<?xml version="1.0" encoding="UTF-8"?>
<!DOCTYPE article PUBLIC "-//NLM//DTD Journal Publishing DTD v2.3 20070202//EN" "journalpublishing.dtd">
<article article-type="research-article" dtd-version="2.3" xml:lang="EN" xmlns:mml="http://www.w3.org/1998/Math/MathML" xmlns:xlink="http://www.w3.org/1999/xlink">
<front>
<journal-meta>
<journal-id journal-id-type="publisher-id">Front. Bioeng. Biotechnol.</journal-id>
<journal-title>Frontiers in Bioengineering and Biotechnology</journal-title>
<abbrev-journal-title abbrev-type="pubmed">Front. Bioeng. Biotechnol.</abbrev-journal-title>
<issn pub-type="epub">2296-4185</issn>
<publisher>
<publisher-name>Frontiers Media S.A.</publisher-name>
</publisher>
</journal-meta>
<article-meta>
<article-id pub-id-type="publisher-id">1119111</article-id>
<article-id pub-id-type="doi">10.3389/fbioe.2022.1119111</article-id>
<article-categories>
<subj-group subj-group-type="heading">
<subject>Bioengineering and Biotechnology</subject>
<subj-group>
<subject>Original Research</subject>
</subj-group>
</subj-group>
</article-categories>
<title-group>
<article-title>Effects of different bicarbonate on <italic>spirulina</italic> in CO<sub>2</sub> absorption and microalgae conversion hybrid system</article-title>
<alt-title alt-title-type="left-running-head">Zhang 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.2022.1119111">10.3389/fbioe.2022.1119111</ext-link>
</alt-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname>Zhang</surname>
<given-names>Pengyu</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
</xref>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Sun</surname>
<given-names>Qian</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
</xref>
</contrib>
<contrib contrib-type="author">
<name>
<surname>Dong</surname>
<given-names>Ye</given-names>
</name>
<xref ref-type="aff" rid="aff1">
<sup>1</sup>
</xref>
</contrib>
<contrib contrib-type="author" corresp="yes">
<name>
<surname>Lian</surname>
<given-names>Shaohan</given-names>
</name>
<xref ref-type="aff" rid="aff2">
<sup>2</sup>
</xref>
<xref ref-type="corresp" rid="c001">&#x2a;</xref>
<uri xlink:href="https://loop.frontiersin.org/people/2128967/overview"/>
</contrib>
</contrib-group>
<aff id="aff1">
<sup>1</sup>
<institution>Tianjin Building Materials Science Research Academy Co. Ltd</institution>, <addr-line>Tianjin</addr-line>, <country>China</country>
</aff>
<aff id="aff2">
<sup>2</sup>
<institution>Tianjin Key Laboratory of Indoor Air Environmental Quality Control</institution>, <institution>School of Environmental Science and Engineering</institution>, <institution>Tianjin University</institution>, <addr-line>Tianjin</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/1122377/overview">Wangbiao Guo</ext-link>, Yale University, United States</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/1772680/overview">Qing Ye</ext-link>, Soochow University, China</p>
<p>
<ext-link ext-link-type="uri" xlink:href="https://loop.frontiersin.org/people/2133076/overview">Weiwei Huang</ext-link>, Hainan University, China</p>
<p>
<ext-link ext-link-type="uri" xlink:href="https://loop.frontiersin.org/people/817451/overview">Wenli Huang</ext-link>, Nankai University, China</p>
<p>
<ext-link ext-link-type="uri" xlink:href="https://loop.frontiersin.org/people/2133753/overview">Yanmei Song</ext-link>, China Huaneng Group Clean Energy Research Institute, China</p>
</fn>
<corresp id="c001">&#x2a;Correspondence: Shaohan Lian, <email>shaohan_lian@163.com</email>
</corresp>
<fn fn-type="other">
<p>This article was submitted to Industrial Biotechnology, a section of the journal Frontiers in Bioengineering and Biotechnology</p>
</fn>
</author-notes>
<pub-date pub-type="epub">
<day>06</day>
<month>01</month>
<year>2023</year>
</pub-date>
<pub-date pub-type="collection">
<year>2022</year>
</pub-date>
<volume>10</volume>
<elocation-id>1119111</elocation-id>
<history>
<date date-type="received">
<day>08</day>
<month>12</month>
<year>2022</year>
</date>
<date date-type="accepted">
<day>20</day>
<month>12</month>
<year>2022</year>
</date>
</history>
<permissions>
<copyright-statement>Copyright &#xa9; 2023 Zhang, Sun, Dong and Lian.</copyright-statement>
<copyright-year>2023</copyright-year>
<copyright-holder>Zhang, Sun, Dong and Lian</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>According to the characteristics of power plant flue gas emission and the requirements of reducing CO<sub>2</sub> capture cost. CO<sub>2</sub> absorption hybrid with microalgae conversion (CAMC) can avoid the challenges of heat consumption during absorbent desorption and nutrient consumption during microalgae culture. In this study, the bicarbonate solution (represents the products of CO<sub>2</sub> absorption by Na<sub>2</sub>CO<sub>3</sub> and K<sub>2</sub>CO<sub>3</sub>) is used as carbon source for mutagenic <italic>Spirulina platensis</italic> cultivation, and different concentrations of bicarbonate were set to explore the best carbon source. The results showed that NaHCO<sub>3</sub> was a better medium for the CO<sub>2</sub> absorption hybrid with microalgae conversion system, which was beneficial for the growth of mutagenic <italic>Spirulina</italic>, compared with K<sub>2</sub>CO<sub>3</sub>. When .3&#xa0;mol/L NaHCO<sub>3</sub> was added to the CO<sub>2</sub> absorption hybrid with microalgae conversion system, the highest biomass dry weight, carbon fixation rate and carbon utilization efficiency were obtained, which were 2.24&#xa0;g/L, 230.36&#xa0;mg/L/d and 26.71%, respectively. In addition, .3&#xa0;mol/L NaHCO<sub>3</sub> was conducive to protein synthesis, reaching 1,625.68&#xa0;mg/L. This study provided a feasible idea for power system to achieve carbon neutrality in the future.</p>
</abstract>
<kwd-group>
<kwd>Spirulina platensis</kwd>
<kwd>CO<sub>2</sub> absorption</kwd>
<kwd>NaHCO<sub>3</sub>
</kwd>
<kwd>KHCO<sub>3</sub>
</kwd>
<kwd>CO<sub>2</sub> absorption hybrid with microalgae conversion</kwd>
</kwd-group>
<contract-num rid="cn001">21878228</contract-num>
<contract-num rid="cn002">2017YFE0127200</contract-num>
<contract-sponsor id="cn001">National Natural Science Foundation of China<named-content content-type="fundref-id">10.13039/501100001809</named-content>
</contract-sponsor>
<contract-sponsor id="cn002">National Key Research and Development Program of China<named-content content-type="fundref-id">10.13039/501100012166</named-content>
</contract-sponsor>
</article-meta>
</front>
<body>
<sec id="s1">
<title>1 Introduction</title>
<p>Nowadays, climate change caused by fossil fuel utilization has attracted more and more attention. As one of the largest carbon emission countries, China has claimed to achieve carbon peaking and carbon neutrality in 2030 and 2060, respectively. To realize these targets, CO<sub>2</sub> capture, storage and utilization (CCUS) has been recognized as an important strategy (<xref ref-type="bibr" rid="B11">Ju et al., 2012</xref>; <xref ref-type="bibr" rid="B12">Kanno et al., 2017</xref>; <xref ref-type="bibr" rid="B13">Khoo et al., 2019</xref>). According to data from the International Energy Agency (IEA), the power sector accounts for nearly two-thirds of the increase in energy-related CO<sub>2</sub> emissions, with more than 10&#xa0;Gt CO<sub>2</sub> from coal. CO<sub>2</sub> capture and utilization in coal-fired power plants can effectively reduce carbon emissions in the power generation industry.</p>
<p>Chemical absorption, physical adsorption, membrane separation, low temperature distillation and microalgae bio-sequestration are commonly used carbon capture technologies (<xref ref-type="bibr" rid="B24">Song C. et al., 2019</xref>). Conventional CO<sub>2</sub> utilization methods include chemical catalytic conversion to prepare chemicals, auxiliary production of petroleum, <italic>etc.</italic> Considering energy consumption and process integrity, the coupling of chemical absorption and biotransformation is a promising solution compared to other capture and utilization technologies (<xref ref-type="bibr" rid="B21">Song et al., 2019b</xref>). Bicarbonate is an intermediate product of conventional CO<sub>2</sub> chemical absorption process and an important carrier of carbon source for microalgae. Therefore, a novel concept to combine CO<sub>2</sub> absorption and microalgae culture, named as CO<sub>2</sub> absorption and microalgae conversion (CAMC) system was proposed (<xref ref-type="bibr" rid="B21">Song et al., 2019b</xref>). The CAMC system with bicarbonate as the link can not only avoid energy consumption in the analytical process, but also solve the nutrient problem in the microalgae culture process, which is an economic and environmentally friendly carbon capture technology (<xref ref-type="bibr" rid="B23">Song et al., 2018</xref>). In CAMC system, the advantages of absorption and bioconversion could be combined and intensify CO<sub>2</sub> capture and utilization efficiency.</p>
<p>The forms of inorganic carbon in medium include CO<sub>2</sub>, CO<sub>3</sub>
<sup>2-</sup>, HCO<sub>3</sub>
<sup>&#x2212;</sup>, H<sub>2</sub>CO<sub>3</sub>, <italic>etc.</italic> However, it should be noted that not every kind of inorganic carbon can be utilized by microalgae, and the two forms of inorganic carbon that <italic>Spirulina</italic> can utilize are CO<sub>2</sub> and HCO<sub>3</sub>
<sup>&#x2212;</sup> (<xref ref-type="bibr" rid="B18">Pereira et al., 2019</xref>; <xref ref-type="bibr" rid="B15">Li et al., 2020</xref>). Compared with green algae, <italic>Spirulina</italic> has strong carbonic anhydrase (CA) activity and higher bicarbonate utilization efficiency (<xref ref-type="bibr" rid="B2">Chang et al., 2013</xref>; <xref ref-type="bibr" rid="B3">Cheng et al., 2017</xref>; <xref ref-type="bibr" rid="B6">de Jesus et al., 2018</xref>). Previous study used different kinds of absorbent to cultivate <italic>Spirulina</italic>, and investigated the growth of microalgae with three initial biomass concentrations in eight concentrations of monoethanolamine (MEA) and three concentrations of sodium hydroxide solutions (<xref ref-type="bibr" rid="B5">da Rosa et al., 2016</xref>). The results showed that the appropriate concentration of MEA did not inhibit the growth of <italic>Spirulina</italic>. Compared with sodium hydroxide, the concentration of inorganic carbon in MEA solution was doubled, and the protein content of <italic>Spirulina</italic> was 17% higher than that obtained by using sodium hydroxide. Therefore, different chemical absorbers could affect the performance of CAMC system. It is necessary to find economic and feasible chemical absorbers to improve the carbon sequestration efficiency of <italic>Spirulina</italic> in CAMC system.</p>
<p>Na<sub>2</sub>CO<sub>3</sub>, K<sub>2</sub>CO<sub>3</sub> are widely used CO<sub>2</sub> absorbers, due to their low toxicity, solvent loss and cost (<xref ref-type="bibr" rid="B9">Fang et al., 2020</xref>). Based on this, NaHCO<sub>3</sub> and KHCO<sub>3</sub>, which could be generated after the full absorption of CO<sub>2</sub> by Na<sub>2</sub>CO<sub>3</sub> and K<sub>2</sub>CO<sub>3</sub>, were selected as the carbon sources for the cultivation of mutagenic <italic>Spirulina</italic>, and different carbon source concentrations (0.1&#xa0;mol/L, .2&#xa0;mol/L and .3&#xa0;mol/L) were also set to get the best absorbent concentration. The effects of different absorbers on biomass and carbon sequestration efficiency of mutagenic <italic>Spirulina</italic> in CAMC system were studied. In addition, the potential value-added components such as protein, lipid and polysaccharide were also measured. CAMC system can provide guidance for the establishment of efficient biorefinery plant to produce high value-added products.</p>
</sec>
<sec sec-type="materials|methods" id="s2">
<title>2 Materials and methods</title>
<sec id="s2-1">
<title>2.1 Microalgae strain</title>
<p>Previous study has shown that <italic>Spirulina</italic> has a developed CO<sub>2</sub> enrichment mechanism (CCM), which can actively pump enough HCO<sub>3</sub>
<sup>&#x2212;</sup> into cells to improve intracellular CO<sub>2</sub> concentration and promote carbon utilization efficiency (<xref ref-type="bibr" rid="B15">Li et al., 2020</xref>). In this study, the used microalgae were mutagenic <italic>Spirulina platensis</italic> which was from Zhejiang University.</p>
</sec>
<sec id="s2-2">
<title>2.2 Experimental procedure</title>
<p>Mutagenic <italic>Spirulina platensis</italic> was initially precultured with Zarrouk medium. After 5&#xa0;days of culture, the mutagenesis <italic>Spirulina platensis</italic> in the logarithmic growth phase was used as inoculum for the formal experiment.</p>
<p>The chemical absorbents selected in this paper were Na<sub>2</sub>CO<sub>3</sub> and K<sub>2</sub>CO<sub>3</sub>, respectively, and the corresponding NaHCO<sub>3</sub> and KHCO<sub>3</sub> were formed after fully absorbing CO<sub>2</sub>. .1&#xa0;mol/L&#x3001;0.2&#xa0;mol/L and .3&#xa0;mol/L NaHCO<sub>3</sub> and KHCO<sub>3</sub> were added to the basal medium as carbon sources, respectively, to investigate the effects of different carbon sources on the growth of mutagenic <italic>Spirulina</italic> in CAMC system, as shown in <xref ref-type="table" rid="T1">Table 1</xref>. Microalgae cultivation was preceded in 250&#xa0;ml serum bottles with 200&#xa0;ml culture medium. The incubator was placed at a constant temperature of 30&#xb0;C &#xb1; 1&#xb0;C and illuminated all day at a light intensity of 4,000&#xa0;Lux. Three parallel experiments were performed in each group and shake the bottle at a set time each day. The biomass, pH, inorganic carbon and other experimental indexes were measured every 3&#xa0;days.</p>
<table-wrap id="T1" position="float">
<label>TABLE 1</label>
<caption>
<p>Batch cultivation condition in CAMC system.</p>
</caption>
<table>
<thead valign="top">
<tr>
<th align="center">Inorganic carbon</th>
<th align="center">Concentration (mol/L)</th>
<th align="left">Group</th>
</tr>
</thead>
<tbody valign="top">
<tr>
<td align="center">NaHCO3</td>
<td align="center">.1</td>
<td align="char" char=".">Na-.1&#xa0;mol/L</td>
</tr>
<tr>
<td align="center">NaHCO3</td>
<td align="center">.2</td>
<td align="left">Na-.2&#xa0;mol/L</td>
</tr>
<tr>
<td align="center">NaHCO3</td>
<td align="center">.3</td>
<td align="center">Na-.3&#xa0;mol/L</td>
</tr>
<tr>
<td align="center">KHCO3</td>
<td align="center">.1</td>
<td align="left">K-.1&#xa0;mol/L</td>
</tr>
<tr>
<td align="center">KHCO3</td>
<td align="center">.2</td>
<td align="left">K-.2&#xa0;mol/L</td>
</tr>
<tr>
<td align="center">KHCO3</td>
<td align="center">.3</td>
<td align="left">K-.3&#xa0;mol/L</td>
</tr>
</tbody>
</table>
</table-wrap>
</sec>
<sec id="s2-3">
<title>2.3 Analytical methods</title>
<p>The standard curve of mutagenic <italic>Spirulina</italic> biomass was obtained based on the linear relationship between dry weight and OD<sub>560</sub>. Firstly, dilute the algae solution with deionized water to OD<sub>560</sub> &#x3d; .2, .4, .6, .8, 1.0, and then measure 100&#xa0;ml, respectively. The filter membrane with a pore size of .45&#xa0;&#x3bc;m was dried in an oven at 105&#xb0;C to a constant weight. Then the filter membrane was weighed and the weight was recorded. The measured 100&#xa0;ml of algae solution was filtered through the membrane, and the membrane was again dried in an oven at 105&#xb0;C to a constant weight and the weight was recorded. The difference between the two membrane weights was the dry weight of mutagenic <italic>Spirulina platensis</italic> biomass. The standard curve was as following:<disp-formula id="e1">
<mml:math id="m1">
<mml:mrow>
<mml:msub>
<mml:mi mathvariant="normal">X</mml:mi>
<mml:mrow>
<mml:mi mathvariant="normal">b</mml:mi>
<mml:mi mathvariant="normal">i</mml:mi>
<mml:mi mathvariant="normal">o</mml:mi>
<mml:mi mathvariant="normal">m</mml:mi>
<mml:mi mathvariant="normal">a</mml:mi>
<mml:mi mathvariant="normal">s</mml:mi>
<mml:mi mathvariant="normal">s</mml:mi>
</mml:mrow>
</mml:msub>
<mml:mo>&#x3d;</mml:mo>
<mml:mn>0.404</mml:mn>
<mml:mo>&#x2022;</mml:mo>
<mml:msub>
<mml:mrow>
<mml:mi mathvariant="normal">O</mml:mi>
<mml:mi mathvariant="normal">D</mml:mi>
</mml:mrow>
<mml:mn>560</mml:mn>
</mml:msub>
<mml:mo>&#x2212;</mml:mo>
<mml:mn>0.0016</mml:mn>
<mml:mo>,</mml:mo>
<mml:msup>
<mml:mi mathvariant="normal">R</mml:mi>
<mml:mn>2</mml:mn>
</mml:msup>
<mml:mo>&#x3d;</mml:mo>
<mml:mn>0.9988</mml:mn>
</mml:mrow>
</mml:math>
<label>(1)</label>
</disp-formula>
</p>
<p>Carbon fixation rate (P<sub>CO2</sub>, mg/L/d) was calculated by referring to (<xref ref-type="bibr" rid="B22">Song et al., 2019c</xref>).<disp-formula id="e2">
<mml:math id="m2">
<mml:mrow>
<mml:msub>
<mml:mi mathvariant="normal">P</mml:mi>
<mml:mrow>
<mml:mi mathvariant="normal">C</mml:mi>
<mml:mi mathvariant="normal">O</mml:mi>
<mml:mn>2</mml:mn>
</mml:mrow>
</mml:msub>
<mml:mrow>
<mml:mfenced open="(" close=")" separators="|">
<mml:mrow>
<mml:mi mathvariant="normal">m</mml:mi>
<mml:mi mathvariant="normal">g</mml:mi>
<mml:mo>/</mml:mo>
<mml:mi mathvariant="normal">L</mml:mi>
<mml:mo>/</mml:mo>
<mml:mi mathvariant="normal">d</mml:mi>
</mml:mrow>
</mml:mfenced>
</mml:mrow>
<mml:mo>&#x3d;</mml:mo>
<mml:msub>
<mml:mi mathvariant="normal">P</mml:mi>
<mml:mrow>
<mml:mi mathvariant="normal">b</mml:mi>
<mml:mi mathvariant="normal">i</mml:mi>
<mml:mi mathvariant="normal">o</mml:mi>
<mml:mi mathvariant="normal">m</mml:mi>
<mml:mi mathvariant="normal">a</mml:mi>
<mml:mi mathvariant="normal">s</mml:mi>
<mml:mi mathvariant="normal">s</mml:mi>
</mml:mrow>
</mml:msub>
<mml:mo>&#xb7;</mml:mo>
<mml:msub>
<mml:mi mathvariant="normal">C</mml:mi>
<mml:mrow>
<mml:mi mathvariant="normal">a</mml:mi>
<mml:mi mathvariant="normal">l</mml:mi>
<mml:mi mathvariant="normal">g</mml:mi>
<mml:mi mathvariant="normal">a</mml:mi>
<mml:mi mathvariant="normal">e</mml:mi>
</mml:mrow>
</mml:msub>
<mml:mo>&#xb7;</mml:mo>
<mml:mrow>
<mml:mfenced open="(" close=")" separators="|">
<mml:mrow>
<mml:msub>
<mml:mi mathvariant="normal">M</mml:mi>
<mml:mrow>
<mml:mi mathvariant="normal">C</mml:mi>
<mml:mi mathvariant="normal">O</mml:mi>
<mml:mn>2</mml:mn>
</mml:mrow>
</mml:msub>
<mml:mo>/</mml:mo>
<mml:msub>
<mml:mi mathvariant="normal">M</mml:mi>
<mml:mi mathvariant="normal">C</mml:mi>
</mml:msub>
</mml:mrow>
</mml:mfenced>
</mml:mrow>
</mml:mrow>
</mml:math>
<label>(2)</label>
</disp-formula>Hereinto, P<sub>biomass</sub> was the biomass yield (mg/L/d), C<sub>algae</sub> was the carbon content in mutagenic <italic>Spirulina</italic>, M<sub>CO2</sub> and M<sub>C</sub> were the molar mass of CO<sub>2</sub> molecule and C atom, respectively.</p>
<p>Carbon utilization efficiency was calculated according to the method mentioned by (<xref ref-type="bibr" rid="B8">Ding et al., 2017</xref>):<disp-formula id="e3">
<mml:math id="m3">
<mml:mrow>
<mml:msub>
<mml:mi mathvariant="normal">E</mml:mi>
<mml:mi mathvariant="normal">C</mml:mi>
</mml:msub>
<mml:mo>&#x3d;</mml:mo>
<mml:mn>100</mml:mn>
<mml:mo>&#xb7;</mml:mo>
<mml:msub>
<mml:mi mathvariant="normal">C</mml:mi>
<mml:mrow>
<mml:mi mathvariant="normal">a</mml:mi>
<mml:mi mathvariant="normal">l</mml:mi>
<mml:mi mathvariant="normal">g</mml:mi>
<mml:mi mathvariant="normal">a</mml:mi>
<mml:mi mathvariant="normal">e</mml:mi>
</mml:mrow>
</mml:msub>
<mml:mo>&#xb7;</mml:mo>
<mml:msub>
<mml:mi mathvariant="normal">X</mml:mi>
<mml:mrow>
<mml:mi mathvariant="normal">b</mml:mi>
<mml:mi mathvariant="normal">i</mml:mi>
<mml:mi mathvariant="normal">o</mml:mi>
<mml:mi mathvariant="normal">m</mml:mi>
<mml:mi mathvariant="normal">a</mml:mi>
<mml:mi mathvariant="normal">s</mml:mi>
<mml:mi mathvariant="normal">s</mml:mi>
</mml:mrow>
</mml:msub>
<mml:mo>/</mml:mo>
<mml:mrow>
<mml:mfenced open="[" close="]" separators="|">
<mml:mrow>
<mml:mn>12</mml:mn>
<mml:mo>/</mml:mo>
<mml:mn>84</mml:mn>
<mml:mo>&#xb7;</mml:mo>
<mml:msub>
<mml:mi mathvariant="normal">D</mml:mi>
<mml:mi mathvariant="normal">C</mml:mi>
</mml:msub>
</mml:mrow>
</mml:mfenced>
</mml:mrow>
</mml:mrow>
</mml:math>
<label>(3)</label>
</disp-formula>
</p>
<p>E<sub>C</sub> represented carbon conversion efficiency (%), X<sub>biomass</sub> represented the biomass dry weight (g/L), D<sub>C</sub> represented the consumption of NaHCO<sub>3</sub> or KHCO<sub>3</sub> (g/L), and C<sub>algae</sub> represented the carbon content of mutagenic <italic>Spirulina platensis</italic> (%).</p>
<p>The lipid content was determined by Nile red staining. 2.55&#xa0;ml algae solution was added with 450&#xa0;&#x3bc;L dimethyl sulfoxide and 24&#xa0;&#x3bc;L Nile red solution. It was placed in a darkroom at 30&#xb0;C for 10&#xa0;min, and 580&#xa0;nm was selected as the excitation fluorescence detection wavelength (<xref ref-type="bibr" rid="B1">Bertozzini et al., 2011</xref>).</p>
<p>20&#xa0;mg of mutagenic <italic>Spirulina</italic> powder was added to the test tube, and 4&#xa0;ml of deionized water was added to the water bath at 100&#xb0;C for 2&#xa0;h. The supernatant was then filtered through a vacuum pump, 1&#xa0;ml of the filtrate was taken and 4&#xa0;ml of ethanol was added, and it was placed in a refrigerator at 4&#xb0;C for 12&#xa0;h. Finally, the content of polysaccharide was determined by phenol sulfuric acid method (<xref ref-type="bibr" rid="B10">Gasljevic et al., 2008</xref>).</p>
<p>Chlorophyll a and b and carotenoids of mutagenic <italic>Spirulina</italic> were determined by spectrophotometer. The detail determination method is as follows: 5&#xa0;ml uniform algal liquid was centrifuged at 5,000&#xa0;rpm for 10&#xa0;min. Then, the supernatant was removed, 5&#xa0;ml methanol (90%) was added, extracted at 4&#xb0;C for 24&#xa0;h, then centrifuged at 5,000&#xa0;rpm for 10&#xa0;min, the supernatant was taken, and the absorbance of the supernatant was measured at 665, 652&#xa0;nm and 470&#xa0;nm by UV&#x2013;visible spectrophotometer. The contents of chlorophyll a and b and carotenoids in microalgae were calculated by using the Formulas (Eqs. <xref ref-type="disp-formula" rid="e4">4</xref>&#x2013;<xref ref-type="disp-formula" rid="e6">6</xref>).<disp-formula id="e4">
<mml:math id="m4">
<mml:mrow>
<mml:mi mathvariant="normal">C</mml:mi>
<mml:mi mathvariant="normal">h</mml:mi>
<mml:mi mathvariant="normal">l</mml:mi>
<mml:mi mathvariant="normal">o</mml:mi>
<mml:mi mathvariant="normal">r</mml:mi>
<mml:mi mathvariant="normal">o</mml:mi>
<mml:mi mathvariant="normal">p</mml:mi>
<mml:mi mathvariant="normal">h</mml:mi>
<mml:mi mathvariant="normal">y</mml:mi>
<mml:mi mathvariant="normal">l</mml:mi>
<mml:mi mathvariant="normal">l</mml:mi>
<mml:mtext>&#x2009;</mml:mtext>
<mml:mi mathvariant="normal">a</mml:mi>
<mml:mtext>&#x2009;</mml:mtext>
<mml:mrow>
<mml:mfenced open="(" close=")" separators="|">
<mml:mrow>
<mml:mi mathvariant="normal">m</mml:mi>
<mml:mi mathvariant="normal">g</mml:mi>
<mml:mo>/</mml:mo>
<mml:mi mathvariant="normal">L</mml:mi>
</mml:mrow>
</mml:mfenced>
</mml:mrow>
<mml:mo>&#x3d;</mml:mo>
<mml:mn>16.82</mml:mn>
<mml:mtext>&#x2009;</mml:mtext>
<mml:msub>
<mml:mi mathvariant="normal">A</mml:mi>
<mml:mn>665</mml:mn>
</mml:msub>
<mml:mtext>&#x2009;</mml:mtext>
<mml:mo>&#x2013;</mml:mo>
<mml:mtext>&#x2009;</mml:mtext>
<mml:mn>9.28</mml:mn>
<mml:mtext>&#x2009;</mml:mtext>
<mml:msub>
<mml:mi mathvariant="normal">A</mml:mi>
<mml:mn>652</mml:mn>
</mml:msub>
</mml:mrow>
</mml:math>
<label>(4)</label>
</disp-formula>
<disp-formula id="e5">
<mml:math id="m5">
<mml:mrow>
<mml:mi mathvariant="normal">C</mml:mi>
<mml:mi mathvariant="normal">h</mml:mi>
<mml:mi mathvariant="normal">l</mml:mi>
<mml:mi mathvariant="normal">o</mml:mi>
<mml:mi mathvariant="normal">r</mml:mi>
<mml:mi mathvariant="normal">o</mml:mi>
<mml:mi mathvariant="normal">p</mml:mi>
<mml:mi mathvariant="normal">h</mml:mi>
<mml:mi mathvariant="normal">y</mml:mi>
<mml:mi mathvariant="normal">l</mml:mi>
<mml:mi mathvariant="normal">l</mml:mi>
<mml:mtext>&#x2009;</mml:mtext>
<mml:mi mathvariant="normal">b</mml:mi>
<mml:mtext>&#x2009;</mml:mtext>
<mml:mrow>
<mml:mfenced open="(" close=")" separators="|">
<mml:mrow>
<mml:mi mathvariant="normal">m</mml:mi>
<mml:mi mathvariant="normal">g</mml:mi>
<mml:mo>/</mml:mo>
<mml:mi mathvariant="normal">L</mml:mi>
</mml:mrow>
</mml:mfenced>
</mml:mrow>
<mml:mo>&#x3d;</mml:mo>
<mml:mn>36.92</mml:mn>
<mml:mtext>&#x2009;</mml:mtext>
<mml:msub>
<mml:mi mathvariant="normal">A</mml:mi>
<mml:mn>652</mml:mn>
</mml:msub>
<mml:mtext>&#x2009;</mml:mtext>
<mml:mo>&#x2013;</mml:mo>
<mml:mtext>&#x2009;</mml:mtext>
<mml:mn>16.54</mml:mn>
<mml:mtext>&#x2009;</mml:mtext>
<mml:msub>
<mml:mi mathvariant="normal">A</mml:mi>
<mml:mn>665</mml:mn>
</mml:msub>
</mml:mrow>
</mml:math>
<label>(5)</label>
</disp-formula>
<disp-formula id="e6">
<mml:math id="m6">
<mml:mrow>
<mml:msub>
<mml:mi mathvariant="normal">C</mml:mi>
<mml:mrow>
<mml:mi mathvariant="normal">c</mml:mi>
<mml:mi mathvariant="normal">a</mml:mi>
<mml:mi mathvariant="normal">r</mml:mi>
<mml:mi mathvariant="normal">o</mml:mi>
<mml:mi mathvariant="normal">t</mml:mi>
<mml:mi mathvariant="normal">e</mml:mi>
<mml:mi mathvariant="normal">n</mml:mi>
<mml:mi mathvariant="normal">o</mml:mi>
<mml:mi mathvariant="normal">i</mml:mi>
<mml:mi mathvariant="normal">d</mml:mi>
</mml:mrow>
</mml:msub>
<mml:mtext>&#x2009;</mml:mtext>
<mml:mrow>
<mml:mfenced open="(" close=")" separators="|">
<mml:mrow>
<mml:mi mathvariant="normal">m</mml:mi>
<mml:mi mathvariant="normal">g</mml:mi>
<mml:mo>/</mml:mo>
<mml:mi mathvariant="normal">L</mml:mi>
</mml:mrow>
</mml:mfenced>
</mml:mrow>
<mml:mo>&#x3d;</mml:mo>
<mml:mrow>
<mml:mfenced open="(" close=")" separators="|">
<mml:mrow>
<mml:mn>1000</mml:mn>
<mml:mtext>&#x2009;</mml:mtext>
<mml:msub>
<mml:mi mathvariant="normal">A</mml:mi>
<mml:mn>470</mml:mn>
</mml:msub>
<mml:mtext>&#x2009;</mml:mtext>
<mml:mo>&#x2013;</mml:mo>
<mml:mtext>&#x2009;</mml:mtext>
<mml:mn>1.91</mml:mn>
<mml:mtext>&#x2009;</mml:mtext>
<mml:msub>
<mml:mi mathvariant="normal">C</mml:mi>
<mml:mi mathvariant="normal">a</mml:mi>
</mml:msub>
<mml:mtext>&#x2009;</mml:mtext>
<mml:mo>&#x2013;</mml:mo>
<mml:mtext>&#x2009;</mml:mtext>
<mml:mn>95.15</mml:mn>
<mml:mtext>&#x2009;</mml:mtext>
<mml:msub>
<mml:mi mathvariant="normal">C</mml:mi>
<mml:mi mathvariant="normal">b</mml:mi>
</mml:msub>
</mml:mrow>
</mml:mfenced>
</mml:mrow>
<mml:mo>/</mml:mo>
<mml:mn>225</mml:mn>
</mml:mrow>
</mml:math>
<label>(6)</label>
</disp-formula>
</p>
<p>After the cultivation and harvesting, the algae powder was dried, and the algae powder was analyzed and measured. The proportion of N element in biomass N<sub>algae</sub> (%) was obtained. The content of protein X<sub>protein</sub> (mg/L) was calculated according to the relationship between nitrogen content and protein production multiplied by the coefficient 6.25. X<sub>biomass</sub> (g/L) was the dry weight of mutagenic <italic>Spirulina platensis</italic> biomass at the end of the cycle (<xref ref-type="bibr" rid="B15">Li et al., 2020</xref>).<disp-formula id="e7">
<mml:math id="m7">
<mml:mrow>
<mml:msub>
<mml:mi mathvariant="normal">X</mml:mi>
<mml:mrow>
<mml:mi mathvariant="normal">p</mml:mi>
<mml:mi mathvariant="normal">r</mml:mi>
<mml:mi mathvariant="normal">o</mml:mi>
<mml:mi mathvariant="normal">t</mml:mi>
<mml:mi mathvariant="normal">e</mml:mi>
<mml:mi mathvariant="normal">i</mml:mi>
<mml:mi mathvariant="normal">n</mml:mi>
</mml:mrow>
</mml:msub>
<mml:mo>&#x3d;</mml:mo>
<mml:msub>
<mml:mi mathvariant="normal">X</mml:mi>
<mml:mrow>
<mml:mi mathvariant="normal">b</mml:mi>
<mml:mi mathvariant="normal">i</mml:mi>
<mml:mi mathvariant="normal">o</mml:mi>
<mml:mi mathvariant="normal">m</mml:mi>
<mml:mi mathvariant="normal">a</mml:mi>
<mml:mi mathvariant="normal">s</mml:mi>
<mml:mi mathvariant="normal">s</mml:mi>
</mml:mrow>
</mml:msub>
<mml:mo>&#xb7;</mml:mo>
<mml:msub>
<mml:mi mathvariant="normal">N</mml:mi>
<mml:mrow>
<mml:mi mathvariant="normal">a</mml:mi>
<mml:mi mathvariant="normal">l</mml:mi>
<mml:mi mathvariant="normal">g</mml:mi>
<mml:mi mathvariant="normal">a</mml:mi>
<mml:mi mathvariant="normal">e</mml:mi>
</mml:mrow>
</mml:msub>
<mml:mo>&#xb7;</mml:mo>
<mml:mn>6.25</mml:mn>
</mml:mrow>
</mml:math>
<label>(7)</label>
</disp-formula>
</p>
<p>One-way analysis of variance (ANOVA) was used for statistical analysis. Experimental results are expressed as mean &#xb1; standard error. The mean is based on parallel experiments and is within a 95% confidence interval.</p>
</sec>
</sec>
<sec sec-type="results|discussion" id="s3">
<title>3 Results and discussion</title>
<sec id="s3-1">
<title>3.1 Dry weight variation of mutagenic <italic>spirulina</italic> biomass</title>
<p>The biomass dry weight curve was shown in <xref ref-type="fig" rid="F1">Figure 1</xref>. The growth of mutagenic <italic>Spirulina</italic> in the CAMC system with different inorganic carbon concentrations were similar in the first 9&#xa0;days, indicating that the three concentration ranges of NaHCO<sub>3</sub> and KHCO<sub>3</sub> (.1, .2, .3&#xa0;mol/L) could maintain the growth of mutagenic <italic>Spirulina</italic> in the CAMC system. After the 9th&#xa0;day, the growth trend of mutagenic <italic>Spirulina</italic> began to show obvious changes. The biomass of mutagenic <italic>Spirulina</italic> with .1&#xa0;mol/L and .2&#xa0;mol/L NaHCO<sub>3</sub> and KHCO<sub>3</sub> tended to be stable, while the biomass of mutagenic <italic>Spirulina</italic> with .3&#xa0;mol/L NaHCO<sub>3</sub> and KHCO<sub>3</sub> still increased rapidly. After 18&#xa0;days of culture, the biomass dry weight of Na-.3&#xa0;mol/L group was the highest, reaching 2.29&#xa0;g/L, while that of K-.3&#xa0;mol/L group was 2.00&#xa0;g/L. Therefore, compared with K<sub>2</sub>CO<sub>3</sub>, Na<sub>2</sub>CO<sub>3</sub> as a CO<sub>2</sub> chemical absorber was more conducive to the growth of mutagenic <italic>Spirulina</italic> in CAMC system, and the optimal concentration was .3&#xa0;mol/L.</p>
<fig id="F1" position="float">
<label>FIGURE 1</label>
<caption>
<p>Dry weight variation of microalgae biomass under different bicarbonate concentrations.</p>
</caption>
<graphic xlink:href="fbioe-10-1119111-g001.tif"/>
</fig>
</sec>
<sec id="s3-2">
<title>3.2 Change of pH in CO<sub>2</sub> absorption hybrid with microalgae conversion system</title>
<p>The change of pH in the CAMC was shown in <xref ref-type="fig" rid="F2">Figure 2</xref>. HCO<sub>3</sub>
<sup>&#x2212;</sup> will enter cells by active transport under the action of transporters, and the pH of the solution will change with the consumption of HCO<sub>3</sub>
<sup>&#x2212;</sup>. After HCO<sub>3</sub>
<sup>&#x2212;</sup> enters the cell, it will react with intracellular H<sup>&#x2b;</sup>, leading to an increase in the concentration of OH<sup>&#x2212;</sup> in the internal environment of cell. H<sup>&#x2b;</sup> in extracellular solution will transmembrane neutralize OH<sup>&#x2212;</sup> in cells, leading to an increase in pH (<xref ref-type="bibr" rid="B4">Chi et al., 2013</xref>). This process involves one or more CA that facilitate the conversion between HCO<sub>3</sub>
<sup>&#x2212;</sup> and CO<sub>2</sub>. Therefore, the pH of each group showed an upward trend during the first 9&#xa0;days of culture. However, the pH of the CAMC system began to decrease on 9<sup>th</sup>&#xa0;day. This could be caused by more CO<sub>3</sub>
<sup>2-</sup> in the system, which absorbed CO<sub>2</sub> from the air. After 18&#xa0;days of culture, the pH of different groups was stable between 8.5 and 10, but the range of pH change was relatively stable in the CAMC system with .3&#xa0;mol/L HCO<sub>3</sub>
<sup>&#x2212;</sup>.</p>
<fig id="F2" position="float">
<label>FIGURE 2</label>
<caption>
<p>Change of pH under different bicarbonate concentrations.</p>
</caption>
<graphic xlink:href="fbioe-10-1119111-g002.tif"/>
</fig>
</sec>
<sec id="s3-3">
<title>3.3 Changes of chlorophyll a content in mutagenic <italic>spirulina</italic>
</title>
<p>Chlorophyll a can be used as an indicator to evaluate the photosynthetic capacity of microalgae. The change of chlorophyll a content of mutagenic <italic>Spirulina</italic> was shown in <xref ref-type="fig" rid="F3">Figure 3</xref>. At the first 9&#xa0;days of culture, the chlorophyll a content of mutagenic <italic>Spirulina</italic> increased with the growth of biomass. In the Na-.2&#xa0;mol/L group, the chlorophyll a content of mutagenic <italic>Spirulina</italic> reached the maximum on the 9<sup>th</sup>&#xa0;day, reaching 11.05&#xa0;mg/L. After 9&#xa0;days of culture, the content of chlorophyll a of mutagenic <italic>Spirulina</italic> showed a downward trend. This may be related to the change of solution pH, which affects the activity of pigment synthetase and the synthesis of chlorophyll a. After 15&#xa0;days of culture, the chlorophyll-a content of mutagenic <italic>Spirulina</italic> decreased obviously, which may be caused by the insufficient nitrogen source in the medium. Under the condition of nitrogen limitation, the activities of enzymes involved in the degradation of organic nitrogen sources in mutagenic <italic>Spirulina</italic> were enhanced, which could degrade the nitrogen pigments in the cells to maintain their normal metabolism (<xref ref-type="bibr" rid="B17">Pancha et al., 2014</xref>; <xref ref-type="bibr" rid="B7">Depraetere et al., 2015</xref>).</p>
<fig id="F3" position="float">
<label>FIGURE 3</label>
<caption>
<p>Changes of chlorophyll a under different bicarbonate concentrations.</p>
</caption>
<graphic xlink:href="fbioe-10-1119111-g003.tif"/>
</fig>
</sec>
<sec id="s3-4">
<title>3.4 Changes of inorganic carbon content, utilization efficiency and fixation rate</title>
<p>The concentration of inorganic carbon in the solution will change with the growth of mutagenic <italic>Spirulina</italic>, and the content of inorganic carbon and carbon sequestration rate in the solution of each group was shown in <xref ref-type="fig" rid="F4">Figure 4A</xref>. After 18&#xa0;days of culture, the inorganic carbon content of Na-.1&#xa0;mol/L group decreased from 1,200&#xa0;mg/L to 970&#xa0;mg/L, and the carbon utilization efficiency was 15.79%. The concentration of inorganic carbon in Na-.2&#xa0;mol/L group decreased from 2,400&#xa0;mg/L to 1998&#xa0;mg/L, and the carbon utilization efficiency was 26.45%. The highest carbon utilization efficiency (26.71%) was obtained in Na-.3&#xa0;mol/L group, and the inorganic carbon concentration decreased from 3,600&#xa0;mg/L to 2,531&#xa0;mg/L. The carbon utilization efficiency of K-.1&#xa0;mol/L, K-.2&#xa0;mol/L and K-.3&#xa0;mol/L groups were 17.25%, 20.38% and 25.49%, respectively. This indicated that NaHCO<sub>3</sub> was more conducive to carbon utilization by mutagenic <italic>Spirulina</italic> in CAMC system.</p>
<fig id="F4" position="float">
<label>FIGURE 4</label>
<caption>
<p>Chane of inorganic carbon content and utilization efficiency <bold>(A)</bold>, carbon fixation rate <bold>(B)</bold> under different bicarbonate concentration.</p>
</caption>
<graphic xlink:href="fbioe-10-1119111-g004.tif"/>
</fig>
<p>The carbon fixation rate of mutagenic <italic>Spirulina</italic> in CAMC system was shown in <xref ref-type="fig" rid="F4">Figure 4B</xref>. The carbon fixation rate of mutagenic <italic>Spirulina</italic> in Na-.1&#xa0;mol/L, Na-.2&#xa0;mol/L and Na-.3&#xa0;mol/L groups were 87.83&#xa0;mg/L/d, 128.55&#xa0;mg/L/d and 230.36&#xa0;mg/L/d, respectively. It was much higher than the 15&#xa0;mg/L/d and 17&#xa0;mg/L/d obtained by Song et al. who using NH<sub>4</sub>HCO<sub>3</sub> as carbon source (<xref ref-type="bibr" rid="B24">Song C. et al., 2019</xref>). (<xref ref-type="bibr" rid="B14">Khoobkar et al., 2022</xref>) reported similar carbon fixation rate when cultivating <italic>Chlorella</italic> sp. in a photobioreactor. While the carbon fixation rate of mutagenic <italic>Spirulina</italic> in K-.1&#xa0;mol/L, K-.2&#xa0;mol/L and K-.3&#xa0;mol/L groups were 86.58&#xa0;mg/L/d, 113.74&#xa0;mg/L/d and 153.41&#xa0;mg/L. This indicated that the carbon fixation rate in NaHCO<sub>3</sub> system was higher than that in KHCO<sub>3</sub> system, which was also consistent with the dry weight of biomass.</p>
</sec>
<sec id="s3-5">
<title>3.5 Value-added components yield of CO<sub>2</sub> absorption hybrid with microalgae conversion system</title>
<sec id="s3-5-1">
<title>3.5.1 Change of lipid content and yield</title>
<p>The lipid content and lipid production yield of mutagenic <italic>Spirulina</italic> in the CAMC system with different inorganic carbon concentrations was shown in <xref ref-type="fig" rid="F5">Figure 5</xref>. After 18&#xa0;days of culture, the contents of lipid in Na-.1&#xa0;mol/L, Na-.2&#xa0;mol/L and Na-.3&#xa0;mol/L groups were 10.95&#xa0;mg/L, 16.62&#xa0;mg/L and 17.62&#xa0;mg/L, respectively. While that of K-.1&#xa0;mol/L, K-.2&#xa0;mol/L and K-.3&#xa0;mol/L groups were 13.20&#xa0;mg/L, 21.04&#xa0;mg/L and 22.60&#xa0;mg/L. In the NaHCO<sub>3</sub> system, the mutated <italic>Spirulina</italic> obtained the highest lipid production rate (.98&#xa0;mg/L/d) at .3 Na-mol/L group. In K-.1&#xa0;mol/L, K-.2&#xa0;mol/L and K-.3&#xa0;mol/L groups, the lipid production rate of mutated <italic>Spirulina</italic> was .73, 1.17 and 1.26&#xa0;mg/L/d, respectively. High concentrations of Na<sup>&#x2b;</sup> and K<sup>&#x2b;</sup> contribute to lipid accumulation, which may be related to the stress effect. Previous study showed that salinity stress has positive impact on lipid synthesis (<xref ref-type="bibr" rid="B16">Mohan &#x26; Devi, 2014</xref>). The results showed that KHCO<sub>3</sub> was beneficial for lipid synthesis in CAMC system, compared with NaHCO<sub>3</sub>.</p>
<fig id="F5" position="float">
<label>FIGURE 5</label>
<caption>
<p>Lipid content and yield under different bicarbonate concentrations.</p>
</caption>
<graphic xlink:href="fbioe-10-1119111-g005.tif"/>
</fig>
</sec>
<sec id="s3-5-2">
<title>3.5.2 Change of polysaccharide content and yield</title>
<p>Polysaccharide is a functional macromolecule with antioxidant, antiviral, immunomodulatory and anti-inflammatory activities (<xref ref-type="bibr" rid="B20">Sathasivam et al., 2019</xref>). The polysaccharide content of mutagenic <italic>Spirulina</italic> in CAMC system was shown in <xref ref-type="fig" rid="F6">Figure 6</xref>. The polysaccharide content in the Na-.1&#xa0;mol/L and Na-.2&#xa0;mol/L group were 17.01&#xa0;mg/L and 12.78&#xa0;mg/L, respectively, and the highest polysaccharide content was obtained in the Na-.3&#xa0;mol/L group (62.97&#xa0;mg/L). The polysaccharide content of mutagenic <italic>Spirulina</italic> in K-.1&#xa0;mol/L, K-.2&#xa0;mol/L and K-.3&#xa0;mol/L groups were 87.80&#xa0;mg/L, 347.70&#xa0;mg/L and 461.28&#xa0;mg/L. Among all groups, the polysaccharide productivity of mutagenic <italic>Spirulina</italic> in K-.3&#xa0;mol/L group was the highest, which was 25.63&#xa0;mg/L/d. The results showed that compared with NaHCO<sub>3</sub>, KHCO<sub>3</sub> was more conducive to polysaccharide synthesis, and .3&#xa0;mol/L promoted the most.</p>
<fig id="F6" position="float">
<label>FIGURE 6</label>
<caption>
<p>Polysaccharide content and yield under different bicarbonate concentrations.</p>
</caption>
<graphic xlink:href="fbioe-10-1119111-g006.tif"/>
</fig>
</sec>
<sec id="s3-5-3">
<title>3.5.3 Change of protein content</title>
<p>
<xref ref-type="fig" rid="F7">Figure 7</xref>. Showed the protein content of mutagenic <italic>Spirulina</italic> in CAMC system. Under the same HCO<sub>3</sub>
<sup>&#x2212;</sup> concentration, the protein content in Na<sup>&#x2b;</sup> system was higher than that in K<sup>&#x2b;</sup> system, which may be because Na<sup>&#x2b;</sup> can transmembrane into cells under the action of transporters (<xref ref-type="bibr" rid="B19">Reinfelder, 2011</xref>). The protein content of mutagenic <italic>Spirulina</italic> in Na-.3&#xa0;mol/L group was the highest (1,625.68&#xa0;mg/L). This maybe more transporters were needed to complete the transport of Na<sup>&#x2b;</sup> in a high concentration Na<sup>&#x2b;</sup> system, and microalgae will preferentially use more energy to synthesize this transporter, leading to an increase in protein content (<xref ref-type="bibr" rid="B25">Tsuji et al., 2021</xref>). This also further revealed the reason why the content of polysaccharide in NaHCO<sub>3</sub> system was not as high as that in KHCO<sub>3</sub> system (<xref ref-type="fig" rid="F6">Figure 6</xref>). More energy was used for protein synthesis, resulting in less energy for polysaccharide synthesis (<xref ref-type="bibr" rid="B18">Pereira et al., 2019</xref>).</p>
<fig id="F7" position="float">
<label>FIGURE 7</label>
<caption>
<p>Protein content and yield under different bicarbonate concentrations.</p>
</caption>
<graphic xlink:href="fbioe-10-1119111-g007.tif"/>
</fig>
</sec>
</sec>
</sec>
<sec sec-type="conclusion" id="s4">
<title>4 Conclusion</title>
<p>In this study, the chemical absorbent NaHCO<sub>3</sub> and KHCO<sub>3</sub> (represent products after Na<sub>2</sub>CO<sub>3</sub> and K<sub>2</sub>CO<sub>3</sub> fully absorb CO<sub>2</sub>) was selected as the research object, and the corresponding bicarbonate was used for the cultivation of mutagenic <italic>Spirulina</italic> to achieve carbon capture and resource utilization. Compared with KHCO<sub>3</sub>, NaHCO<sub>3</sub> was conductive to the growth of mutagenic <italic>Spirulina</italic>, and .3&#xa0;mol/L NaHCO<sub>3</sub> promoted the biomass accumulation and carbon sequestration efficiency of CAMC system (reaching 2.24&#xa0;g/L and 26.71%). KHCO<sub>3</sub> promoted the production of lipid and polysaccharide, and NaHCO<sub>3</sub> was conducive to the accumulation of protein (reaching 1,625.68&#xa0;mg/L). In the subsequent application process, Na<sub>2</sub>CO<sub>3</sub> or K<sub>2</sub>CO<sub>3</sub> can be selected as the absorbent of CAMC system to cultivate mutagenic <italic>Spirulina</italic> according to the requirements of the target products. It is worth noting that a variety of new CO<sub>2</sub> absorbents have been developed in recent years, and their feasibility and operating effects in coupled systems need to be continuously paid attention to.</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/Supplementary Material, further inquiries can be directed to the corresponding author.</p>
</sec>
<sec id="s6">
<title>Author contributions</title>
<p>PZ: Data curation, Software. QS: Software. YD: Data curation. SL: Conceptualization, Methodology, Writing - review and editing.</p>
</sec>
<sec id="s7">
<title>Funding</title>
<p>This research was financially supported by the National Key Research and Development Program-China (No. 2017YFE0127200), National Natural Science Foundation of China (No. 21878228), International Cooperation Research center of Carbon Capture in Ultra-low Energy-consumption (Tianjin).</p>
</sec>
<sec sec-type="COI-statement" id="s8">
<title>Conflict of interest</title>
<p>Authors PZ, QS, and YD are employed by Tianjin Building Materials Science Research Academy Co., Ltd.</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>
</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>
<ref-list>
<title>References</title>
<ref id="B1">
<citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname>Bertozzini</surname>
<given-names>E.</given-names>
</name>
<name>
<surname>Galluzzi</surname>
<given-names>L.</given-names>
</name>
<name>
<surname>Penna</surname>
<given-names>A.</given-names>
</name>
<name>
<surname>Magnani</surname>
<given-names>M.</given-names>
</name>
</person-group> (<year>2011</year>). <article-title>Application of the standard addition method for the absolute quantification of neutral lipids in microalgae using Nile red</article-title>. <source>J. Microbiol. Methods</source> <volume>87</volume> (<issue>1</issue>), <fpage>17</fpage>&#x2013;<lpage>23</lpage>. <pub-id pub-id-type="doi">10.1016/j.mimet.2011.06.018</pub-id>
</citation>
</ref>
<ref id="B2">
<citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname>Chang</surname>
<given-names>Y.</given-names>
</name>
<name>
<surname>Wu</surname>
<given-names>Z.</given-names>
</name>
<name>
<surname>Bian</surname>
<given-names>L.</given-names>
</name>
<name>
<surname>Feng</surname>
<given-names>D.</given-names>
</name>
<name>
<surname>Leung</surname>
<given-names>D. Y. C.</given-names>
</name>
</person-group> (<year>2013</year>). <article-title>Cultivation of <italic>Spirulina platensis</italic> for biomass production and nutrient removal from synthetic human urine</article-title>. <source>Appl. Energy</source> <volume>102</volume>, <fpage>427</fpage>&#x2013;<lpage>431</lpage>. <pub-id pub-id-type="doi">10.1016/j.apenergy.2012.07.024</pub-id>
</citation>
</ref>
<ref id="B3">
<citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname>Cheng</surname>
<given-names>J.</given-names>
</name>
<name>
<surname>Lu</surname>
<given-names>H.</given-names>
</name>
<name>
<surname>He</surname>
<given-names>X.</given-names>
</name>
<name>
<surname>Yang</surname>
<given-names>W.</given-names>
</name>
<name>
<surname>Zhou</surname>
<given-names>J.</given-names>
</name>
<name>
<surname>Cen</surname>
<given-names>K.</given-names>
</name>
</person-group> (<year>2017</year>). <article-title>Mutation of <italic>Spirulina</italic> sp. by nuclear irradiation to improve growth rate under 15% carbon dioxide in flue gas</article-title>. <source>Bioresour. Technol.</source> <volume>238</volume>, <fpage>650</fpage>&#x2013;<lpage>656</lpage>. <pub-id pub-id-type="doi">10.1016/j.biortech.2017.04.107</pub-id>
</citation>
</ref>
<ref id="B4">
<citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname>Chi</surname>
<given-names>Z. Y.</given-names>
</name>
<name>
<surname>Xie</surname>
<given-names>Y. X.</given-names>
</name>
<name>
<surname>Elloy</surname>
<given-names>F.</given-names>
</name>
<name>
<surname>Zheng</surname>
<given-names>Y. B.</given-names>
</name>
<name>
<surname>Hu</surname>
<given-names>Y. C.</given-names>
</name>
<name>
<surname>Chen</surname>
<given-names>S. L.</given-names>
</name>
</person-group> (<year>2013</year>). <article-title>Bicarbonate-based integrated carbon capture and algae production system with alkalihalophilic cyanobacterium</article-title>. <source>Bioresour. Technol.</source> <volume>133</volume>, <fpage>513</fpage>&#x2013;<lpage>521</lpage>. <pub-id pub-id-type="doi">10.1016/j.biortech.2013.01.150</pub-id>
</citation>
</ref>
<ref id="B5">
<citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname>da Rosa</surname>
<given-names>G. M.</given-names>
</name>
<name>
<surname>Moraes</surname>
<given-names>L.</given-names>
</name>
<name>
<surname>de Souza</surname>
<given-names>M. D. A. Z.</given-names>
</name>
<name>
<surname>Costa</surname>
<given-names>J. A. V.</given-names>
</name>
</person-group> (<year>2016</year>). <article-title>
<italic>Spirulina</italic> cultivation with a CO<sub>2</sub> absorbent: Influence on growth parameters and macromolecule production</article-title>. <source>Bioresour. Technol.</source> <volume>200</volume>, <fpage>528</fpage>&#x2013;<lpage>534</lpage>. <pub-id pub-id-type="doi">10.1016/j.biortech.2015.10.025</pub-id>
</citation>
</ref>
<ref id="B6">
<citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname>de Jesus</surname>
<given-names>C. S.</given-names>
</name>
<name>
<surname>da Silva Uebel</surname>
<given-names>L.</given-names>
</name>
<name>
<surname>Costa</surname>
<given-names>S. S.</given-names>
</name>
<name>
<surname>Miranda</surname>
<given-names>A. L.</given-names>
</name>
<name>
<surname>de Morais</surname>
<given-names>E. G.</given-names>
</name>
<name>
<surname>de Morais</surname>
<given-names>M. G.</given-names>
</name>
<etal/>
</person-group> (<year>2018</year>). <article-title>Outdoor pilot-scale cultivation of <italic>Spirulina</italic> sp. LEB-18 in different geographic locations for evaluating its growth and chemical composition</article-title>. <source>Bioresour. Technol.</source> <volume>256</volume>, <fpage>86</fpage>&#x2013;<lpage>94</lpage>. <pub-id pub-id-type="doi">10.1016/j.biortech.2018.01.149</pub-id>
</citation>
</ref>
<ref id="B7">
<citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname>Depraetere</surname>
<given-names>O.</given-names>
</name>
<name>
<surname>Deschoenmaeker</surname>
<given-names>F.</given-names>
</name>
<name>
<surname>Badri</surname>
<given-names>H.</given-names>
</name>
<name>
<surname>Monsieurs</surname>
<given-names>P.</given-names>
</name>
<name>
<surname>Foubert</surname>
<given-names>I.</given-names>
</name>
<name>
<surname>Leys</surname>
<given-names>N.</given-names>
</name>
<etal/>
</person-group> (<year>2015</year>). <article-title>Trade-off between growth and carbohydrate accumulation in nutrient-limited Arthrospira sp PCC 8005 studied by integrating transcriptomic and proteomic approaches</article-title>. <source>Plos One</source> <volume>10</volume> (<issue>7</issue>), <fpage>e0132461</fpage>. <pub-id pub-id-type="doi">10.1371/journal.pone.0132461</pub-id>
</citation>
</ref>
<ref id="B8">
<citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname>Ding</surname>
<given-names>Y.</given-names>
</name>
<name>
<surname>Li</surname>
<given-names>X. L.</given-names>
</name>
<name>
<surname>Wang</surname>
<given-names>Z. J.</given-names>
</name>
<name>
<surname>Li</surname>
<given-names>Z. K.</given-names>
</name>
<name>
<surname>Yin</surname>
<given-names>D. C.</given-names>
</name>
<name>
<surname>Geng</surname>
<given-names>Y. H.</given-names>
</name>
<etal/>
</person-group> (<year>2017</year>). <article-title>Ammonium bicarbonate supplementation as carbon source in alkaliphilic <italic>Spirulina</italic> mass culture</article-title>. <source>Aquac. Res.</source> <volume>48</volume> (<issue>9</issue>), <fpage>4886</fpage>&#x2013;<lpage>4896</lpage>. <pub-id pub-id-type="doi">10.1111/are.13308</pub-id>
</citation>
</ref>
<ref id="B9">
<citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname>Fang</surname>
<given-names>M. X.</given-names>
</name>
<name>
<surname>Yi</surname>
<given-names>N. T.</given-names>
</name>
<name>
<surname>Di</surname>
<given-names>W. T.</given-names>
</name>
<name>
<surname>Wang</surname>
<given-names>T.</given-names>
</name>
<name>
<surname>Wang</surname>
<given-names>Q. H.</given-names>
</name>
</person-group> (<year>2020</year>). <article-title>Emission and control of flue gas pollutants in CO<sub>2</sub> chemical absorption system - a review</article-title>. <source>Int. J. Greenh. Gas Control</source> <volume>93</volume>, <fpage>102904</fpage>. <pub-id pub-id-type="doi">10.1016/j.ijggc.2019.102904</pub-id>
</citation>
</ref>
<ref id="B10">
<citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname>Gasljevic</surname>
<given-names>K.</given-names>
</name>
<name>
<surname>Hall</surname>
<given-names>K.</given-names>
</name>
<name>
<surname>Chapman</surname>
<given-names>D.</given-names>
</name>
<name>
<surname>Matthys</surname>
<given-names>E. F.</given-names>
</name>
</person-group> (<year>2008</year>). <article-title>Drag-reducing polysaccharides from marine microalgae: Species productivity and drag reduction effectiveness</article-title>. <source>J. Appl. Phycol.</source> <volume>20</volume> (<issue>3</issue>), <fpage>299</fpage>&#x2013;<lpage>310</lpage>. <pub-id pub-id-type="doi">10.1007/s10811-007-9250-z</pub-id>
</citation>
</ref>
<ref id="B11">
<citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname>Ju</surname>
<given-names>Z. Y.</given-names>
</name>
<name>
<surname>Deng</surname>
<given-names>D.-F.</given-names>
</name>
<name>
<surname>Dominy</surname>
<given-names>W.</given-names>
</name>
</person-group> (<year>2012</year>). <article-title>A defatted microalgae (Haematococcus pluvialis) meal as a protein ingredient to partially replace fishmeal in diets of Pacific white shrimp (Litopenaeus vannamei, Boone, 1931)</article-title>. <source>Aquaculture</source> <volume>354</volume>, <fpage>50</fpage>&#x2013;<lpage>55</lpage>. <pub-id pub-id-type="doi">10.1016/j.aquaculture.2012.04.028</pub-id>
</citation>
</ref>
<ref id="B12">
<citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname>Kanno</surname>
<given-names>M.</given-names>
</name>
<name>
<surname>Carroll</surname>
<given-names>A. L.</given-names>
</name>
<name>
<surname>Atsumi</surname>
<given-names>S.</given-names>
</name>
</person-group> (<year>2017</year>). <article-title>Global metabolic rewiring for improved CO<sub>2</sub> fixation and chemical production in cyanobacteria</article-title>. <source>Nat. Commun.</source> <volume>8</volume>, <fpage>14724</fpage>. <pub-id pub-id-type="doi">10.1038/ncomms14724</pub-id>
</citation>
</ref>
<ref id="B13">
<citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname>Khoo</surname>
<given-names>K. S.</given-names>
</name>
<name>
<surname>Lee</surname>
<given-names>S. Y.</given-names>
</name>
<name>
<surname>Ooi</surname>
<given-names>C. W.</given-names>
</name>
<name>
<surname>Fu</surname>
<given-names>X. T.</given-names>
</name>
<name>
<surname>Miao</surname>
<given-names>X. L.</given-names>
</name>
<name>
<surname>Ling</surname>
<given-names>T. C.</given-names>
</name>
<etal/>
</person-group> (<year>2019</year>). <article-title>Recent advances in biorefinery of astaxanthin from Haematococcus pluvialis</article-title>. <source>Bioresour. Technol.</source> <volume>288</volume>, <fpage>121606</fpage>. <pub-id pub-id-type="doi">10.1016/j.biortech.2019.121606</pub-id>
</citation>
</ref>
<ref id="B14">
<citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname>Khoobkar</surname>
<given-names>Z.</given-names>
</name>
<name>
<surname>Amrei</surname>
<given-names>H. D.</given-names>
</name>
<name>
<surname>Heydarinasab</surname>
<given-names>A.</given-names>
</name>
<name>
<surname>Mirzaie</surname>
<given-names>M. A. M.</given-names>
</name>
</person-group> (<year>2022</year>). <article-title>Biofixation of CO<sub>2</sub> and biomass production from model natural gas using microalgae: An attractive concept for natural gas sweetening</article-title>. <source>J. CO<sub>2</sub> Util.</source> <volume>64</volume>, <fpage>102153</fpage>. <pub-id pub-id-type="doi">10.1016/j.jcou.2022.102153</pub-id>
</citation>
</ref>
<ref id="B15">
<citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname>Li</surname>
<given-names>S. H.</given-names>
</name>
<name>
<surname>Song</surname>
<given-names>C. F.</given-names>
</name>
<name>
<surname>Li</surname>
<given-names>M. D.</given-names>
</name>
<name>
<surname>Chen</surname>
<given-names>Y.</given-names>
</name>
<name>
<surname>Lei</surname>
<given-names>Z. F.</given-names>
</name>
<name>
<surname>Zhang</surname>
<given-names>Z. Y.</given-names>
</name>
</person-group> (<year>2020</year>). <article-title>Effect of different nitrogen ratio on the performance of CO<sub>2</sub> absorption and microalgae conversion (CAMC) hybrid system</article-title>. <source>Bioresour. Technol.</source> <volume>306</volume>, <fpage>123126</fpage>. <pub-id pub-id-type="doi">10.1016/j.biortech.2020.123126</pub-id>
</citation>
</ref>
<ref id="B16">
<citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname>Mohan</surname>
<given-names>S. V.</given-names>
</name>
<name>
<surname>Devi</surname>
<given-names>M. P.</given-names>
</name>
</person-group> (<year>2014</year>). <article-title>Salinity stress induced lipid synthesis to harness biodiesel during dual mode cultivation of mixotrophic microalgae</article-title>. <source>Bioresour. Technol.</source> <volume>165</volume>, <fpage>288</fpage>&#x2013;<lpage>294</lpage>. <pub-id pub-id-type="doi">10.1016/j.biortech.2014.02.103</pub-id>
</citation>
</ref>
<ref id="B17">
<citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname>Pancha</surname>
<given-names>I.</given-names>
</name>
<name>
<surname>Chokshi</surname>
<given-names>K.</given-names>
</name>
<name>
<surname>George</surname>
<given-names>B.</given-names>
</name>
<name>
<surname>Ghosh</surname>
<given-names>T.</given-names>
</name>
<name>
<surname>Paliwal</surname>
<given-names>C.</given-names>
</name>
<name>
<surname>Maurya</surname>
<given-names>R.</given-names>
</name>
<etal/>
</person-group> (<year>2014</year>). <article-title>Nitrogen stress triggered biochemical and morphological changes in the microalgae Scenedesmus sp CCNM 1077</article-title>. <source>Bioresour. Technol.</source> <volume>156</volume>, <fpage>146</fpage>&#x2013;<lpage>154</lpage>. <pub-id pub-id-type="doi">10.1016/j.biortech.2014.01.025</pub-id>
</citation>
</ref>
<ref id="B18">
<citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname>Pereira</surname>
<given-names>M. I. B.</given-names>
</name>
<name>
<surname>Chagas</surname>
<given-names>B. M. E.</given-names>
</name>
<name>
<surname>Sassi</surname>
<given-names>R.</given-names>
</name>
<name>
<surname>Medeiros</surname>
<given-names>G. F.</given-names>
</name>
<name>
<surname>Aguiar</surname>
<given-names>E. M.</given-names>
</name>
<name>
<surname>Borba</surname>
<given-names>L. H. F.</given-names>
</name>
<etal/>
</person-group> (<year>2019</year>). <article-title>Mixotrophic cultivation of <italic>Spirulina platensis</italic> in dairy wastewater: Effects on the production of biomass, biochemical composition and antioxidant capacity</article-title>. <source>Plos One</source> <volume>14</volume> (<issue>10</issue>), <fpage>e0224294</fpage>. <pub-id pub-id-type="doi">10.1371/journal.pone.0224294</pub-id>
</citation>
</ref>
<ref id="B19">
<citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname>Reinfelder</surname>
<given-names>J. R.</given-names>
</name>
</person-group> (<year>2011</year>). <article-title>Carbon concentrating mechanisms in eukaryotic marine phytoplankton</article-title>. <source>Annu. Rev. Mar. Sci.</source> <volume>3</volume> (<issue>3</issue>), <fpage>291</fpage>&#x2013;<lpage>315</lpage>. <pub-id pub-id-type="doi">10.1146/annurev-marine-120709-142720</pub-id>
</citation>
</ref>
<ref id="B20">
<citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname>Sathasivam</surname>
<given-names>R.</given-names>
</name>
<name>
<surname>Radhakrishnan</surname>
<given-names>R.</given-names>
</name>
<name>
<surname>Hashem</surname>
<given-names>A.</given-names>
</name>
<name>
<surname>Abd Allah</surname>
<given-names>E. F.</given-names>
</name>
</person-group> (<year>2019</year>). <article-title>Microalgae metabolites: A rich source for food and medicine</article-title>. <source>Saudi J. Biol. Sci.</source> <volume>26</volume> (<issue>4</issue>), <fpage>709</fpage>&#x2013;<lpage>722</lpage>. <pub-id pub-id-type="doi">10.1016/j.sjbs.2017.11.003</pub-id>
</citation>
</ref>
<ref id="B21">
<citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname>Song</surname>
<given-names>C. F.</given-names>
</name>
<name>
<surname>Liu</surname>
<given-names>Q. L.</given-names>
</name>
<name>
<surname>Qi</surname>
<given-names>Y.</given-names>
</name>
<name>
<surname>Chen</surname>
<given-names>G. Y.</given-names>
</name>
<name>
<surname>Song</surname>
<given-names>Y. J.</given-names>
</name>
<name>
<surname>Kansha</surname>
<given-names>Y.</given-names>
</name>
<etal/>
</person-group> (<year>2019b</year>). <article-title>Absorption-microalgae hybrid CO<sub>2</sub> capture and biotransformation strategy-A review</article-title>. <source>Int. J. Greenh. Gas Control</source> <volume>88</volume>, <fpage>109</fpage>&#x2013;<lpage>117</lpage>. <pub-id pub-id-type="doi">10.1016/j.ijggc.2019.06.002</pub-id>
</citation>
</ref>
<ref id="B22">
<citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname>Song</surname>
<given-names>C. F.</given-names>
</name>
<name>
<surname>Qiu</surname>
<given-names>Y. T.</given-names>
</name>
<name>
<surname>Xie</surname>
<given-names>M. L.</given-names>
</name>
<name>
<surname>Qi</surname>
<given-names>Y.</given-names>
</name>
<name>
<surname>Li</surname>
<given-names>S. H.</given-names>
</name>
<name>
<surname>Kitamura</surname>
<given-names>Y.</given-names>
</name>
</person-group> (<year>2019c</year>). <article-title>Novel bio-regeneration concept via using rich solution as nutrition resource for microalgae cultivation: Effect of ph and feeding modes</article-title>. <source>Acs Sustain. Chem. Eng.</source> <volume>7</volume> (<issue>17</issue>), <fpage>14471</fpage>&#x2013;<lpage>14478</lpage>. <pub-id pub-id-type="doi">10.1021/acssuschemeng.9b01839</pub-id>
</citation>
</ref>
<ref id="B23">
<citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname>Song</surname>
<given-names>C.</given-names>
</name>
<name>
<surname>Liu</surname>
<given-names>Q.</given-names>
</name>
<name>
<surname>Ji</surname>
<given-names>N.</given-names>
</name>
<name>
<surname>Deng</surname>
<given-names>S.</given-names>
</name>
<name>
<surname>Zhao</surname>
<given-names>J.</given-names>
</name>
<name>
<surname>Li</surname>
<given-names>Y.</given-names>
</name>
<etal/>
</person-group> (<year>2018</year>). <article-title>Alternative pathways for efficient CO<sub>2</sub> capture by hybrid processes&#x2014;a review</article-title>. <source>Renew. Sustain. Energy Rev.</source> <volume>82</volume>, <fpage>215</fpage>&#x2013;<lpage>231</lpage>. <pub-id pub-id-type="doi">10.1016/j.rser.2017.09.040</pub-id>
</citation>
</ref>
<ref id="B24">
<citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname>Song</surname>
<given-names>C.</given-names>
</name>
<name>
<surname>Xie</surname>
<given-names>M.</given-names>
</name>
<name>
<surname>Qiu</surname>
<given-names>Y.</given-names>
</name>
<name>
<surname>Liu</surname>
<given-names>Q.</given-names>
</name>
<name>
<surname>Sun</surname>
<given-names>L.</given-names>
</name>
<name>
<surname>Wang</surname>
<given-names>K.</given-names>
</name>
<etal/>
</person-group> (<year>2019a</year>). <article-title>Integration of CO<sub>2</sub> absorption with biological transformation via using rich ammonia solution as a nutrient source for microalgae cultivation</article-title>. <source>Energy</source> <volume>179</volume>, <fpage>618</fpage>&#x2013;<lpage>627</lpage>. <pub-id pub-id-type="doi">10.1016/j.energy.2019.05.039</pub-id>
</citation>
</ref>
<ref id="B25">
<citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname>Tsuji</surname>
<given-names>Y.</given-names>
</name>
<name>
<surname>Kusi-Appiah</surname>
<given-names>G.</given-names>
</name>
<name>
<surname>Kozai</surname>
<given-names>N.</given-names>
</name>
<name>
<surname>Fukuda</surname>
<given-names>Y.</given-names>
</name>
<name>
<surname>Yamano</surname>
<given-names>T.</given-names>
</name>
<name>
<surname>Fukuzawa</surname>
<given-names>H.</given-names>
</name>
</person-group> (<year>2021</year>). <article-title>Characterization of a CO<sub>2</sub>-concentrating mechanism with low sodium dependency in the centric diatom chaetoceros gracilis</article-title>. <source>Mar. Biotechnol.</source> <volume>23</volume> (<issue>3</issue>), <fpage>456</fpage>&#x2013;<lpage>462</lpage>. <pub-id pub-id-type="doi">10.1007/s10126-021-10037-4</pub-id>
</citation>
</ref>
</ref-list>
</back>
</article>