup>3</sup>/g)</th>
<th align="center">Langmuirpressure P<sub>L</sub>/MPa</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="left">Pretest</td>
<td align="char" char=".">2.99</td>
<td align="char" char=".">13.13</td>
<td align="char" char=".">6.68</td>
<td align="char" char=".">78.63</td>
<td align="char" char=".">4.13</td>
<td align="char" char=".">1.791</td>
<td align="char" char=".">0.0018</td>
<td align="char" char=".">5.398</td>
<td align="char" char=".">0.0530</td>
<td align="char" char=".">34.84</td>
<td align="char" char=".">2.73</td>
</tr>
<tr>
<td align="left">Posttest1</td>
<td align="char" char=".">5.58</td>
<td align="char" char=".">16.34</td>
<td align="char" char=".">5.42</td>
<td align="char" char=".">74.70</td>
<td align="char" char=".">6.33</td>
<td align="char" char=".">6.365</td>
<td align="char" char=".">0.0050</td>
<td align="char" char=".">5.434</td>
<td align="char" char=".">0.0709</td>
<td align="char" char=".">36.45</td>
<td align="char" char=".">3.31</td>
</tr>
<tr>
<td align="left">Posttest2</td>
<td align="char" char=".">5.48</td>
<td align="char" char=".">14.96</td>
<td align="char" char=".">4.76</td>
<td align="char" char=".">76.55</td>
<td align="char" char=".">8.41</td>
<td align="char" char=".">1.648</td>
<td align="char" char=".">0.0051</td>
<td align="char" char=".">5.058</td>
<td align="char" char=".">0.0543</td>
<td align="char" char=".">36.23</td>
<td align="char" char=".">3.24</td>
</tr>
</tbody>
</table>
<table-wrap-foot>
<fn>
<p>M<sub>ad</sub>, moisture content, air dried basis; A<sub>d</sub>, ash yield, dry basis; V<sub>daf</sub>, volatile matter, dry ash-free basis; FC<sub>ad</sub>, fixed carbon; BET, Brunauer-Emmett-Teller multi-molecular adsorption formula; LTNA, low-temperature nitrogen adsorption; MP, Mercury porosimetry.</p>
</fn>
</table-wrap-foot>
</table-wrap>
</sec>
<sec id="s2-2">
<title>Experimental Procedure</title>
<p>The MECBM treatments were performed using specially designed apparatus (<xref ref-type="fig" rid="F1">Figure 1</xref>). The flora and experimental water were taken from CBM wells in the Sihe mine. The floras were cultured in the laboratory. To ensure the enrichment of methanogens in water samples, fluorescence observation and counting were performed before the experiment under a fluorescence microscope with 420&#xa0;nm incident light. Preparation of 10&#xa0;L of substrate was carried out, and the components mainly included glucose, peptone, sodium chloride, beef extract, <sc>l</sc>-cysteine hydrochloride, resazurin, sodium bicarbonate, and sodium sulfide. The experiment lasted for 47&#xa0;days (until 72&#xa0;h no gas production was noted). Two experimental devices produced 10,449 and 11,120&#xa0;ml of gas respectively, of which the methane content was 4,013 and 4,583&#xa0;ml.</p>
</sec>
<sec id="s2-3">
<title>Test Methods</title>
<p>An Automatic Proximate Analysis Instrument was used to perform proximate analysis (the moisture, ash, and volatile and fixed carbon contents) experiments, as per ISO 17246-2010. A Micromeritics ASAP-2020 automated surface area analyzer (United States) was adopted to perform the low-temperature nitrogen adsorption/desorption experiments, as per the ISO 15901.2-2006 test method over a pore diameter analysis range of 0.35&#x2013;300&#xa0;nm. An Automated Isothermal Gas Adsorption/Desorption Experiment System TerraTek ISO-300 (United States) was used to conduct the isothermal adsorption/desorption experiments, as per Chinese National Standard GB/T 19560-2008. All the above tests were completed at the State Key Laboratory of Coal and Coalbed Methane Co-Extraction in China. A Micromeritics Autopore IV 9500 Instrument (United States) was used to perform mercury porosimetry experiments, according to the ISO 15901-1-2005 test method, the particle size of the coal sample used was 4.75&#x2013;3.35&#xa0;mm over a pore-diameter analysis range of 7.5&#xa0;nm&#x2013;360&#xa0;&#x3bc;m. The pore characteristics of coal and methanobacteria were observed under FEI Quanta 250 FEG (United States) field emission scanning electron microscopy (these two tests were conducted at Henan Polytechnic University in China).</p>
</sec>
</sec>
<sec sec-type="results|discussion" id="s3">
<title>Results and Discussion</title>
<sec id="s3-1">
<title>Pore Properties</title>
<p>In this study, the following Xo&#x434;ot criteria developed in the former USSR were adopted: the pores in a coal specimen were divided into: micropores (&#x3c;10&#xa0;nm), minipores (10&#x2013;100&#xa0;nm), mesopores (100&#x2013;1,000&#xa0;nm), and macropores (&#x3e;1,000&#xa0;nm) (<xref ref-type="bibr" rid="B17">Hudot, 1966</xref>; <xref ref-type="bibr" rid="B6">Cheng et al., 2021</xref>).</p>
<p>From the distribution of specific surface area (<xref ref-type="fig" rid="F2">Figure 2</xref>), the specific surface area of coal samples comprised mostly micropores and minipores. The specific surface area of micropores and minipores of coal samples increased from 93.6% to 97.8% and 96.5% after bioconversion under LTNA test conditions, and the specific surface of micropores and micropores of coal samples decreased from 99.7 % to 99.5% under mercury injection test conditions. From <xref ref-type="fig" rid="F3">Figures 3</xref>, <xref ref-type="fig" rid="F4">4A</xref>,<xref ref-type="fig" rid="F3">4B</xref>, the specific surface area of micropores of coal samples was found to increase significantly after bioconversion, while that of the minipores increased slightly, and the overall specific surface area increased from 1.79 to 4.01&#xa0;m<sup>2</sup>/g on average after LTNA testing; however, the overall specific surface area decreased slightly, from 5.398 to 5.246&#xa0;m<sup>2</sup>/g under mercury injection test conditions.</p>
<fig id="F2" position="float">
<label>FIGURE 2</label>
<caption>
<p>Percentage of specific surface area and pore volume in each pore size interval (left panel: LTNA; right panel: MP). S1&#x223c;S3 and V1&#x223c;V3 are specific surface area ratios and the pore volume ratios of micropores, minipores, and meso-macropores, respectively.</p>
</caption>
<graphic xlink:href="feart-10-869917-g002.tif"/>
</fig>
<fig id="F3" position="float">
<label>FIGURE 3</label>
<caption>
<p>Specific surface area and pore volume distribution characteristics based on pore distribution change according to LTNA measurements for <bold>(A) (C) (E)</bold> and MP measurements for <bold>(B) (D) (F)</bold>; the left ordinate is the incremental pore area (m<sup>2</sup>/g) and the right ordinate denotes the incremental pore volume cm<sup>3</sup>/g).</p>
</caption>
<graphic xlink:href="feart-10-869917-g003.tif"/>
</fig>
<fig id="F4" position="float">
<label>FIGURE 4</label>
<caption>
<p>The changes in specific surface area and pore volume based on pore size change [<bold>(A,C)</bold>: LTNA; <bold>(B,D)</bold>: MP].</p>
</caption>
<graphic xlink:href="feart-10-869917-g004.tif"/>
</fig>
<p>Different from the specific surface area, the contribution of pore volume arose mainly from minipores, mesopores, and macropores (<xref ref-type="fig" rid="F3">Figure 3</xref>), the contribution of meso-macropores increased from 72.4 % to 76.7% and 73.1% after bioconversion under MP test conditions (<xref ref-type="fig" rid="F2">Figure 2</xref>). The contribution of micropores to the pore volume increased from 4.34 % to 18.0% and 12.98% under the LTNA test, although the contribution of micropores to the increase in pore volume after the experiment was large, the proportion of micropores to the increase in the pore volume remained small. As can be seen from <xref ref-type="fig" rid="F4">Figures 4C,D</xref>, the pore volume of coal samples increased from 0.0018&#xa0;cm<sup>3</sup>/g (LTNA) and 0.0530&#xa0;cm<sup>3</sup>/g (MP) before testing to 0.0051&#xa0;cm<sup>3</sup>/g (LTNA) and 0.0626&#xa0;cm<sup>3</sup>/g (MP) after testing in LTNA and MP conditions, respectively (<xref ref-type="table" rid="T1">Table 1</xref>).</p>
<p>The differences in the data of specific surface area and pore volume between the LTNA and MP tests methods are mainly based on two reasons: one is that MP focuses on macropores and mesopores, while LTNA is more advantageous for micropores and minipores; the other is that according to the experimental results, microbial modification of mesopores is greater, which reduces the specific surface area of mesopores and increases the pore volume.</p>
</sec>
<sec id="s3-2">
<title>Surface Fractal Dimension</title>
<p>The pore structure of coal has strong heterogeneity and anisotropy, with fractal characteristics (<xref ref-type="bibr" rid="B30">Zhang et al., 2017</xref>), therefore, the fractal dimension is often used to quantify and characterize the pore structure in coal reservoirs (<xref ref-type="bibr" rid="B27">Wang et al., 2021</xref>). In this study, the Frenkel-Halsey-Hill (FHH) fractal model was used to estimate the fractal dimension from the LTNA data. The FHH equation can be expressed as (<xref ref-type="bibr" rid="B19">Lowell et al., 2004</xref>; <xref ref-type="bibr" rid="B31">Zhang et al., 2014</xref>):<disp-formula id="e1">
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<mml:mrow>
<mml:mrow>
<mml:mo>(</mml:mo>
<mml:mrow>
<mml:mi>D</mml:mi>
<mml:mo>&#x2212;</mml:mo>
<mml:mn>3</mml:mn>
</mml:mrow>
<mml:mo>)</mml:mo>
</mml:mrow>
</mml:mrow>
<mml:mo>/</mml:mo>
<mml:mn>3</mml:mn>
</mml:mrow>
</mml:mrow>
</mml:math>
<label>(2)</label>
</disp-formula>
<disp-formula id="e3">
<mml:math id="m3">
<mml:mrow>
<mml:mtext>Or&#xa0;</mml:mtext>
<mml:mi>A</mml:mi>
<mml:mo>&#x3d;</mml:mo>
<mml:mi>D</mml:mi>
<mml:mo>&#x2212;</mml:mo>
<mml:mn>3</mml:mn>
</mml:mrow>
</mml:math>
<label>(3)</label>
</disp-formula>where <inline-formula id="inf1">
<mml:math id="m4">
<mml:mi>v</mml:mi>
</mml:math>
</inline-formula> is the sorption capacity; <inline-formula id="inf2">
<mml:math id="m5">
<mml:mrow>
<mml:msub>
<mml:mi>v</mml:mi>
<mml:mi>o</mml:mi>
</mml:msub>
</mml:mrow>
</mml:math>
</inline-formula> denotes the volume of monolayer coverage; <italic>D</italic> is the fractal dimension; <italic>A</italic> represents the pre-exponential factor, which is dependent on <italic>D</italic>; <italic>P</italic>
<sub>0</sub> is the saturated vapor pressure; <italic>C</italic> is a constant.</p>
<p>According to <xref ref-type="disp-formula" rid="e1">Eq. 1</xref>, there must be a linear relationship between ln <italic>V</italic> and ln (ln (<italic>P</italic>
<sub>0</sub>/<italic>P</italic>)) when the pores have fractal characteristics. As can be seen from <xref ref-type="fig" rid="F5">Figure 5</xref>, the bilogarithmic coordinates show a significant linear relationship, indicating that the pores of coal samples can be characterized by fractal theory. It is noteworthy that there are two different formulae available for calculating <italic>D</italic> with <italic>A</italic> based on the different situations: <xref ref-type="disp-formula" rid="e2">Eq. 2</xref>,<xref ref-type="disp-formula" rid="e3">3</xref> (<xref ref-type="bibr" rid="B24">Pfeifer and Avnir, 1984</xref>; <xref ref-type="bibr" rid="B2">Avnir and Jaroniec, 1989</xref>; <xref ref-type="bibr" rid="B18">Ismail and Pfeifer, 1994</xref>; <xref ref-type="bibr" rid="B29">Yao et al., 2008</xref>; <xref ref-type="bibr" rid="B8">Dou et al., 2021</xref>). <xref ref-type="disp-formula" rid="e2">Eq. 2</xref> is applicable to the membrane/gas interface controlled by van der Waals force, and <xref ref-type="disp-formula" rid="e3">Eq. 3</xref> is applicable to the interface controlled by liquid&#x2013;gas tension. In this study, many of these <italic>D</italic> values are less than 2 as calculated using <xref ref-type="disp-formula" rid="e2">Eq. 2</xref>, which is unrealistic, so <italic>D</italic> is calculated using <xref ref-type="disp-formula" rid="e3">Eq. 3</xref> (<xref ref-type="table" rid="T2">Table 2</xref>).</p>
<fig id="F5" position="float">
<label>FIGURE 5</label>
<caption>
<p>Relationship between ln <italic>V</italic> and ln (ln (<italic>P</italic>
<sub>
<italic>0</italic>
</sub>
<italic>/P</italic>)) based on LTNA.</p>
</caption>
<graphic xlink:href="feart-10-869917-g005.tif"/>
</fig>
<table-wrap id="T2" position="float">
<label>TABLE 2</label>
<caption>
<p>Fractal dimension calculations based on the FHH model.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th rowspan="2" align="left">Sample ID</th>
<th colspan="3" align="center">d &#x2264; 10&#xa0;nm</th>
<th colspan="3" align="center">10&#xa0;nm &#x3c; d &#x3c; 100&#xa0;nm</th>
<th colspan="3" align="center">d &#x2265; 100&#xa0;nm</th>
</tr>
<tr>
<th align="center">
<italic>A</italic>
</th>
<th align="center">
<italic>D</italic>
</th>
<th align="center">
<italic>R</italic>
<sup>2</sup>
</th>
<th align="center">
<italic>A</italic>
</th>
<th align="center">
<italic>D</italic>
</th>
<th align="center">
<italic>R</italic>
<sup>2</sup>
</th>
<th align="center">
<italic>A</italic>
</th>
<th align="center">
<italic>D</italic>
</th>
<th align="center">
<italic>R</italic>
<sup>2</sup>
</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="left">Pretest</td>
<td align="char" char=".">&#x2212;0.2708</td>
<td align="char" char=".">2.7292</td>
<td align="char" char=".">0.84</td>
<td align="char" char=".">&#x2212;0.4016</td>
<td align="char" char=".">2.5984</td>
<td align="char" char=".">1.0</td>
<td align="char" char=".">&#x2212;0.1010</td>
<td align="char" char=".">2.899</td>
<td align="char" char=".">1.0</td>
</tr>
<tr>
<td align="left">Posttest1</td>
<td align="char" char=".">&#x2212;0.0606</td>
<td align="char" char=".">2.9394</td>
<td align="char" char=".">0.87</td>
<td align="char" char=".">&#x2212;0.1251</td>
<td align="char" char=".">2.8749</td>
<td align="char" char=".">0.99</td>
<td align="char" char=".">&#x2212;0.1238</td>
<td align="char" char=".">2.8762</td>
<td align="char" char=".">1.0</td>
</tr>
<tr>
<td align="left">Posttest2</td>
<td align="char" char=".">&#x2212;0.1606</td>
<td align="char" char=".">2.8394</td>
<td align="char" char=".">0.99</td>
<td align="char" char=".">&#x2212;0.2522</td>
<td align="char" char=".">2.7478</td>
<td align="char" char=".">1.0</td>
<td align="char" char=".">&#x2212;0.1791</td>
<td align="char" char=".">2.8209</td>
<td align="char" char=".">0.99</td>
</tr>
</tbody>
</table>
</table-wrap>
<p>To study the effect of microbial action on pore structure of coal, the data are divided into three regions to calculate the fractal dimension, <italic>d</italic> &#x2264; 10&#xa0;nm, 10&#xa0;nm &#x3c; <italic>d</italic> &#x3c; 100&#xa0;nm, <italic>d</italic> &#x2265; 100&#xa0;nm. The fractal results showed that when <italic>d</italic> &#x2264; 10&#xa0;nm, the fractal dimension of coal after microbial treatment was increased from 2.73 to 2.89, when 10&#xa0;nm &#x3c; <italic>d</italic> &#x3c; 100&#xa0;nm, the fractal dimension <italic>D</italic> was increased from 2.60 to 2.81, however, when <italic>d</italic> &#x2265; 100&#xa0;nm, the fractal dimension <italic>D</italic> was reduced from 2.90 to 2.85, The results indicated that the surface irregularities of mesopores and macropores decreased, the pores became smoother and the pore volume decreased after the bioconversion (<xref ref-type="fig" rid="F6">Figure 6</xref>). This finding was consistent with the aforementioned research (the pore structure evolution model is shown in <xref ref-type="fig" rid="F7">Figure 7</xref>).</p>
<fig id="F6" position="float">
<label>FIGURE 6</label>
<caption>
<p>SEM image of spherical microbial attachment to the coal after microbial treatment.</p>
</caption>
<graphic xlink:href="feart-10-869917-g006.tif"/>
</fig>
<fig id="F7" position="float">
<label>FIGURE 7</label>
<caption>
<p>A conceptual pore structure evolution model with microbial treatment. <bold>(A)</bold> Pore structure before microbial treatment. <bold>(B)</bold> Pore structure after microbial treatment.</p>
</caption>
<graphic xlink:href="feart-10-869917-g007.tif"/>
</fig>
</sec>
<sec id="s3-3">
<title>Proximate Analysis and Adsorption Characteristics</title>
<p>From the perspective of industrial analysis (<xref ref-type="table" rid="T1">Table 1</xref>), compared with pre-test values, the moisture content, ash yield, and clay content of coal samples increased from 2.99%, 13.13 % and 4.13%&#x2013;5.53%, 15.65 % and 7.37%, respectively, while the volatile matter and fixed carbon contents reduced from 6.68%, 78.63 %&#x2013;5.09% and 75.63%, respectively. This showed that microorganisms participated in the degradation of coal reservoir and promoted the generation of methane gas.</p>
<p>The curves of the methane adsorption on samples can be drawn according to the Langmuir model <xref ref-type="disp-formula" rid="e4">Eq. 4</xref>:<disp-formula id="e4">
<mml:math id="m6">
<mml:mrow>
<mml:mtext>V</mml:mtext>
<mml:mo>&#x3d;</mml:mo>
<mml:mfrac>
<mml:mrow>
<mml:msub>
<mml:mi>v</mml:mi>
<mml:mi>L</mml:mi>
</mml:msub>
<mml:mi>P</mml:mi>
</mml:mrow>
<mml:mrow>
<mml:msub>
<mml:mi>P</mml:mi>
<mml:mi>L</mml:mi>
</mml:msub>
<mml:mo>&#x2b;</mml:mo>
<mml:mi>P</mml:mi>
</mml:mrow>
</mml:mfrac>
</mml:mrow>
</mml:math>
<label>(4)</label>
</disp-formula>where <italic>V</italic> is the adsorption volume, <italic>V</italic>
<sub>L</sub> denotes the Langmuir volume, <inline-formula id="inf3">
<mml:math id="m7">
<mml:mi>P</mml:mi>
</mml:math>
</inline-formula> is the equilibrium pressure, <italic>P</italic>
<sub>L</sub> is the Langmuir pressure (<xref ref-type="bibr" rid="B30">Zhang et al., 2017</xref>; <xref ref-type="bibr" rid="B5">Chen et al., 2018</xref>). It can be concluded from <xref ref-type="fig" rid="F8">Figure 8</xref> that the Langmuir volume was increased after bioconversion, from 34.84 to 36.34&#xa0;cm<sup>3</sup>/g (mean average), and the Langmuir pressure was increased from 2.73 to 3.28&#xa0;MPa (mean average) after bioconversion based on the isothermal methane adsorption experimental data (<xref ref-type="table" rid="T1">Table 1</xref>). This result showed that transformation of coal by microorganisms is more beneficial to the adsorption and production of CBM.</p>
<fig id="F8" position="float">
<label>FIGURE 8</label>
<caption>
<p>Curves of methane isothermal adsorption on samples.</p>
</caption>
<graphic xlink:href="feart-10-869917-g008.tif"/>
</fig>
</sec>
</sec>
<sec sec-type="conclusion" id="s4">
<title>Conclusion</title>
<p>In this study, No. 3 coal seams in Qinshui Basin were taken as the research objects to observe the pore structure characteristics after microbial treatment, and the following conclusions can be drawn.</p>
<p>The contribution of micropores and minipores to the specific surface area of coal samples reached more than 93%, and the contribution was further increased after microbial treatment. After bioconversion, the specific surface area increased from 1.79 to 4.01&#xa0;m<sup>2</sup>/g under LTNA test conditions, while the specific surface area decreased from 5.398 to 5.246&#xa0;m<sup>2</sup>/g under MP test conditions. The fractal dimension of micropores and minipores increased from 2.73 and 2.60 to 2.89 and 2.81, respectively, but the fractal dimension of meso-macropores decreased from 2.90 to 2.85.</p>
<p>The pore volume of coal samples arose mainly from minipores, mesopores, and macropores, and the contribution of minipores, mesopores, and macropores to the increase in the pore volume was more than 70%. The pore volume of coal samples increased from 0.0018&#xa0;cm<sup>3</sup>/g to 0.0530&#xa0;cm<sup>3</sup>/g to 0.0051&#xa0;cm<sup>3</sup>/g to 0.0626&#xa0;cm<sup>3</sup>/g after testing under LTNA and MP test conditions, respectively.</p>
<p>The volatile matter and fixed carbon were both reduced from 6.68 % to 78.63% to 5.09 % to 75.63%, and the Langmuir volume and Langmuir pressure increased from 34.84&#xa0;cm<sup>3</sup>/g and 2.73&#xa0;MPa to 36.34&#xa0;cm<sup>3</sup>/g and 3.28&#xa0;MPa, respectively.</p>
<p>The results demonstrated that microorganism participated in the degradation of coal reservoir and promoted the production of methane gas. The meso-macropores were more obviously modified by the microorganisms, so that the pore diameter stabilized, the pores became smoother, the specific surface area decreased, and the pore volume increased. After microbial treatment, the coal body was more conducive to the adsorption of methane gas. The increase of Langmuir pressure was more conducive to the subsequent production of CBM.</p>
</sec>
</body>
<back>
<sec 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>DG searched the literature; DG and BG analyzed the data and wrote the paper; KT and HR treated samples and performed the experiments; HG processed some data and drew some maps.</p>
</sec>
<sec id="s7">
<title>Funding</title>
<p>This work is supported by the National Natural Science Foundation of China (No. 41402094), the Foundation of State Key Laboratory of Petroleum Resources and Prospecting, China University of Petroleum, Beijing (No. PRP/open-2008) and the Fundamental Research Funds for the Universities of Henan Province (No. NSFRF220411).</p>
</sec>
<sec sec-type="COI-statement" id="s8">
<title>Conflict of Interest</title>
<p>The authors declare that the research was conducted in the absence of any commercial or financial relationships that could be construed as a potential conflict of interest.</p>
</sec>
<sec sec-type="disclaimer" id="s9">
<title>Publisher&#x2019;s Note</title>
<p>All claims expressed in this article are solely those of the authors and do not necessarily represent those of their affiliated organizations, or those of the publisher, the editors and the reviewers. Any product that may be evaluated in this article, or claim that may be made by its manufacturer, is not guaranteed or endorsed by the publisher.</p>
</sec>
<ack>
<p>We thank all the staff of the State Key Laboratory of Coal and Coalbed Methane Co-mining, especially Professor Baoyu Wang and Bin Hu, they put forward the research direction and provide a good experimental environment. Special thanks are given to the reviewers for their valuable advice and comments on the manuscript.</p>
</ack>
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