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<front>
<journal-meta>
<journal-id journal-id-type="publisher-id">Front. Sustain. Food Syst.</journal-id>
<journal-title>Frontiers in Sustainable Food Systems</journal-title>
<abbrev-journal-title abbrev-type="pubmed">Front. Sustain. Food Syst.</abbrev-journal-title>
<issn pub-type="epub">2571-581X</issn>
<publisher>
<publisher-name>Frontiers Media S.A.</publisher-name>
</publisher>
</journal-meta>
<article-meta>
<article-id pub-id-type="doi">10.3389/fsufs.2022.883069</article-id>
<article-categories>
<subj-group subj-group-type="heading">
<subject>Sustainable Food Systems</subject>
<subj-group>
<subject>Original Research</subject>
</subj-group>
</subj-group>
</article-categories>
<title-group>
<article-title>Influence of Process Operation on the Production of Exopolysaccharides in <italic>Arthrospira platensis</italic> and <italic>Chlamydomonas asymmetrica</italic></article-title>
</title-group>
<contrib-group>
<contrib contrib-type="author" corresp="yes">
<name><surname>Jung</surname> <given-names>Sun-Hwa</given-names></name>
<xref ref-type="aff" rid="aff1"><sup>1</sup></xref>
<xref ref-type="corresp" rid="c001"><sup>&#x0002A;</sup></xref>
<uri xlink:href="http://loop.frontiersin.org/people/1769582/overview"/>
</contrib>
<contrib contrib-type="author">
<name><surname>Zell</surname> <given-names>Niklas</given-names></name>
<xref ref-type="aff" rid="aff1"><sup>1</sup></xref>
</contrib>
<contrib contrib-type="author">
<name><surname>Bo&#x000DF;le</surname> <given-names>Fabian</given-names></name>
<xref ref-type="aff" rid="aff1"><sup>1</sup></xref>
<uri xlink:href="http://loop.frontiersin.org/people/1735083/overview"/>
</contrib>
<contrib contrib-type="author">
<name><surname>Teipel</surname> <given-names>Ulrich</given-names></name>
<xref ref-type="aff" rid="aff2"><sup>2</sup></xref>
</contrib>
<contrib contrib-type="author">
<name><surname>Rauh</surname> <given-names>Cornelia</given-names></name>
<xref ref-type="aff" rid="aff3"><sup>3</sup></xref>
<uri xlink:href="http://loop.frontiersin.org/people/173526/overview"/>
</contrib>
<contrib contrib-type="author">
<name><surname>McHardy</surname> <given-names>Christopher</given-names></name>
<xref ref-type="aff" rid="aff3"><sup>3</sup></xref>
<uri xlink:href="http://loop.frontiersin.org/people/864457/overview"/>
</contrib>
<contrib contrib-type="author">
<name><surname>Lindenberger</surname> <given-names>Christoph</given-names></name>
<xref ref-type="aff" rid="aff1"><sup>1</sup></xref>
<uri xlink:href="http://loop.frontiersin.org/people/1535313/overview"/>
</contrib>
</contrib-group>
<aff id="aff1"><sup>1</sup><institution>Department of Mechanical Engineering/Environmental Technology, OTH Amberg-Weiden</institution>, <addr-line>Amberg</addr-line>, <country>Germany</country></aff>
<aff id="aff2"><sup>2</sup><institution>Department of Process Engineering, Nuremberg Tech</institution>, <addr-line>Nuremberg</addr-line>, <country>Germany</country></aff>
<aff id="aff3"><sup>3</sup><institution>Chair of Food Biotechnology and Food Process Engineering, Technische Universit&#x000E4;t Berlin</institution>, <addr-line>Berlin</addr-line>, <country>Germany</country></aff>
<author-notes>
<fn fn-type="edited-by"><p>Edited by: Lutz Grossmann, University of Massachusetts Amherst, United States</p></fn>
<fn fn-type="edited-by"><p>Reviewed by: Hema Rajaram, Bhabha Atomic Research Centre (BARC), India; Priscilla Bezerra, Universit&#x000E9; Clermont Auvergne, France</p></fn>
<corresp id="c001">&#x0002A;Correspondence: Sun-Hwa Jung <email>S.Jung&#x00040;oth-aw.de</email></corresp>
<fn fn-type="other" id="fn001"><p>This article was submitted to Sustainable Food Processing, a section of the journal Frontiers in Sustainable Food Systems</p></fn></author-notes>
<pub-date pub-type="epub">
<day>19</day>
<month>05</month>
<year>2022</year>
</pub-date>
<pub-date pub-type="collection">
<year>2022</year>
</pub-date>
<volume>6</volume>
<elocation-id>883069</elocation-id>
<history>
<date date-type="received">
<day>24</day>
<month>02</month>
<year>2022</year>
</date>
<date date-type="accepted">
<day>22</day>
<month>04</month>
<year>2022</year>
</date>
</history>
<permissions>
<copyright-statement>Copyright &#x000A9; 2022 Jung, Zell, Bo&#x000DF;le, Teipel, Rauh, McHardy and Lindenberger.</copyright-statement>
<copyright-year>2022</copyright-year>
<copyright-holder>Jung, Zell, Bo&#x000DF;le, Teipel, Rauh, McHardy and Lindenberger</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>Extracellular polysaccharides, or exopolysaccharides are high&#x02013;molecular weight sugar-based polymers expressed and secreted by many microorganisms. As host organisms, the functions of exopolysaccharides are diverse, ranging from physical protection via biofilm formation, adhesion, and water retention to biological functions that are not entirely understood such as viral attachment inhibition. Industrial applications of exopolysaccharides can be found in food texture modification; for example, utilizing the hydrocolloidal properties of exopolysaccharides for thickening and gelling purposes to improve food quality and texture. Over the last decade, biologically active exopolysaccharides produced by microalgae have received attention for their potential as antiviral, antibacterial and antioxidative compounds and in the applications. However, relatively low yield and productivity are the limiting factors for full-scale industrial application. In this study, the well-known prokaryotic phototrophic microorganism <italic>Arthrospira platensis</italic> and the comparatively unknown eukaryotic unicellular green alga <italic>Chlamydomonas asymmetrica</italic> were used to evaluate the influence of different process parameters on exopolysaccharides formation and productivity. In addition to the essential control variables (light and temperature), the influence of operational techniques (batch and turbidostat) were also investigated. Although the two studied algae are differently affected by above parameters. The light intensity was the most influential parameter observed in the study, leading to differences in exopolysaccharides concentrations by a factor of 10, with the highest measured concentration for <italic>A. platensis</italic> of <italic>c</italic><sub><italic>EPS</italic></sub> &#x0003D; 0.138 g L<sup>&#x02212;1</sup> at 180 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup> and for <italic>C. asymmetrica</italic> of <italic>c</italic><sub><italic>EPS</italic></sub> &#x0003D; 1.2 g L<sup>&#x02212;1</sup> at 1,429 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup>. In continuous systems, the achieved exopolysaccharides concentrations were low compared to batch process, however, slightly higher productivities were reached. Regardless of all screened process parameters, <italic>C. asymmetrica</italic> is the better organism in terms of exopolysaccharides concentrations and productivity.</p></abstract>
<kwd-group>
<kwd><italic>A. platensis</italic></kwd>
<kwd><italic>C. asymmetrica</italic></kwd>
<kwd>exopolysaccharides</kwd>
<kwd>light</kwd>
<kwd>temperature</kwd>
<kwd>batch</kwd>
<kwd>turbidostat</kwd>
</kwd-group>
<counts>
<fig-count count="4"/>
<table-count count="2"/>
<equation-count count="6"/>
<ref-count count="52"/>
<page-count count="10"/>
<word-count count="8048"/>
</counts>
</article-meta>
</front>
<body>
<sec sec-type="intro" id="s1">
<title>Introduction</title>
<p>Polymers based on sugars are well-known for their high diversity in chemical composition and secondary structure. The innumerable chemo-diversity based on glycosidic linkage of different sugars, as well as many modifications containing non-sugar constituents (sulfates, organic acid, methyl, amino acids, or amine), leads to a big variety of possible structures (Delattre et al., <xref ref-type="bibr" rid="B11">2016</xref>). The polysaccharides (PS) have diverse structure and architecture based on their type and origin. PS have natural biological functions, starting from energy storage over structural support and cell adherence to protect the organism from various endangerments, e.g., heavy metal toxicity, desiccation, radiation, oxidation, viral infections, and predators (Li et al., <xref ref-type="bibr" rid="B30">2001</xref>; Bazaka et al., <xref ref-type="bibr" rid="B2">2011</xref>; Reichert et al., <xref ref-type="bibr" rid="B43">2017</xref>; Fritzsche et al., <xref ref-type="bibr" rid="B13">2021</xref>; Potnis et al., <xref ref-type="bibr" rid="B41">2021</xref>). The protective properties are mainly found in the secreted PS, known as extracellular polysaccharides (EPS). This sub-category of PS can further be divided into cell-bound polysaccharides (BPS) and released polysaccharides (RPS) (Cruz et al., <xref ref-type="bibr" rid="B7">2020</xref>). Besides EPS, PS are also present inside the cells, known as intracellular polysaccharides (IPS). Due to thickening, gelatinous properties and secondary functions, including emulsification, suspension stabilization, encapsulation, flocculation, film-forming and coating, PS are used in the food and cosmetic industries and also in several other processes where the rheological properties of water have to be altered for easier processing or higher commercial value (Sanford and Baird, <xref ref-type="bibr" rid="B44">1983</xref>; Lewis et al., <xref ref-type="bibr" rid="B29">2000</xref>; Paniagua-Michel et al., <xref ref-type="bibr" rid="B39">2014</xref>; Kumar et al., <xref ref-type="bibr" rid="B23">2018</xref>; Gouda et al., <xref ref-type="bibr" rid="B17">2022</xref>). The biological functions are becoming increasingly interesting for commercial application, particularly in the field of nutraceuticals and therapeutics. Recent discoveries of the antioxidative, immunomodulatory, antitumor, antithrombotic, anticoagulant, anti-inflammatory, antimicrobial, and antiviral activities of PS are of particular interest (de Jesus et al., <xref ref-type="bibr" rid="B8">2019</xref>). Whereas, PS from terrestrial plants, seaweed, fungi and non-phototrophic microorganisms are widely described in the literature, detailed information on chemical structure, rheologic properties, possible industrial relevance (i.e., information regarding process parameters and productivity) of PS obtained from microalgae and cyanobacteria are harder to find (Prybylski et al., <xref ref-type="bibr" rid="B42">2020</xref>), which could be due to lower productivities of phototrophic microorganisms.</p>
<p>EPS from microalgae and cyanobacteria are mainly non-repeating, hetero-polysaccharides with glycosidic bonds to non-carbohydrate components. Pierre et al. (<xref ref-type="bibr" rid="B40">2019</xref>) attempted to summarize the available information about the structural deviation of EPS gained from microalgae and cyanobacteria. For phylogenetically closed eukaryotic microalgae, the group concluded some general information about the chemical composition of EPS; however, such statements are less clear for cyanobacteria. The intragenus heterogeneity of EPS composition is highly distinctive (Gaignard et al., <xref ref-type="bibr" rid="B15">2019</xref>; Prybylski et al., <xref ref-type="bibr" rid="B42">2020</xref>) and the chemical diversity is also reflected by the quantity of published biological activity of EPS, occasionally even hypothesizing structure-function relationships.</p>
<p>As the efficacy of these biopolymers is significant (Li et al., <xref ref-type="bibr" rid="B30">2001</xref>; Bazaka et al., <xref ref-type="bibr" rid="B2">2011</xref>; Reichert et al., <xref ref-type="bibr" rid="B43">2017</xref>), the question arises why their commercial application, especially in the field of therapeutics, is not yet realized. One main reason lies in the economic perspective of the production process as the yield of EPS from microalgae and the cost for the upstream and downstream processing are not yet economically been found feasible and are currently the object of research projects, including Spiralg (BBI-H2020) or AnViPi (FNR Germany). The common aspect in these projects is the implantation of EPS production into a product cascade leading to a phase II biorefinery, which describes the concept of making use of side streams and byproducts to gain multiple end products from the biomass. Nevertheless, even if PS serve &#x0201C;only&#x0201D; as an added-value product, the question arises, which process parameters influence productivity or space-time yield to further increase the benefit of the process?</p>
<p>Regardless of whether microalgae and cyanobacteria grow by phototrophic, heterotrophic, or mixotrophic processes, the composition of the culture media has a significant influence on EPS production. Until now, the main focus of investigations was on the supply of the elements N, P, and S. It was found that starvation of these three nutritional components led to a higher expression of EPS into the supernatant, while the associated reduction of growth determines the overall productivity. Researchers reported optimal parameters for the supply of carbon with air being enriched with &#x0007E;2% CO<sub>2</sub> (Iqbal and Zafar, <xref ref-type="bibr" rid="B21">1993</xref>; Cheng et al., <xref ref-type="bibr" rid="B4">2015</xref>).</p>
<p>For phototrophic cultures, light supply is one of the critical process parameters concerning all products from microalgae or cyanobacteria. Generally, there is a positive effect of high light intensity on EPS (Delattre et al., <xref ref-type="bibr" rid="B11">2016</xref>). When comparing different reports, one could conclude that EPS production is enhanced at low irradiations by increasing the light supply, leading to a light inhibition at high light intensities (Trabelsi et al., <xref ref-type="bibr" rid="B49">2009</xref>; Delattre et al., <xref ref-type="bibr" rid="B11">2016</xref>; Silva et al., <xref ref-type="bibr" rid="B45">2020</xref>). The optimum light supply strongly depends on the production organism (Trabelsi et al., <xref ref-type="bibr" rid="B49">2009</xref>; Silva et al., <xref ref-type="bibr" rid="B45">2020</xref>) and the reactor system (Iqbal and Zafar, <xref ref-type="bibr" rid="B21">1993</xref>).</p>
<p>The influence of temperature on productivity is not as easy to describe and is highly species- and strain-dependent. Notably, optimum temperature for EPS production does not always overlap with the optimum culture growth temperature. <italic>Botryococcus braunii</italic> is described as being highly dependent on a narrow temperature window in which, both fast growth and high EPS production, can be achieved (Iqbal and Zafar, <xref ref-type="bibr" rid="B21">1993</xref>). For <italic>Anabaena sp.</italic>, it was observed that a sudden increase in temperature from 30 to 35&#x000B0;C (optimum growth) to 40&#x02013;45&#x000B0;C increased (4&#x02013;5-fold) the release of EPS. Similar behavior is described for <italic>Dictyosphaerium chlorelloides</italic>, where an increase of 5&#x000B0;C decreases the growth by 30% but doubles the EPS production (Kumar et al., <xref ref-type="bibr" rid="B24">2017</xref>). Other very relevant studies regarding the influence of light and temperature on EPS production for photoautotrophic growing microorganisms have been published. An overview of some outcomes is provided in <xref ref-type="table" rid="T1">Table 1</xref>.</p>
<table-wrap position="float" id="T1">
<label>Table 1</label>
<caption><p>Influences on light and temperature on EPS production in different photoautotrophic microorganisms.</p></caption>
<table frame="hsides" rules="groups">
<thead><tr>
<th valign="top" align="left"><bold>Species</bold></th>
<th valign="top" align="left"><bold>EPS concentration, yield or productivity</bold></th>
<th valign="top" align="center" colspan="2" style="border-bottom: thin solid #000000;"><bold>Temperature (&#x000B0;C)</bold></th>
<th valign="top" align="center" colspan="2" style="border-bottom: thin solid #000000;"><bold>Light (&#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup>)</bold></th>
<th valign="top" align="center"><bold>Source</bold></th>
</tr>
<tr>
<th/>
<th/>
<th valign="top" align="center"><bold>Optimum</bold></th>
<th valign="top" align="center"><bold>Tested range</bold></th>
<th valign="top" align="center"><bold>Optimum</bold></th>
<th valign="top" align="center"><bold>Tested range</bold></th>
<th/>
</tr>
</thead>
<tbody>
<tr>
<td valign="top" align="left"><italic>Porphyridium cruentum</italic></td>
<td valign="top" align="left">4.63 g L<sup>&#x02212;1</sup></td>
<td valign="top" align="center">25</td>
<td/>
<td valign="top" align="center">70</td>
<td valign="top" align="center">20-120</td>
<td valign="top" align="left">(You and Barnett, <xref ref-type="bibr" rid="B52">2004</xref>)</td>
</tr>
<tr>
<td valign="top" align="left"><italic>Cyanobacterium aponinum</italic></td>
<td valign="top" align="left">0.084 g g<sup>&#x02212;1</sup></td>
<td valign="top" align="center">35</td>
<td valign="top" align="center">28&#x02013;45</td>
<td valign="top" align="center">15</td>
<td valign="top" align="center">15&#x02013;650</td>
<td valign="top" align="left">(Gris et al., <xref ref-type="bibr" rid="B18">2017</xref>)</td>
</tr>
<tr>
<td valign="top" align="left"><italic>Anabaena sp</italic></td>
<td valign="top" align="left">12.5 g L<sup>&#x02212;1</sup></td>
<td/>
<td/>
<td valign="top" align="center">460</td>
<td valign="top" align="center">115-1840</td>
<td valign="top" align="left">(Moreno et al., <xref ref-type="bibr" rid="B34">1998</xref>)</td>
</tr>
<tr>
<td valign="top" align="left"><italic>Spirulina sp</italic>.</td>
<td valign="top" align="left">0.13 g g<sup>&#x02212;1</sup></td>
<td valign="top" align="center">30</td>
<td/>
<td valign="top" align="center">10</td>
<td valign="top" align="center">10&#x02013;120</td>
<td valign="top" align="left">(Chentir et al., <xref ref-type="bibr" rid="B5">2017</xref>)</td>
</tr>
<tr>
<td valign="top" align="left"><italic>Scenedesmus obliquus</italic></td>
<td valign="top" align="left">0.024 g L<sup>&#x02212;1</sup></td>
<td/>
<td/>
<td valign="top" align="center">180</td>
<td valign="top" align="center">80&#x02013;180</td>
<td valign="top" align="left">(Castro et al., <xref ref-type="bibr" rid="B3">2012</xref>)</td>
</tr>
<tr>
<td valign="top" align="left"><italic>Pophyridium marinum</italic></td>
<td valign="top" align="left">0.15 g L<sup>&#x02212;1</sup> d<sup>&#x02212;1</sup></td>
<td valign="top" align="center">28</td>
<td valign="top" align="center">24&#x02013;28</td>
<td valign="top" align="center">360</td>
<td valign="top" align="center">200 &#x00026; 360</td>
<td valign="top" align="left">(Soanen et al., <xref ref-type="bibr" rid="B47">2016</xref>)</td>
</tr>
<tr>
<td valign="top" align="left"><italic>Chlorophyta grasiella</italic></td>
<td valign="top" align="left">11.8 g L<sup>&#x02212;1</sup>d<sup>&#x02212;1</sup></td>
<td valign="top" align="center">40</td>
<td valign="top" align="center">20&#x02013;40</td>
<td valign="top" align="center">20</td>
<td valign="top" align="center">20-120</td>
<td valign="top" align="left">(Mezhoud et al., <xref ref-type="bibr" rid="B33">2014</xref>)</td>
</tr>
<tr>
<td valign="top" align="left"><italic>Botryococcus braunii</italic></td>
<td valign="top" align="left">4.5 g L<sup>&#x02212;1</sup></td>
<td valign="top" align="center">25&#x02013;30</td>
<td valign="top" align="center">20&#x02013;33</td>
<td valign="top" align="center">250</td>
<td/>
<td valign="top" align="left">(Lupi et al., <xref ref-type="bibr" rid="B31">1991</xref>)</td>
</tr>
<tr>
<td valign="top" align="left"><italic>Rhodella violacea</italic></td>
<td valign="top" align="left">0.59 g L<sup>&#x02212;1</sup></td>
<td/>
<td valign="top" align="center">10&#x02013;30</td>
<td/>
<td valign="top" align="center">150 &#x00026; 420</td>
<td valign="top" align="left">(Villay et al., <xref ref-type="bibr" rid="B50">2013</xref>)</td>
</tr>
<tr>
<td valign="top" align="left"><italic>Phaeodactylum tricornutum</italic></td>
<td valign="top" align="left">0.140 g L<sup>&#x02212;1</sup></td>
<td valign="top" align="center">25</td>
<td valign="top" align="center">20-25</td>
<td/>
<td/>
<td valign="top" align="left">(Nur et al., <xref ref-type="bibr" rid="B37">2019</xref>)</td>
</tr>
<tr>
<td valign="top" align="left"><italic>Arthrospira platensis</italic></td>
<td valign="top" align="left">0.219 g L<sup>&#x02212;1</sup></td>
<td/>
<td valign="top" align="center">32</td>
<td valign="top" align="center">100</td>
<td/>
<td valign="top" align="left">(Trabelsi et al., <xref ref-type="bibr" rid="B49">2009</xref>)</td>
</tr>
<tr>
<td valign="top" align="left"><italic>Arthrospira platensis</italic></td>
<td valign="top" align="left">0.146 g L<sup>&#x02212;1</sup></td>
<td/>
<td valign="top" align="center">28</td>
<td valign="top" align="center">192</td>
<td valign="top" align="center">24-192</td>
<td valign="top" align="left">(Lee et al., <xref ref-type="bibr" rid="B27">2012</xref>)</td>
</tr>
<tr>
<td valign="top" align="left"><italic>Arthrospira platensis</italic></td>
<td valign="top" align="left">0.141 g L<sup>&#x02212;1</sup></td>
<td valign="top" align="center">38</td>
<td valign="top" align="center">18&#x02013;38</td>
<td/>
<td valign="top" align="center">36</td>
<td/>
</tr>
<tr>
<td valign="top" align="left"><italic>Arthrospira platensis</italic></td>
<td valign="top" align="left">0.138 g L<sup>&#x02212;1</sup></td>
<td/>
<td valign="top" align="center">35</td>
<td valign="top" align="center">180</td>
<td valign="top" align="center">74-975</td>
<td valign="top" align="left">This study</td>
</tr>
<tr>
<td valign="top" align="left"><italic>Arthrospira platensis</italic></td>
<td valign="top" align="left">0.065 g L<sup>&#x02212;1</sup></td>
<td valign="top" align="center">38</td>
<td valign="top" align="center">20&#x02013;38</td>
<td valign="top" align="center">277</td>
<td/>
<td/>
</tr>
<tr>
<td valign="top" align="left"><italic>Chlamydomonas asymmetrica</italic></td>
<td valign="top" align="left">0.56 g L<sup>&#x02212;1</sup></td>
<td valign="top" align="center">30</td>
<td valign="top" align="center">15&#x02013;35</td>
<td/>
<td valign="top" align="center">476</td>
<td/>
</tr>
<tr>
<td valign="top" align="left"><italic>Chlamydomonas asymmetrica</italic></td>
<td valign="top" align="left">1.2 g L<sup>&#x02212;1</sup></td>
<td/>
<td valign="top" align="center">30</td>
<td valign="top" align="center">1,429</td>
<td valign="top" align="center">96-1429</td>
<td/>
</tr>
<tr>
<td valign="top" align="left"><italic>Nostoc sp</italic>.</td>
<td valign="top" align="left">0.134 g g<sup>&#x02212;1</sup></td>
<td/>
<td valign="top" align="center">25</td>
<td valign="top" align="center">80</td>
<td valign="top" align="center">40 &#x00026; 80</td>
<td valign="top" align="left">(Ge et al., <xref ref-type="bibr" rid="B16">2014</xref>)</td>
</tr>
</tbody>
</table>
</table-wrap>
<p>In this study, the prokaryotic microalga <italic>Arthrospira platensis</italic> and the eukaryotic unicellular green alga <italic>Chlamydomonas asymmetrica</italic> were used to identify the influence of process parameters and operational techniques on the formation and productivity of EPS, hoping to find some intragenus trends by investigating to microorganism from different domains.</p>
<p><italic>Arthrospira platensis</italic> is a well-known and studied cyanobacteria, limited information has been published about <italic>C. asymmetrica</italic>, a recent study by group of researchers shows its prospect as a lutein production organism, reporting lutein concentrations of up to 30 mg per gram dry biomass (Hahm et al., <xref ref-type="bibr" rid="B19">2021</xref>).</p></sec>
<sec sec-type="materials and methods" id="s2">
<title>Materials and Methods</title>
<sec>
<title>Microalgae Strain and Cultivation</title>
<p>The cyanobacterium <italic>Arthrospira platensis</italic> (NIES-39) was obtained from the National Institute for Environmental Studies (NIES Collection, Tsukuba, JAPAN) and cultivated in SOT-media according to the formulation recommended by NIES (Ogawa and Terui, <xref ref-type="bibr" rid="B38">1970</xref>). The green alga <italic>Chlamydomonas asymmetrica</italic> was self-isolated from freshwater habitats in South Korea. The cultivation medium of <italic>C. asymmetrica</italic> was the artificial fresh water medium (AF6), according to the formulation of Watanabe (Andersen et al., <xref ref-type="bibr" rid="B1">2005</xref>).</p>
<p>The precultures of both strains were cultivated in shake flasks with a liquid height of approximately 3 cm (T = 25&#x000B0;C, PFD = 250 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup>). For inoculation of the main experiments, biomass from the late exponential phase of the preculture was diluted to a starting optical density (OD) of 0.1. For the cultivation, cylindrical bubble column reactor systems (volume = ca. 800 mL, diameter = 5 cm) were used. The aeration was kept constant at approximately 1.0 vvm with sterile compressed air. For the experiments with <italic>C. asymmetrica</italic>, aeration occurred with air enriched with 3% CO<sub>2</sub>. Light was supplied continuously (24 h) from 4 directions (Mitras LB2, 60 daylight, GHL), and the intensity was measured at nine different points on the reactor surface using a light meter (LI-250A, LI-COR). The irradiation varied from 50 to 975 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup> for <italic>A. platensis</italic> and from 96 to 1,429 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup> for <italic>C. asymmetrica</italic>. The temperature ranged between 15 and 35&#x000B0;C for <italic>C. asymmetrica</italic> and 25&#x02013;38&#x000B0;C for <italic>A. platensis</italic>. For temperature measurement, a combined pH/temperature electrode was placed in the reactor (Polilyte plus, Hamilton). The continuous reactors were controlled by an adjustable feed pump (SK-BQ50, Longer Precision Pump Co., Ltd, CHN) and a level controller. Samples were taken once the culture reached an equilibrium state for a set of parameters. In this study the results of EPS concentration, yield or space-time yields represent the average of three biological and a minimum three technical replicates and the error bars indicate the standard deviation with <italic>n</italic> &#x0003E; 9.</p></sec>
<sec>
<title>Biomass and EPS Quantification</title>
<p>For the tracking the culture development, the biomass was quantified in terms of OD at 750 nm [UV-1800 (Shimadzu), UV7 spectrometer (Mettler Toledo)], with the pure medium used as a blank value. Measurement at 750 nm avoids interference with light absorption of by cellular pigments (chlorophyll, carotenoids, and phycobilins). The OD values were calibrated to the dry biomass weight for each used photometer and species. The growth rates (&#x003BC; [d<sup>&#x02212;1</sup>]) were calculated by fitting the experimental data from the batch experiments to an empirical growth model (Jung et al., <xref ref-type="bibr" rid="B22">2021</xref>). To ensure comparability of single cultivations with different process parameters, the model was fitted to all cultivations using a global light affinity constant <italic>K</italic><sub><italic>S</italic></sub> and a temperature-dependent &#x003BC;<sub>max</sub>. The light affinity constant (<italic>K</italic><sub><italic>S</italic></sub>) for the two algae is different but assumed to be constant for different temperatures and light intensities. In the model used here, the light dependency of &#x003BC; is supposed to follow a Monod kinetic so that the overall average growth rate (&#x003BC;<sub>max</sub>) is global for different light intensities. The relative <italic>R</italic><sup>2</sup> combined with the standard percentage error (SPE) are used as an optimality criterion (<xref ref-type="table" rid="T2">Table 2</xref>).</p>
<table-wrap position="float" id="T2">
<label>Table 2</label>
<caption><p>Results of non-linear zero-bias relative least squares regression.</p></caption>
<table frame="hsides" rules="groups">
<thead><tr>
<th valign="top" align="left"><bold>Algae</bold></th>
<th valign="top" align="center"><bold>Temperature</bold><break/> <bold>(&#x000B0;C)</bold></th>
<th valign="top" align="center"><bold><italic><inline-formula><mml:math id="M1"><mml:msub><mml:mrow><mml:mover class="overset"><mml:mrow><mml:mi>&#x003BC;</mml:mi></mml:mrow><mml:mrow><mml:mover accent="false" class="mml-overline"><mml:mrow></mml:mrow><mml:mo accent="true">&#x000AF;</mml:mo></mml:mover></mml:mrow></mml:mover></mml:mrow><mml:mrow><mml:mo class="qopname">max</mml:mo></mml:mrow></mml:msub></mml:math></inline-formula></italic></bold><break/><bold>(d<sup><bold>&#x02212;1</bold></sup>)</bold></th>
<th valign="top" align="center"><bold><italic>K</italic><sub>S</sub></bold><break/><bold>(&#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup>)</bold></th>
<th valign="top" align="center"><bold>Relative</bold><break/><bold><italic>R<sup>2</sup></italic></bold></th>
<th valign="top" align="center"><bold>Standard percentage error <italic>SPE</italic></bold></th>
<th valign="top" align="center"><bold>Average relative error</bold></th>
</tr>
</thead>
<tbody>
<tr>
<td valign="top" align="left"><italic>Arthrospira platensis</italic></td>
<td valign="top" align="center">25</td>
<td valign="top" align="center">1.45</td>
<td valign="top" align="center">61.2</td>
<td valign="top" align="center">0.955</td>
<td valign="top" align="center">15.5%</td>
<td valign="top" align="center">&#x000B1;9.4%</td>
</tr>
<tr>
<td/>
<td valign="top" align="center">30</td>
<td valign="top" align="center">1.76</td>
<td/>
<td/>
<td/>
<td valign="top" align="center">&#x000B1;8.5%</td>
</tr>
<tr>
<td/>
<td valign="top" align="center">35</td>
<td valign="top" align="center">2.12</td>
<td/>
<td/>
<td/>
<td valign="top" align="center">&#x000B1;11.0%</td>
</tr>
<tr>
<td/>
<td valign="top" align="center">38</td>
<td valign="top" align="center">2.36</td>
<td/>
<td/>
<td/>
<td valign="top" align="center">&#x000B1;17.0%</td>
</tr>
<tr>
<td valign="top" align="left"><italic>Chlamydomonas asymmetrica</italic></td>
<td valign="top" align="center">15</td>
<td valign="top" align="center">1.59</td>
<td valign="top" align="center">87.0</td>
<td valign="top" align="center">0.977</td>
<td valign="top" align="center">9.2%</td>
<td valign="top" align="center">&#x000B1;8.5%</td>
</tr>
<tr>
<td/>
<td valign="top" align="center">20</td>
<td valign="top" align="center">2.04</td>
<td/>
<td/>
<td/>
<td valign="top" align="center">&#x000B1;6.7%</td>
</tr>
<tr>
<td/>
<td valign="top" align="center">25</td>
<td valign="top" align="center">2.60</td>
<td/>
<td/>
<td/>
<td valign="top" align="center">&#x000B1;5.6%</td>
</tr>
<tr>
<td/>
<td valign="top" align="center">30</td>
<td valign="top" align="center">3.29</td>
<td/>
<td/>
<td/>
<td valign="top" align="center">&#x000B1;6.0%</td>
</tr>
</tbody>
</table>
</table-wrap>
<p>The EPS quantification was conducted using a modified method of the total carbohydrate quantification developed by DuBois et al. (<xref ref-type="bibr" rid="B12">1951</xref>) and Nielsen (<xref ref-type="bibr" rid="B36">2003</xref>). Cell-free supernatant was used for the measurement so that the detected carbohydrates can be correlated to the RPS. Even though the total carbohydrate content in the media increases when the culture remains in the stationary phase, the result in this publication refer to the early stationary phase to avoid biases by leakage of intracellular polysaccharides (IPS).</p>
<p>Samples taken from the photobioreactors during cultivation were centrifuged (4,500 g, 10 min) and the cell-free supernatants were kept frozen (&#x02212;20&#x000B0;C) for further analysis. For the Dubois assay, 160 &#x003BC;L of supernatant was added to 1.5 mL safety reaction tubes along with 160 &#x003BC;L of phenol solution (5 wt. %). Then, 800 &#x003BC;L of concentrated sulfuric acid (&#x0003E;95%) rapidly added to the mixture by pipetting. Reproducible mixing was ensured by sucking the reaction mixture into the pipette and ejecting it back into the reaction tube. The mixing was repeated three times. After incubation at room temperature (10 min., ca. 21&#x000B0;C), the reaction took place at 30&#x000B0;C for 20 min before recording the absorbance spectra between 190 and 1,100 nm using spectrophotometer (Mettler Toledo, UV7). From this spectrum the spectrum of deionized water was subtracted as a blank. Since the method requires a calibration in terms of a reference carbohydrate, aqueous glucose standards were analyzed along with the samples. The absorbance at 490 nm served as a reference for quantification. For the subsequent analysis, the raw spectra were smoothed with a triangular filter and then approximated with finite difference derivation.</p>
<p>During the Dubois assay, ionic species of nitrous oxides, namely nitrate (NO<inline-formula><mml:math id="M2"><mml:msubsup><mml:mrow></mml:mrow><mml:mrow><mml:mn>3</mml:mn></mml:mrow><mml:mrow><mml:mo>-</mml:mo></mml:mrow></mml:msubsup></mml:math></inline-formula>) and especially nitrite (NO<inline-formula><mml:math id="M3"><mml:msubsup><mml:mrow></mml:mrow><mml:mrow><mml:mn>2</mml:mn></mml:mrow><mml:mrow><mml:mo>-</mml:mo></mml:mrow></mml:msubsup></mml:math></inline-formula>), also participate in reactions with phenol and form products with high absorbance over the full VIS-region of the spectrum. The assay was carried out for aqueous mixtures of glucose, fructose, sodium nitrate, and sodium nitrite to correct their influences. Afterward, the spectra of glucose and fructose, calculated from a calibration using pure aqueous standards, were subtracted from the processed spectrum of the sample to obtain the background caused by NO<inline-formula><mml:math id="M4"><mml:msubsup><mml:mrow></mml:mrow><mml:mrow><mml:mn>3</mml:mn></mml:mrow><mml:mrow><mml:mo>-</mml:mo></mml:mrow></mml:msubsup></mml:math></inline-formula> and NO<inline-formula><mml:math id="M5"><mml:msubsup><mml:mrow></mml:mrow><mml:mrow><mml:mn>2</mml:mn></mml:mrow><mml:mrow><mml:mo>-</mml:mo></mml:mrow></mml:msubsup></mml:math></inline-formula>. Using the spectral region with wavelengths above 600 nm, which is unaffected by the carbohydrate spectra, the obtained background at 490 nm was fitted to two characteristic points from the original spectra, by a combination of weighted multiple linear regression and an evolutionary algorithm for wavelength selection. With this method, the best fit (<italic>wR</italic><sup>2</sup> = 0.9929, <italic>wQ</italic><sup>2</sup> = 0.9900) was found to be:</p>
<disp-formula id="E1"><label>(1)</label><mml:math id="M6"><mml:mtable class="eqnarray" columnalign="right center left"><mml:mtr><mml:mtd><mml:msub><mml:mrow><mml:mi>A</mml:mi></mml:mrow><mml:mrow><mml:msup><mml:mrow><mml:mi>N</mml:mi><mml:msub><mml:mrow><mml:mi>O</mml:mi></mml:mrow><mml:mrow><mml:mi>x</mml:mi></mml:mrow></mml:msub></mml:mrow><mml:mrow><mml:mo>-</mml:mo></mml:mrow></mml:msup><mml:mo>;</mml:mo><mml:mn>490</mml:mn></mml:mrow></mml:msub><mml:mo>=</mml:mo><mml:mn>1</mml:mn><mml:mo>.</mml:mo><mml:mn>376</mml:mn><mml:mo>&#x000B7;</mml:mo><mml:msub><mml:mrow><mml:mi>A</mml:mi></mml:mrow><mml:mrow><mml:mn>660</mml:mn></mml:mrow></mml:msub><mml:mo>-</mml:mo><mml:mn>51</mml:mn><mml:mo>.</mml:mo><mml:mn>53</mml:mn><mml:mo>&#x000B7;</mml:mo><mml:msub><mml:mrow><mml:mrow><mml:mo stretchy="false">(</mml:mo><mml:mrow><mml:mfrac><mml:mrow><mml:mi>d</mml:mi><mml:mi>A</mml:mi></mml:mrow><mml:mrow><mml:mi>d</mml:mi><mml:mi>&#x003BB;</mml:mi></mml:mrow></mml:mfrac></mml:mrow><mml:mo stretchy="false">)</mml:mo></mml:mrow></mml:mrow><mml:mrow><mml:mn>740</mml:mn></mml:mrow></mml:msub></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula>
<p>The first summand of Equation 1 accounts for both NO<inline-formula><mml:math id="M7"><mml:msubsup><mml:mrow></mml:mrow><mml:mrow><mml:mn>3</mml:mn></mml:mrow><mml:mrow><mml:mo>-</mml:mo></mml:mrow></mml:msubsup></mml:math></inline-formula> and NO<inline-formula><mml:math id="M8"><mml:msubsup><mml:mrow></mml:mrow><mml:mrow><mml:mn>2</mml:mn></mml:mrow><mml:mrow><mml:mo>-</mml:mo></mml:mrow></mml:msubsup></mml:math></inline-formula>, whereas the second summand mainly considers NO<inline-formula><mml:math id="M9"><mml:msubsup><mml:mrow></mml:mrow><mml:mrow><mml:mn>2</mml:mn></mml:mrow><mml:mrow><mml:mo>-</mml:mo></mml:mrow></mml:msubsup></mml:math></inline-formula>, whose reaction products dominate the first order derivative of the spectra. For quantification purposes, Equation 1 is applied to correct the measured absorbance at 490 nm before calculating the total carbohydrate concentration from a calibration with aqueous glucose standards, which leads to Equation 2. The protocol of the Dubois assay remains unchanged.</p>
<disp-formula id="E2"><label>(2)</label><mml:math id="M10"><mml:mtable class="eqnarray" columnalign="right center left"><mml:mtr><mml:mtd><mml:msub><mml:mrow><mml:mi>&#x003B2;</mml:mi></mml:mrow><mml:mrow><mml:mi>R</mml:mi><mml:mi>e</mml:mi><mml:mi>f</mml:mi><mml:mo>-</mml:mo><mml:mi>C</mml:mi><mml:mi>a</mml:mi><mml:mi>r</mml:mi><mml:mi>b</mml:mi></mml:mrow></mml:msub><mml:mo>=</mml:mo><mml:mfrac><mml:mrow><mml:msub><mml:mrow><mml:mi>A</mml:mi></mml:mrow><mml:mrow><mml:mn>490</mml:mn></mml:mrow></mml:msub><mml:mo>-</mml:mo><mml:msub><mml:mrow><mml:mi>A</mml:mi></mml:mrow><mml:mrow><mml:msup><mml:mrow><mml:mi>N</mml:mi><mml:msub><mml:mrow><mml:mi>O</mml:mi></mml:mrow><mml:mrow><mml:mi>x</mml:mi></mml:mrow></mml:msub></mml:mrow><mml:mrow><mml:mo>-</mml:mo></mml:mrow></mml:msup><mml:mo>;</mml:mo><mml:mn>490</mml:mn></mml:mrow></mml:msub></mml:mrow><mml:mrow><mml:msub><mml:mrow><mml:mi>&#x003B5;</mml:mi></mml:mrow><mml:mrow><mml:mi>R</mml:mi><mml:mi>e</mml:mi><mml:mi>f</mml:mi><mml:mo>;</mml:mo><mml:mn>490</mml:mn></mml:mrow></mml:msub><mml:mo>&#x000B7;</mml:mo><mml:mi>d</mml:mi></mml:mrow></mml:mfrac></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula>
<p>The results of the EPS measurement is given in three different forms: the EPS concentration (<italic>c</italic><sub><italic>EPS</italic></sub>) in g L<sup>&#x02212;1</sup>; the specific product yield coefficient (<italic>Y</italic><sub><italic>EPS</italic>/<italic>X</italic></sub>) in g g<sup>&#x02212;1</sup>, which calculates by the quotient of the EPS concentration and the measured dry biomass concentration (&#x003C7;); and&#x02014;as an indicator for productivity&#x02014;the space-time yield of EPS (<italic>STY</italic><sub><italic>EPS</italic></sub>) in g L<sup>&#x02212;1</sup> d<sup>&#x02212;1</sup> (Equation 3).</p>
<disp-formula id="E5"><label>(3)</label><mml:math id="M11"><mml:mtable class="eqnarray" columnalign="right center left"><mml:mtr><mml:mtd><mml:mi>S</mml:mi><mml:mi>T</mml:mi><mml:msub><mml:mrow><mml:mi>Y</mml:mi></mml:mrow><mml:mrow><mml:mi>E</mml:mi><mml:mi>P</mml:mi><mml:mi>S</mml:mi></mml:mrow></mml:msub><mml:mo>=</mml:mo><mml:mtext>&#x000A0;</mml:mtext><mml:mfrac><mml:mrow><mml:mi>&#x00394;</mml:mi><mml:msub><mml:mrow><mml:mi>c</mml:mi></mml:mrow><mml:mrow><mml:mi>E</mml:mi><mml:mi>P</mml:mi><mml:mi>S</mml:mi></mml:mrow></mml:msub></mml:mrow><mml:mrow><mml:mi>&#x00394;</mml:mi><mml:mi>t</mml:mi></mml:mrow></mml:mfrac></mml:mtd></mml:mtr></mml:mtable></mml:math></disp-formula>
<p>For batch processes delta (&#x00394;) refers to the differences between inoculum and measurement. For continuous systems, the time difference is the hydraulic retention time, and <italic>c</italic><sub><italic>EPS</italic></sub> refers to the difference between the concentrations at the inlet and outlet of the reactor. In this study the results of EPS concentration, yield or space-time yields represent the average of three biological and a minimum three technical replicates and the error bars indicate the standard deviation with <italic>n</italic> &#x0003E; 9.</p></sec></sec>
<sec sec-type="results" id="s3">
<title>Results</title>
<sec>
<title>Growth Characterization</title>
<p>To avoid a false interpretation of the EPS concentration, the provided data of the batch experiments are derived from measurements in the early stationary phase, right after transmission from the exponential phase.</p>
<p><xref ref-type="fig" rid="F1">Figure 1</xref> shows examples of <italic>A. platensis</italic> and <italic>C. asymmetrica</italic> growth to indicate the sampling point for EPS. The growth rates in this study refer to the highest achieved growth rates (&#x003BC;) without light limitation, evaluated by fitting the experimental values to the model of Jung et al. (<xref ref-type="bibr" rid="B22">2021</xref>). The results and the quality of the fitting are summarized in <xref ref-type="table" rid="T2">Table 2</xref>.</p>
<fig id="F1" position="float">
<label>Figure 1</label>
<caption><p>Culture development of <italic>Arthrospira platensis</italic> (open circles) cultivated at 35&#x000B0;C and 180 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup> and <italic>C. asymmetrica</italic> (open squares) at 30&#x000B0;C and 1,429 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup>. The error bars indicate the standard deviation of three independent measurements. The solid lines indicate the simulation of the growth behavior. The arrows indicate the beginning of the stationary phase, where sampling was carried out.</p></caption>
<graphic mimetype="image" mime-subtype="tiff" xlink:href="fsufs-06-883069-g0001.tif"/>
</fig></sec>
<sec>
<title>Temperature Effects</title>
<p>The effect of temperature on the growth rate of <italic>A. platensis</italic> was determined between 20 and 38&#x000B0;C at a constant light intensity of 277 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup> (<xref ref-type="fig" rid="F2">Figure 2A</xref>). The highest specific growth rate was observed at 38&#x000B0;C (&#x003BC;= 1.98 d<sup>&#x02212;1</sup>). With decreasing temperature, the specific growth rate steadily declines to 1.32 d<sup>&#x02212;1</sup> at 25&#x000B0;C, and then drops to 0.4 at 20&#x000B0;C. Due to the low growth at 20&#x000B0;C, the comparably high EPS concentrations of <italic>c</italic><sub><italic>EPS</italic></sub>= 0.051 g L<sup>&#x02212;1</sup> (where <italic>Y</italic><sub><italic>EPS</italic>/<italic>X</italic></sub> &#x0003D; 0.053 g g<sup>&#x02212;1</sup>) resulted in low EPS productivities of <italic>STY</italic><sub><italic>EPS</italic></sub> &#x0003D; 0.003 g L<sup>&#x02212;1</sup> d<sup>&#x02212;1</sup>.</p>
<fig id="F2" position="float">
<label>Figure 2</label>
<caption><p>Effect of temperature on the EPS concentration (black), EPS yield (gray), space-time yield (white) and specific growth (white circles) in batch processes for <bold>(A)</bold> <italic>A. platensis</italic> cultivated at 277 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup>, and <bold>(B)</bold> <italic>C. asymmetrica</italic> cultivated at 476 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup>.</p></caption>
<graphic mimetype="image" mime-subtype="tiff" xlink:href="fsufs-06-883069-g0002.tif"/>
</fig>
<p>At temperature above 20&#x000B0;C, the EPS concentration and <italic>Y</italic><sub><italic>EPS</italic>/<italic>X</italic></sub> steadily increased from <italic>c</italic><sub><italic>EPS</italic></sub> &#x0003D; 0.023 g L<sup>&#x02212;1</sup> (<italic>Y</italic><sub><italic>EPS</italic>/<italic>X</italic></sub> &#x0003D; 0.012 g g<sup>&#x02212;1</sup>) at 25&#x000B0;C to <italic>c</italic><sub><italic>EPS</italic></sub> &#x0003D; 0.065 g L<sup>&#x02212;1</sup> (<italic>Y</italic><sub><italic>EPS</italic>/<italic>X</italic></sub> &#x0003D; 0.066 g g<sup>&#x02212;1</sup>) at 38&#x000B0;C. It should be noted that determined EPS yield/concentration at 20&#x000B0;C must be considered uncertain as the culture contained a lot of cell debris and small broken cells so that the quantified carbohydrates do not necessarily represent released EPS. The space-time yields also enhanced with increasing temperature and reached plateaus at approximately <italic>STY</italic><sub><italic>EPS</italic></sub> &#x0003D; 0.02 g L<sup>&#x02212;1</sup> d<sup>&#x02212;1</sup> for the two highest temperatures.</p>
<p>The experiments for determining the temperature influence on <italic>C. asymmetrica</italic> (<xref ref-type="fig" rid="F2">Figure 2B</xref>) were performed at a light intensity of 476 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup>. The green alga achieves slightly higher growth rates compared to <italic>A. platensis</italic> with an optimum temperature at &#x0007E;30&#x000B0;C with &#x003BC; &#x0003D; 2.27 d<sup>&#x02212;1</sup>. Higher temperatures result in a substantial reduction of growth to &#x003BC; &#x0003D; 0.7 d<sup>&#x02212;1</sup> at 35&#x000B0;C. While with decrease in the temperature, growth reduces steadily to a rate of 1.0 d<sup>&#x02212;1</sup> at 15&#x000B0;C.</p>
<p>The EPS concentration and yield at 15&#x000B0;C were higher than at 20&#x000B0;C, whereas the space-time yield at 20&#x000B0;C was 20% higher than at 15&#x000B0;C. The highest EPS concentration was measured at 30&#x000B0;C with <italic>c</italic><sub><italic>EPS</italic></sub> &#x0003D; 0.56 g L<sup>&#x02212;1</sup>, resulting in <italic>Y</italic><sub><italic>EPS</italic>/<italic>X</italic></sub> = 0.86 g g<sup>&#x02212;1</sup> and <italic>STY</italic><sub><italic>EPS</italic></sub> &#x0003D; 0.24 g L<sup>&#x02212;1</sup>d<sup>&#x02212;1</sup>. It is worth mentioning that the temperature had the most substantial effect on EPS yield, resulting in a more than 10-fold increase compared to the lowest value obtained at 20&#x000B0;C (<italic>Y</italic><sub><italic>EPS</italic>/<italic>X</italic></sub> &#x0003D; 0.067 g g<sup>&#x02212;1</sup>). Due to the high level of cell breakage in the experiments at 35&#x000B0;C, the carbohydrate quantification of the supernatant at this temperature is not displayed.</p></sec>
<sec>
<title>Light Effects</title>
<p>The experiments to investigate the influence of light on EPS production were conducted at 30&#x000B0;C for <italic>C. asymmetrica</italic> cultures and 35&#x000B0;C for <italic>A. platensis</italic> cultures. As the light supply in algae cultures is not a static parameter but is strongly influenced by the growing biomass (self-shading effects), different process modes were investigated. Batch processes, or repeated batches, are the most common production mode as the process control is straightforward. Furthermore, due to high biomass and product concentrations reached in batch processes, downstream processing is often more economical. Nevertheless, the drawback of this cultivation method is the changing biomass concentration and, hence, the impracticality of establishing a causal relation between light supply and product formation. Turbidostat process control overcomes these issues, as the culture is kept at a constant biomass concentration and, therefore, maintains a constant influence of self-shading. A constant biomass concentration of 1 g L<sup>&#x02212;1</sup> was chosen in our experiments.</p></sec>
<sec>
<title>Batch Cultivation</title>
<p>In the investigated range of light intensities, the influence of the light intensity on the growth rate of <italic>A. platensis</italic> (<xref ref-type="fig" rid="F3">Figure 3A</xref>) can be described with the Monod kinetics, choosing the light supply as the limiting substrate. Using the kinetic model introduced by Jung et al. (<xref ref-type="bibr" rid="B22">2021</xref>), the biomass development of all cultures can be simulated using <italic>K</italic><sub><italic>S</italic></sub> = 61.2 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup> and &#x003BC;<sub>max</sub> = 2.39 d<sup>&#x02212;1</sup>. The best match between model and experiments was achieved for the cultivation at 277 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup>.</p>
<fig id="F3" position="float">
<label>Figure 3</label>
<caption><p>Influence of light on the EPS concentration (black), EPS yield (gray), space-time yield (white), and specific growth (white circles) in batch processes for <bold>(A)</bold> <italic>A. platensis</italic> cultivated at 35&#x000B0;C, and <bold>(B)</bold> <italic>C. asymmetrica</italic> cultivated at 30&#x000B0;C.</p></caption>
<graphic mimetype="image" mime-subtype="tiff" xlink:href="fsufs-06-883069-g0003.tif"/>
</fig>
<p>The highest EPS concentration at low light intensities was 0.138 g L<sup>&#x02212;1</sup> for cultivation at 180 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup>, whereas in the cultivation at 74 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup> the highest EPS yield observed was 0.166 g g<sup>&#x02212;1</sup>. The EPS concentration and yield at these low light intensities were 10-fold higher than in the experiments with irradiation of 440 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup> and above. The influence of light intensity on the space-time yield of EPS is not as strong, with the highest value of 0.024 g L<sup>&#x02212;1</sup> d<sup>&#x02212;1</sup> observed at 180 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup>, and the lowest value of 0.012 g L<sup>&#x02212;1</sup> d<sup>&#x02212;1</sup> at 975 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup>.</p>
<p><italic>Chlamydomonas asymmetrica</italic> (<xref ref-type="fig" rid="F3">Figure 3B</xref>) has a slightly higher light affinity (compared to <italic>A. platensis</italic>) with <italic>K</italic><sub><italic>S</italic></sub> = 87 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup>. The volume-averaged growth rate was estimated to be &#x003BC;<sub>max</sub> &#x0003D; 2.64 d<sup>&#x02212;1</sup>. The highest growth rate was 2.5 d<sup>&#x02212;1</sup> at 1,429 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup>. At a light intensity of 96 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup>, the culture still achieved a growth rate of 1.5 d<sup>&#x02212;1</sup>. Light positively influences EPS production, leading to higher concentrations, yields, and space-time yields. The concentration increases approximately by a factor 10 from <italic>c</italic><sub><italic>EPS</italic></sub> &#x0003D; 0.13 g L<sup>&#x02212;1</sup> at 96 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup> to <italic>c</italic><sub><italic>EPS</italic></sub> &#x0003D; 1.4 g L<sup>&#x02212;1</sup> at the highest light intensity. As a consequence of the higher concentrations and growth rates, the space-time yield increases by a factor of 30, reaching <italic>STY</italic><sub><italic>EPS</italic></sub> &#x0003D; 0.84 g L<sup>&#x02212;1</sup>d<sup>&#x02212;1</sup> at 1,429 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup>. The maximum EPS yield is obtained at 953 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup> where <italic>Y</italic><sub><italic>EPS</italic>/<italic>X</italic></sub> &#x0003D; 1.12 g g<sup>&#x02212;1</sup>, which corresponds to a 3.2-fold increase compared to that at the lowest light intensity.</p>
<p>The separate investigations on the parameter influence of temperature and light on EPS production with <italic>C. asymmetrica</italic> lead to a combined optimum of 30&#x000B0;C and 1,429 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup>. For <italic>A. platensis</italic>, the light intensity screening was not conducted at the suggested optimum temperature of 38&#x000B0;C; instead at 35&#x000B0;C. Additional cultivations using the combination of the indicated optimal parameters (e.g., 38&#x000B0;C and 180 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup>) led to a concentration of <italic>c</italic><sub><italic>EPS</italic></sub> &#x0003D; 0.116 g L<sup>&#x02212;1</sup>, a yield of <italic>Y</italic><sub><italic>EPS</italic>/<italic>X</italic></sub>= 0.098 g g<sup>&#x02212;1</sup> and a space-time yield of <italic>STY</italic><sub><italic>EPS</italic></sub> &#x0003D; 0.0259 g L<sup>&#x02212;1</sup>d<sup>&#x02212;1</sup>, which are just slightly lower than the values obtained at 35&#x000B0;C at the same light intensity.</p></sec>
<sec>
<title>Continuous Process</title>
<p>As steady-state conditions are not reached in batch cultures, conclusions about parameter influences may be strongly biased to the culture&#x00027;s state at the time of sampling. For example, the light availability in the culture decreases with increasing biomass concentration due to self-shading effects.</p>
<p>To overcome this, the influence of light supply was additionally investigated using a continuous, turbidostat process mode, with constant biomass concentration at 1 g L<sup>&#x02212;1</sup>, which was ensured by regulating the dilution rate.</p>
<p>Unlike in the batch experiments, the turbidostat cultures of <italic>A. platensis</italic> showed no significant influence of light on the EPS concentration (average <italic>c</italic><sub><italic>EPS</italic></sub> &#x0003D; 0.056 g L<sup>&#x02212;1</sup> &#x000B1; 0.0036) and EPS yield (average <italic>Y</italic><sub><italic>EPS</italic>/<italic>X</italic></sub> &#x0003D; 0.059 g g<sup>&#x02212;1</sup> &#x000B1; 0.0041) (<xref ref-type="fig" rid="F4">Figure 4A</xref>). Compared to the batch experiments, this results in a decrease in EPS concentration and yield of more than 50%. For light intensities at &#x0007E;450 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup>, the EPS concentration and yield in the continuous process is about twice as high as in batch cultures. At this light intensity, the space-time yield in the turbidostat experiments reached the highest value of 0.080 g L<sup>&#x02212;1</sup> d<sup>&#x02212;1</sup>, which is significantly higher than the space-time yield achieved in batch cultivations at comparable light intensities.</p>
<fig id="F4" position="float">
<label>Figure 4</label>
<caption><p>Influence of light on the EPS concentration (black), EPS yield (gray), and space-time yield (white) in turbidostat processes at a biomass concentration of 1 g L<sup>&#x02212;1</sup> for <bold>(A)</bold> <italic>A. platensis</italic> cultivated at 35&#x000B0;C, and <bold>(B)</bold> <italic>C. asymmetrica</italic> cultivated at 30&#x000B0;C.</p></caption>
<graphic mimetype="image" mime-subtype="tiff" xlink:href="fsufs-06-883069-g0004.tif"/>
</fig>
<p><italic>Chlamydomonas asymmetrica</italic> similarly response to light intensities in the continuous processes (<xref ref-type="fig" rid="F4">Figure 4B</xref>) as observed in the batch cultivations. Accordingly, EPS concentration, yield, and space-time yield increase with stronger irradiation. At 1,429 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup>, the EPS concentration (<italic>c</italic><sub><italic>EPS</italic></sub> &#x0003D; 0.056 g L<sup>&#x02212;1</sup>) is only one-third, and the yield (<italic>Y</italic><sub><italic>EPS</italic>/<italic>X</italic></sub> &#x0003D; 0.52 g g<sup>&#x02212;1</sup>) is half of the respective values in the batch culture. However, the space-time yield in both cultivation systems is comparable to each other and takes values of 0.84 g L<sup>&#x02212;1</sup> (conti) and 0.88 g L<sup>&#x02212;1</sup> (batch), respectively.</p></sec></sec>
<sec sec-type="discussion" id="s4">
<title>Discussion</title>
<p>The effects of light and temperature on EPS production were evaluated in two different phototrophic organisms, the cyanobacterium <italic>A. platensis</italic>, and the green alga <italic>C. asymmetrica</italic>. Both process parameters influenced the amount of produced EPS and differ for both organisms. To estimate the comparability of different parameter settings regarding EPS production, we fitted the results of the growth behavior with the growth model of Jung et al. (<xref ref-type="bibr" rid="B22">2021</xref>). The significant fit of the model to the experimental data, using the same kinetic parameters (<inline-formula><mml:math id="M12"><mml:msub><mml:mrow><mml:mi>K</mml:mi></mml:mrow><mml:mrow><mml:mi>S</mml:mi></mml:mrow></mml:msub></mml:math></inline-formula>, &#x003BC;<sub>max</sub>) for all temperature and light intensity variations, indicates a low bias to other influencing factors. When evaluating all experiments by comparing the experimental biomass development of the cultures with the growth model, a significance level of <italic>P</italic> &#x0003C; 0.005 is estimated for the experiments with <italic>A. platensis</italic> and <italic>C. asymmetrica</italic>, by using the Chi-square test (&#x003C7;<sup>2</sup> &#x0003D; 1.2, <italic>n</italic> &#x0003D; 63) The residuals between the model and the experimental data are independent and well-distributed. Regarding the growth behavior of <italic>A. platensis</italic>, in this study the evaluated growth parameter <italic>K</italic><sub><italic>S</italic></sub> <italic>(61,2</italic> &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup>) is similar to those published by Levert and Xia (<xref ref-type="bibr" rid="B28">2001</xref>) and Cornet and Dussap (<xref ref-type="bibr" rid="B6">2009</xref>) with around 80 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup>. Using a <italic>K</italic><sub><italic>S</italic></sub> value of 80 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup> for fitting our data (&#x003BC;<sub>max</sub> remain unchanged) leads to insignificant changes of the quality of the fit. For example, it was observed that an increase of the quality of the fit by 5 percent points (average relative error) for the culture 975 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup> and 35&#x000B0;C. Fitting the model to the experimental data for culture growth at 25&#x000B0;C and 277 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup> lead to a 3 percent point decrease of the average relative error. The maximum growth rate at 35&#x000B0;C is estimated by the model to &#x003BC;<sub>max</sub> = 2.12 d<sup>&#x02212;1</sup>, which is in agreement with the values given from Huang and Chen, who reported global growth rate of &#x003BC;<sub>max</sub> &#x0003D; 2.0 d<sup>&#x02212;1</sup> (Huang and Chen, <xref ref-type="bibr" rid="B20">1986</xref>), and the growth rate published by Lee et al. with &#x003BC;<sub>max</sub> &#x0003D; 2.06 d<sup>&#x02212;1</sup> (Lee et al., <xref ref-type="bibr" rid="B26">1987</xref>). The standard textbook for <italic>A. platensis</italic> cultivations from Vonshak states the optimum growth temperature window between 35 and 38&#x000B0;C (Vonshak, <xref ref-type="bibr" rid="B51">1997</xref>), which is congruent to the data of current study. In the current study, the growth reduced by 42% comparing the highest and the lowest growth rate, the same reduction in growth by temperature is reported by De Oliveira et al. (<xref ref-type="bibr" rid="B9">1999</xref>), investigating a temperature range (20&#x02013;35&#x000B0;C).</p>
<p>In the case of <italic>C. asymmetrica</italic>, such a comparison with literature data is strongly biased, as the only published growth parameters regarding this green alga originates from the authors of this study. However, regarding an evaluated culture growth of &#x003BC;&#x02248;2.5 d<sup>&#x02212;1</sup> at optimum conditions, a light-dependent growth being describable by Monod kinetics with an optimal growth temperature of 30&#x000B0;C is unexceptional and lies within an expectancy range (Lee et al., <xref ref-type="bibr" rid="B25">2015</xref>). Thus, the goodness-of-fit of the model and the comparability of the current findings and growth data to published data leads to the conclusion that the growth behaviors and culture developments observed in these experiments are plausible.</p>
<p>Regarding the EPS production of both investigated microalgae, it should be stated that <italic>C. asymmetrica</italic> achieves 10-fold higher EPS concentrations than <italic>A. platensis</italic> (up to <italic>c</italic><sub><italic>EPS</italic></sub> &#x0003D; 1.4 g L<sup>&#x02212;1</sup>), yields (up to <italic>Y</italic><sub><italic>EPS</italic>/<italic>X</italic></sub> &#x0003D; 1.12 g g<sup>&#x02212;1</sup>) and space-time yields (up to <italic>STY</italic><sub><italic>EPS</italic></sub> &#x0003D; 0.84 g L<sup>&#x02212;1</sup> d<sup>&#x02212;1</sup>). These high values for EPS production are similar to those described for <italic>Phorphyridium sp</italic>. with concentrations <italic>c</italic><sub><italic>EPS</italic></sub>&#x0003E; 1 g L<sup>&#x02212;1</sup> (Singh et al., <xref ref-type="bibr" rid="B46">2000</xref>) but are even surpassed by the EPS production of <italic>Botryococcus braunii</italic>, which is reported with <italic>c</italic><sub><italic>EPS</italic></sub> &#x0003D; 4.5 g L<sup>&#x02212;1</sup> (Lupi et al., <xref ref-type="bibr" rid="B31">1991</xref>). Comparing EPS data with literature can be error-prone, as the culture conditions or age at harvesting are often not clearly stated. The measurable carbohydrates in the supernatant increase with cell breakage, especially noticeable with prolonged retention in the stationary phase. Margo et al. reported for <italic>A. platensis</italic> a 2-fold rise in EPS concentration compared to early stationary phase (<italic>c</italic><sub><italic>EPS</italic></sub> &#x0003D; 0.055 g L<sup>&#x02212;1</sup> and death phase (<italic>c</italic><sub><italic>EPS</italic></sub> &#x0003D; 0.108 g L<sup>&#x02212;1</sup>) (Magro et al., <xref ref-type="bibr" rid="B32">2018</xref>). The data from the early phase, as well as the EPS concentrations published by Strieth et al. (Strieth et al., <xref ref-type="bibr" rid="B48">2020</xref>), are a similar range as the concentrations in current experiments (0.012&#x02013;0.138 g L<sup>&#x02212;1</sup>) reported here.</p>
<p>Although the effect of temperature on EPS production is known to be inconsistent between different organisms (Delattre et al., <xref ref-type="bibr" rid="B11">2016</xref>), in current experiments, increasing temperature had a positive influence on EPS production by <italic>A. platensis</italic> and <italic>C. asymmetrica</italic>. In a study about exopolysaccharides from cyanobacteria, Nicolaus et al. (<xref ref-type="bibr" rid="B35">1999</xref>) described for <italic>A. platensis</italic> that in the absence of NaCl the EPS production slightly decreased with increasing temperatures, which is contradictory to the current findings and those of Trabelsi et al. (<xref ref-type="bibr" rid="B49">2009</xref>) and Lee et al. (<xref ref-type="bibr" rid="B27">2012</xref>). This may lead to the conclusion that the absence of NaCl was the primary influencing factor. Trabelsi et al. and Lee et al. investigated the influence of light and temperature on EPS production. Both publications show increasing EPS release at higher cultivation temperatures. The highest concentration reported by Trabelsi et al. is <italic>c</italic><sub><italic>EPS</italic></sub> &#x0003D; 0.297 g L<sup>&#x02212;1</sup> at 35 &#x000B0;C and 180 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup>, whereas Lee et. al reached <italic>c</italic><sub><italic>EPS</italic></sub> &#x0003D; 0.141 g L<sup>&#x02212;1</sup> at 38&#x000B0;C and 36 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup> (Trabelsi et al., <xref ref-type="bibr" rid="B49">2009</xref>; Lee et al., <xref ref-type="bibr" rid="B27">2012</xref>). Both findings are comparable to the current study of EPS concentrations of <italic>c</italic><sub><italic>EPS</italic></sub> &#x0003D; 0.138 g L<sup>&#x02212;1</sup> at 35&#x000B0;C and 180 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup>. The differences in the total amount of EPS may originate in the different harvesting times. Our experimental setup was designed to harvest at the early stationary phase, not to be biased by the release of IPS due to cell lysis. In contrast, the previous report used data form the late stationary phase. The comparison between growth and EPS concentration published by Trabelsi et al. perfectly shows the accelerated increase of EPS concentration after reaching the stationary phase, where biomass starts declining (Trabelsi et al., <xref ref-type="bibr" rid="B49">2009</xref>). Studies on the temperature dependency of the cyanobacterium <italic>Cyanobacterium aponinum</italic> showed that the highest EPS productivity was at 35&#x000B0;C (<italic>STY</italic><sub><italic>EPS</italic></sub>&#x0007E;9 mg L<sup>&#x02212;1</sup> d<sup>&#x02212;1</sup>), whereas the highest growth rate was at 40&#x000B0;C. Although, the productivity of <italic>A. platensis</italic> is about twice as high (<italic>STY</italic><sub><italic>EPS</italic></sub> &#x0003D; 24 mg L<sup>&#x02212;1</sup> d<sup>&#x02212;1</sup>) at similar culture conditions (76 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup>, 35&#x000B0;C), the observed trend of reaching the highest EPS productivity at slightly lower temperatures than the optimum growth is similar (Gris et al., <xref ref-type="bibr" rid="B18">2017</xref>).</p>
<p>In the well-researched review by Delattre et al. a general rule-of-thumb was formulated: higher light intensities lead to higher EPS release (Delattre et al., <xref ref-type="bibr" rid="B11">2016</xref>). Results of current study regarding the influence of light on EPS production by <italic>C. asymmetrica</italic> are supporting this statement. In both experimental approaches, the batch and the turbidostat processes with increase of illumination in the range of 96&#x02013;1,429 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup> enhanced EPS production in terms of concentration, yield, and space-time yield. However, the results obtained for <italic>A. platensis</italic> showed a different relationship with respect to light than previously described, Trabelsi et al. were able to show a significant increase of EPS-production with stronger illumination in the range between 50 and 180 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup>. A similar range was investigated by Lee et al. (<xref ref-type="bibr" rid="B27">2012</xref>) by observing a maximum EPS release at 180 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup> with <italic>c</italic><sub><italic>EPS</italic></sub> &#x0003D; 0.146 g L<sup>&#x02212;1</sup>. This is in accordance with the findings of Dejsungkranont et al., who proposed an optimum light intensity of 203 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup> for EPS production (Dejsungkranont et al., <xref ref-type="bibr" rid="B10">2017</xref>). Those results support our findings that the optimum light intensity is around 100&#x02013;200 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup> with maximum EPS concentrations of <italic>c</italic><sub><italic>EPS</italic></sub> &#x0003D; 0.138 g L<sup>&#x02212;1</sup> The significant decrease in EPS production by increasing irradiation in the range of 180&#x02013;975 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup> correlates with the findings of Silva et al., who reported a reduction in EPS yield from <italic>Y</italic><sub><italic>EPS</italic>/<italic>X</italic></sub> &#x0003D; 0.12 g g<sup>&#x02212;1</sup> at 200 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup> to <italic>Y</italic><sub><italic>EPS</italic>/<italic>X</italic></sub> &#x0003D; 0.054 g g<sup>&#x02212;1</sup> at 1,000 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup> (Silva et al., <xref ref-type="bibr" rid="B45">2020</xref>). In different experiments of current study, the specific EPS concentration dropped from <italic>Y</italic><sub><italic>EPS</italic>/<italic>X</italic></sub> = 0.106 g g<sup>&#x02212;1</sup> at 180 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup> to <italic>Y</italic><sub><italic>EPS</italic>/<italic>X</italic></sub> &#x0003D; 0.026 g g<sup>&#x02212;1</sup> at 975 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup>. It should be mentioned here that the highest specific EPS concentration was reached at 74 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup> with <italic>Y</italic><sub><italic>EPS</italic>/<italic>X</italic></sub> &#x0003D; 0.166 g g<sup>&#x02212;1</sup>.</p>
<p>Interestingly, the experiments in the continuous processes showed a lower light influence on EPS concentration and yield than in the results of the batch experiments, with a slight positive effect on the space-time yield, which can be explained by the higher dilution rates. Comparing the two process modes, the results of current study indicate that higher EPS concentrations can be achieved compared to continuous systems. The cultivation of <italic>A. platensis</italic> at higher light intensities (above 180 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup>), is an exception, since the continuous system performed better under these conditions. Nevertheless, this strongly resembles the Gaden type III category of processes, traditionally operated in batch mode (Gaden, <xref ref-type="bibr" rid="B14">2000</xref>).</p></sec>
<sec sec-type="conclusions" id="s5">
<title>Conclusions</title>
<p>For <italic>A. platensis</italic>, the light intensity with the highest EPS release was found to be 180 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup>. Stronger irradiations resulted in a substantial decrease in EPS production. The experiments regarding the temperature influences, conducted at a light intensity of 277 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup>, suggested an optimum for EPS production at 38&#x000B0;C. However, the best combination of process conditions was found to be 180 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup> and 35&#x000B0;C with <italic>c</italic><sub><italic>EPS</italic></sub> &#x0003D; 0.138 g L<sup>&#x02212;1</sup>. The optimum parameter combination for <italic>C. asymmetrica</italic>, according to our results, is 30&#x000B0;C and 1,429 &#x003BC;mol m<sup>&#x02212;2</sup> s<sup>&#x02212;1</sup> where an EPS concentration of <inline-formula><mml:math id="M13"><mml:msub><mml:mrow><mml:mi>c</mml:mi></mml:mrow><mml:mrow><mml:mi>E</mml:mi><mml:mi>P</mml:mi><mml:mi>S</mml:mi></mml:mrow></mml:msub><mml:mo>=</mml:mo><mml:mn>1</mml:mn><mml:mo>.</mml:mo><mml:mn>2</mml:mn><mml:mtext>&#x000A0;g&#x000A0;</mml:mtext><mml:msup><mml:mrow><mml:mtext>L</mml:mtext></mml:mrow><mml:mrow><mml:mo>-</mml:mo><mml:mn>1</mml:mn></mml:mrow></mml:msup></mml:math></inline-formula> was reached. Combining the high EPS concentrations with the fast growth, <italic>C. asymmetrica</italic> is the better production organism, reaching 30 times the space-time yield of <italic>A. platensis</italic> with <italic>STY</italic><sub><italic>EPS</italic></sub> &#x0003D; 0.86 g L<sup>&#x02212;1</sup> d<sup>&#x02212;1</sup>. Although the turbidostat process with <italic>C. asymmetrica</italic> led to the highest space-time yield in our experiments, continuous systems are generally not suitable for high production rates&#x02014;especially at low biomass concentrations.</p></sec>
<sec sec-type="data-availability" id="s6">
<title>Data Availability Statement</title>
<p>The raw data supporting the conclusions of this article will be made available by the authors, without undue reservation.</p></sec>
<sec id="s7">
<title>Author Contributions</title>
<p>S-HJ, NZ, FB, CM, and CL planned and designed the research and interpreted the results. S-HJ, NZ, and FB performed the experiments and proceeding of the raw data. S-HJ and CL wrote the manuscript. S-HJ, NZ, FB, UT, CR, CM, and CL revised the manuscript. All authors read and approved the final manuscript.</p></sec>
<sec sec-type="funding-information" id="s8">
<title>Funding</title>
<p>This work was funded by the German Federal Ministry for Education and Research (BMBF 03SF0457) and the German Federal Ministry of Food and Agriculture (FNR 22017518 and 2219NR287).</p></sec>
<sec sec-type="COI-statement" id="conf1">
<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&#x00027;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> </body>
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