Difference between revisions of "Team:TJU/Design"

 
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         <ul>  
 
         <ul>  
 
             <li class="hmain" style="margin-top:20px;">  
 
             <li class="hmain" style="margin-top:20px;">  
                     <a href="#Safety_training">Overview</a>
+
                     <a href="https://2015.igem.org/Team:TJU/Overview">Overview</a>
 
           </li>  
 
           </li>  
 
             <li class="hmain">  
 
             <li class="hmain">  
                 <a href="#Researcher Safety">Background</a>
+
                 <a href="https://2015.igem.org/Team:TJU/Background">Background</a>
 
                 <ul>  
 
                 <ul>  
 
                     <li>  
 
                     <li>  
                         <a href="#Microbial">Microbial fuel cells (MFCs)</a>  
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                         <a href="https://2015.igem.org/Team:TJU/Background#Microbial">Microbial fuel cells (MFCs)</a>  
 
                     </li>  
 
                     </li>  
 
                     <li>  
 
                     <li>  
                         <a href="#Typical">Typical exoelectrogens of MFCs</a>  
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                         <a href="https://2015.igem.org/Team:TJU/Background#Typical">Typical exoelectrogens of MFCs</a>  
 
                     </li>  
 
                     </li>  
 
                     <li>  
 
                     <li>  
                         <a href="#consortia">Microbial consortia</a>  
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                         <a href="https://2015.igem.org/Team:TJU/Background#consortia">Microbial consortia</a>  
 
                     </li>
 
                     </li>
 
                     <li>  
 
                     <li>  
                        <a href="#Intracellular">Intracellular protein degradation</a>  
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                      <a href="https://2015.igem.org/Team:TJU/Background#Intracellular">Intracellular protein degradation</a>
 
                     </li>  
 
                     </li>  
                    <li>
 
                        <a href="#Acid">Acid inducible promoter -P170</a>
 
                    </li>
 
                    <li>
 
                        <a href="#Reference1">References</a>
 
                    </li>
 
 
                 </ul>  
 
                 </ul>  
 
             </li>  
 
             </li>  
             <li class="hmain"><a href="#Safety_Control_Diagram">Design</a>  
+
             <li class="hmain"><a href="https://2015.igem.org/Team:TJU/Design">Design</a>  
            <ul>  
+
                <ul>  
                     <li>  
+
                     <li>
                        <a href="#Lactate">Lactate producing system</a>  
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                    <a href="https://2015.igem.org/Team:TJU/Design#Lactate producing system">Lactate producing system</a>  
 
                     </li>
 
                     </li>
 
                     <li>  
 
                     <li>  
                         <a href="#Flavins">Flavins producing system</a>  
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                         <a href="https://2015.igem.org/Team:TJU/Design#Flavins producing system">Flavins producing system</a>  
 
                     </li>
 
                     </li>
 
                     <li>  
 
                     <li>  
                         <a href="#Co-culture">Co-culture MFC</a>  
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                         <a href="https://2015.igem.org/Team:TJU/Design#Co-culture MFC">Co-culture MFC</a>  
 
                     </li>
 
                     </li>
 
                     <li>  
 
                     <li>  
                         <a href="#Proteolysis">Proteolysis system</a>  
+
                         <a href="https://2015.igem.org/Team:TJU/Design#References">References</a>  
                     </li>
+
                     </li>  
            </ul>
+
                </ul>  
             </li>            
+
             </li>
             <li class="hmain"><a href="#Dispersing and killing system">Results</a>  
+
             <li class="hmain"><a href="https://2015.igem.org/Team:TJU/Results">Results</a>
 +
            </li>
 +
            <li class="hmain"><a href="https://2015.igem.org/Team:TJU/Future Work">Future Work</a>  
 
                 <ul>  
 
                 <ul>  
                     <li>  
+
                     <li>
                        <a href="#Dispersing and killing system">Dispersing and killing system</a>  
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                    <a href="https://2015.igem.org/Team:TJU/Future Work#Proteolysis system">Proteolysis system</a>  
 
                     </li>
 
                     </li>
 
                     <li>  
 
                     <li>  
                         <a href="#References2">References</a>  
+
                         <a href="https://2015.igem.org/Team:TJU/Future Work#References2">References</a>  
 
                     </li>
 
                     </li>
              <li class="hmain">
+
                 </ul>             
                 <a href="#Link To Our Safety Form">Link To Our Safety Form</a>  
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             </li>  
             </li> 
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             <li> <a href="https://2015.igem.org" ></br></br></br></br><img src="https://static.igem.org/mediawiki/2015/1/1a/TJU_main.png" width="200"  border="none" /></a>  
                </ul>
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             </li>
+
             <li>  
+
            <a href="https://2015.igem.org" ></br></br></br></br><img src="https://static.igem.org/mediawiki/2015/1/1a/TJU_main.png" width="200"  border="none" /></a>  
+
 
             </li>
 
             </li>
 
         </ul>  
 
         </ul>  
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<div class="kuang" style="width:700px">
 
<div class="kuang" style="width:700px">
</br><a href="https://static.igem.org/mediawiki/2015/e/ea/Start1.png" target="_blank" ><img src= "https://static.igem.org/mediawiki/2015/e/ea/Start1.png"  width="680" alt=""/></a>
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</br><a href="https://static.igem.org/mediawiki/2015/d/d5/Background_11%27.png" target="_blank" ><img src= "http:  alt=""/></a>
 
<div id="Enlarge">           
 
<div id="Enlarge">           
<p> <b>Figure 1.</b> <span style="font-size: 14px"> The overall relationship of three kinds of bacteria in our co-culture system.</span><a href="https://static.igem.org/mediawiki/2015/e/ea/Start1.png"  target="_blank"><img src="https://static.igem.org/mediawiki/2013/9/90/Enlarge.jpg" width="20" height="20" align="right" alt="" /></a></p></div></div></br>
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<p> <b>Figure 1.</b> <span style="font-size: 14px"> The overall relationship of bacteria in our co-culture system.</span><a href="https://static.igem.org/mediawiki/2015/d/d5/Background_11%27.png"  target="_blank"><img src="https://static.igem.org/mediawiki/2013/9/90/Enlarge.jpg" width="20" height="20" align="right" alt="" /></a></p></div></div></br>
  
     <a name="Lactate" id="Lactate"></a><h3>1 Lactate producing system </h3> <hr></br>
+
     <a name="Lactate producing system" id="Lactate producing system"></a><h3>1 Lactate producing system </h3> <hr></br>
 
<p>Generally material flow, information flow, together with energy flow are key factors to regulate relations among bacterial consortium. Material flow, in particular, known as the most reliable and convenient method, is adopted in our construction. Typically the substances of the flow are often necessary nutrition for bacterial survival such as essential amino acid and carbon sources. </p></br>
 
<p>Generally material flow, information flow, together with energy flow are key factors to regulate relations among bacterial consortium. Material flow, in particular, known as the most reliable and convenient method, is adopted in our construction. Typically the substances of the flow are often necessary nutrition for bacterial survival such as essential amino acid and carbon sources. </p></br>
  
 
<div class="kuang" style="width:420px">
 
<div class="kuang" style="width:420px">
</br><a href="https://static.igem.org/mediawiki/2015/e/e6/%E7%A2%B3%E6%BA%90%EF%BC%88%E5%B8%8C%E7%93%A6%E6%B0%8F%EF%BC%89.png" target="_blank" ><img src= "https://static.igem.org/mediawiki/2015/e/e6/%E7%A2%B3%E6%BA%90%EF%BC%88%E5%B8%8C%E7%93%A6%E6%B0%8F%EF%BC%89.png"  width="400"  alt=""/></a>
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</br><a href="https://static.igem.org/mediawiki/2015/f/f2/Background_11111.png" target="_blank" ><img src= "https://static.igem.org/mediawiki/2015/f/f2/Background_11111.png"  width="400"  alt=""/></a>
 
<div id="Enlarge">           
 
<div id="Enlarge">           
<p> <b>Figure 2.</b> <span style="font-size: 14px"> The raletively narrow range of carbon source of <span style="font-style: italic">Shewanella</span>.</span><a href="https://static.igem.org/mediawiki/2015/e/e6/%E7%A2%B3%E6%BA%90%EF%BC%88%E5%B8%8C%E7%93%A6%E6%B0%8F%EF%BC%89.png"  target="_blank"><img src="https://static.igem.org/mediawiki/2013/9/90/Enlarge.jpg" width="20" height="20" align="right" alt="" /></a></p></div></div></br>
+
<p> <b>Figure 2.</b> <span style="font-size: 14px"> The raletively narrow range of carbon source of <span style="font-style: italic">Shewanella</span>.</span><a href="https://static.igem.org/mediawiki/2015/f/f2/Background_11111.png"  target="_blank"><img src="https://static.igem.org/mediawiki/2013/9/90/Enlarge.jpg" width="20" height="20" align="right" alt="" /></a></p></div></div></br>
  
 
<p><span style="font-style: italic">Shewanella oneidensis</span> can generate electricity with a relatively narrow range of carbon substrates, including lactate, acetate, formate, pyruvate and some amino acid.[1] It has been shown that <span style="font-style: italic">Shewanella oneidensis</span> MR-1 prefers the utilization of lactate as an energy-favorable carbon substrate as lactate-based biomass yield was higher than that for either acetate or pyruvate. Similarly, the lactate-based growth rate was much higher as well.[2] Thus, lactate is the most suitable carbon source and also the key mediator for the material flow in our system. </p></br>
 
<p><span style="font-style: italic">Shewanella oneidensis</span> can generate electricity with a relatively narrow range of carbon substrates, including lactate, acetate, formate, pyruvate and some amino acid.[1] It has been shown that <span style="font-style: italic">Shewanella oneidensis</span> MR-1 prefers the utilization of lactate as an energy-favorable carbon substrate as lactate-based biomass yield was higher than that for either acetate or pyruvate. Similarly, the lactate-based growth rate was much higher as well.[2] Thus, lactate is the most suitable carbon source and also the key mediator for the material flow in our system. </p></br>
  
 
<div class="kuang" style="width:670px">
 
<div class="kuang" style="width:670px">
</br><a href="https://static.igem.org/mediawiki/2015/c/c1/碳源(新体系1).png" target="_blank" ><img src= "https://static.igem.org/mediawiki/2015/c/c1/碳源(新体系1).png"  width="650"  alt=""/></a>
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</br><a href="https://static.igem.org/mediawiki/2015/6/69/Background_2222222222.png" target="_blank" ><img src= "https://static.igem.org/mediawiki/2015/6/69/Background_2222222222.png"  width="650"  alt=""/></a>
 
<div id="Enlarge">           
 
<div id="Enlarge">           
<p> <b>Figure 3.</b> <span style="font-size: 14px"> Our design of broadening the spectrum of carbon sources for MFCs based on <span style="font-style: italic">Shewanella</span>. Through it, we will presents the prospect of its expanding application range.</span><a href="https://static.igem.org/mediawiki/2015/c/c1/碳源(新体系1).png"  target="_blank"><img src="https://static.igem.org/mediawiki/2013/9/90/Enlarge.jpg" width="20" height="20" align="right" alt="" /></a></p></div></div></br>
+
<p> <b>Figure 3.</b> <span style="font-size: 14px"> Our design of broadening the spectrum of carbon sources for MFCs based on <span style="font-style: italic">Shewanella</span>. Through it, we will presents the prospect of its expanding application range.</span><a href="https://static.igem.org/mediawiki/2015/6/69/Background_2222222222.png"  target="_blank"><img src="https://static.igem.org/mediawiki/2013/9/90/Enlarge.jpg" width="20" height="20" align="right" alt="" /></a></p></div></div></br>
  
<p>In order to develop a proper mechanism for lactate supply, we use <span style="font-style: italic">Escherichia coli</span>, a well characterized bacterium, to produce lactate. Previously, researchers has developed a system that was able to produce 142.2 g/l of L-lactate with no more than 1.2 g/l of by-products accumulated by knocking out <span style="font-style: italic">ldhA</span> and <span style="font-style: italic">lldD</span> and inserting <span style="font-style: italic">L-LDH</span>.[3] Consequently, <span style="font-style: italic">E.coli</span> has many advantages as a host for production of lactic acid, including the ability to produce optically pure lactate, rapid growth under both aerobic and anaerobic conditions, and its simple nutritional requirements.[4] </p></br>
+
<p>In order to develop a proper mechanism for lactate supply, we use <span style="font-style: italic">Escherichia coli</span>, a well characterized bacterium, to produce lactate. Previously, researchers has developed a system that was able to produce 142.2 g/L of L-lactate with no more than 1.2 g/L of by-products accumulated by knocking out <span style="font-style: italic">ldhA</span> and <span style="font-style: italic">lldD</span> and inserting <span style="font-style: italic">L-LDH</span>.[3] Consequently, <span style="font-style: italic">E.coli</span> has many advantages as a host for production of lactic acid, including the ability to produce optically pure lactate, rapid growth under both aerobic and anaerobic conditions, and its simple nutritional requirements.[4] </p></br>
  
<p><span style="font-style: italic">Escherichia coli</span> grows fermentatively in glucose-containing medium under anaerobic condition with formation of a mixture of organic acids (lactate, acetate, formate and succinate) and ethanol, and lactate only takes no more than 50% of the total metabolites.[4] Since we need to provide enough material support for the growth and metabolism of <span style="font-style: italic">Shewanella</span> under anaerobic condition, we decide to enhance the yield of lactate by genetic engineering through two strategies: </p></br>
+
<p><span style="font-style: italic">Escherichia coli</span> grows fermentatively in glucose-containing medium under anaerobic condition with formation of a mixture of organic acids (lactate, acetate, formate and succinate) and ethanol, and lactate only takes no more than 50% of the total metabolites.[4] Since we need to provide enough material support for the growth and metabolism of <span style="font-style: italic">Shewanella</span> under anaerobic condition, we decided to enhance the yield of lactate by genetic engineering through two strategies: </p></br>
 
<p style="font-weight: bolder">1.1  ldh- Lactate dehydrogenase(LDHE) </p>
 
<p style="font-weight: bolder">1.1  ldh- Lactate dehydrogenase(LDHE) </p>
  
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</br><a href=" https://static.igem.org/mediawiki/2015/c/c8/Ldhe_gene.png" target="_blank" ><img src= " https://static.igem.org/mediawiki/2015/c/c8/Ldhe_gene.png"  width="450"  alt=""/></a>
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</br><a href=" https://static.igem.org/mediawiki/2015/1/12/%E5%9B%BE%E7%89%8710.png" target="_blank" ><img src= " https://static.igem.org/mediawiki/2015/1/12/%E5%9B%BE%E7%89%8710.png"  width="450"  alt=""/></a>
 
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<p> <b>Figure 4.</b> <span style="font-size: 14px"> The part we design to produce L-lactate(LB medium).</span><a href=" https://static.igem.org/mediawiki/2015/c/c8/Ldhe_gene.png"  target="_blank"><img src="https://static.igem.org/mediawiki/2013/9/90/Enlarge.jpg" width="20" height="20" align="right" alt="" /></a></p></div></div></br>
 
<p> <b>Figure 4.</b> <span style="font-size: 14px"> The part we design to produce L-lactate(LB medium).</span><a href=" https://static.igem.org/mediawiki/2015/c/c8/Ldhe_gene.png"  target="_blank"><img src="https://static.igem.org/mediawiki/2013/9/90/Enlarge.jpg" width="20" height="20" align="right" alt="" /></a></p></div></div></br>
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</br><a href="https://static.igem.org/mediawiki/2015/6/67/QQ图片20150916215609.jpg" target="_blank" ><img src= "https://static.igem.org/mediawiki/2015/6/67/QQ图片20150916215609.jpg"  width="450"  alt=""/></a>
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</br><a href="https://static.igem.org/mediawiki/parts/2/2b/LdhE-3.png" target="_blank" ><img src= "https://static.igem.org/mediawiki/parts/2/2b/LdhE-3.png"  width="450"  alt=""/></a>
 
<div id="Enlarge">           
 
<div id="Enlarge">           
 
<p> <b>Figure 5.</b> <span style="font-size: 14px"> The yield of lactate in flask-shaking fermentation condition (LB medium) </span>
 
<p> <b>Figure 5.</b> <span style="font-size: 14px"> The yield of lactate in flask-shaking fermentation condition (LB medium) </span>
<a href="https://static.igem.org/mediawiki/2015/6/67/QQ图片20150916215609.jpg"  target="_blank"><img src="https://static.igem.org/mediawiki/2013/9/90/Enlarge.jpg" width="20" height="20" align="right" alt="" /></a></p></div></div></br>
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<a href="https://static.igem.org/mediawiki/parts/2/2b/LdhE-3.png"  target="_blank"><img src="https://static.igem.org/mediawiki/2013/9/90/Enlarge.jpg" width="20" height="20" align="right" alt="" /></a></p></div></div></br>
  
<div class="kuang" style="width:470px">
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<p>In order to enhance the transformation efficiency from glucose to lactate, as well as improve the characterization of our <span style="font-style: italic">ldhE</span> part, we decided to knockout the the <span style="font-style: italic">pflB</span> and <span style="font-style: italic">poxB</span>.</p></br>
</br><a href="https://static.igem.org/mediawiki/2015/1/19/LdhE.png" target="_blank" ><img src= "https://static.igem.org/mediawiki/2015/1/19/LdhE.png"  width="450"  alt=""/></a>
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 +
<div class="kuang" style="width:370px">
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</br><a href="https://static.igem.org/mediawiki/2015/1/19/LdhE.png" target="_blank" ><img src= "https://static.igem.org/mediawiki/2015/1/19/LdhE.png"  width="350"  alt=""/></a>
 
<div id="Enlarge">           
 
<div id="Enlarge">           
<p> <b>Figure 5.</b> <span style="font-size: 14px"> XXXXXXXXXXXXXXXXXX</span>
+
<p> <b>Figure 6.</b> <span style="font-size: 14px"> Lactate metabolic pathway. The <span style="font-style: italic">pflB</span> and <span style="font-style: italic">poxB</span> knocking out and <span style="font-style: italic">ldhE</span> insertion will result in the accumulation of lactate.
 +
</span>
 
<a href="https://static.igem.org/mediawiki/2015/1/19/LdhE.png"  target="_blank"><img src=" https://static.igem.org/mediawiki/2013/9/90/Enlarge.jpg " width="20" height="20" align="right" alt="" /></a></p></div></div></br>
 
<a href="https://static.igem.org/mediawiki/2015/1/19/LdhE.png"  target="_blank"><img src=" https://static.igem.org/mediawiki/2013/9/90/Enlarge.jpg " width="20" height="20" align="right" alt="" /></a></p></div></div></br>
  
 
 
(ldhe表征的描述和结果)
 
  
  
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<p>PFL is a crucial enzyme in the glucose metabolism under anaerobic condition, which can catalyze one molecule of pyruvate to one molecule of formicate and one molecule of acetylcoenzyme A (AcCoA). According to metabolic pathway, pyruvate is consumed both in the PFL and LDH reactions. In the wild type <span style="font-style: italic">E. coli</span>, LDH reaction is not as competitive as the reaction through PFL, and therefore, knockout of the PFL related genes will contribute to redistribute the metabolic flux. When the PFL pathway is blocked, <span style="font-style: italic">E. coli</span> will conceivably alter the distribution of these products to overcome the imbalanced reducing equivalents caused by the pathway knockout. Therefore, knockout of <span style="font-style: italic">pflB</span> not only decreased the carbon flow to acetyl-CoA under anaerobic condition but also reduced the anaerobic consumption of NADH through reductive TCA. [5] </p></br>  
 
<p>PFL is a crucial enzyme in the glucose metabolism under anaerobic condition, which can catalyze one molecule of pyruvate to one molecule of formicate and one molecule of acetylcoenzyme A (AcCoA). According to metabolic pathway, pyruvate is consumed both in the PFL and LDH reactions. In the wild type <span style="font-style: italic">E. coli</span>, LDH reaction is not as competitive as the reaction through PFL, and therefore, knockout of the PFL related genes will contribute to redistribute the metabolic flux. When the PFL pathway is blocked, <span style="font-style: italic">E. coli</span> will conceivably alter the distribution of these products to overcome the imbalanced reducing equivalents caused by the pathway knockout. Therefore, knockout of <span style="font-style: italic">pflB</span> not only decreased the carbon flow to acetyl-CoA under anaerobic condition but also reduced the anaerobic consumption of NADH through reductive TCA. [5] </p></br>  
  
 +
<p>After the knockout of <span style="font-style: italic">pflB</span>, though the growth rate was slightly slowed down, the yield of lactate of engineered strain was improved greatly and showed a significant difference from the wild type MG1655. From the result, we can see our part functioned as expected.</p></br>
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<div class="kuang" style="width:470px">
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</br><a href="https://static.igem.org/mediawiki/2015/3/3e/Little_prinence.png" target="_blank" ><img src= "https://static.igem.org/mediawiki/2015/3/3e/Little_prinence.png"  width="450"  alt=""/></a>
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<p> <b>Figure 7.</b> <span style="font-size: 14px">  Comparison diagram of lactate production of three different strains.  MG1655: wild type ; MG1655Δ<span style="font-style: italic">pflB</span>: <span style="font-style: italic">pflB</span> knockout, <span style="font-style: italic">ldhE</span> blank; MG1655Δ<span style="font-style: italic">pflB</span>+<span style="font-style: italic">ldhE</span>: containing the functional <span style="font-style: italic">ldhE</span> part we design  </span>
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<a href="https://static.igem.org/mediawiki/2015/a/a6/屏幕快照_2015-09-16_下午11.16.03.png"  target="_blank"><img src="https://static.igem.org/mediawiki/2013/9/90/Enlarge.jpg" width="20" height="20" align="right" alt="" /></a></p></div></div></br>
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<p style="font-weight: bolder">1.3  Knockout strategy</p>
 
<p>For genes knockout, we adopted a effective, easy-to-use two-step system in which the cell is first transformed with a helper plasmid harboring genes encoding the λ-Red enzymes, I-SceI endonuclease, and RecA. λ-Red enzymes expressed from the helper plasmid are used to recombineer a small ‘landing pad’, a tetracycline resistance gene (<span style="font-style: italic">tetA</span>) flanked by I-SceI recognition sites and landing pad regions, into the desired location in the chromosome. After tetracycline selection for successful landing pad integrants, the cell is transformed with a donor plasmid carrying the desired insertion fragment; this fragment is excised by I-SceI and incorporated into the landing pad via recombination at the landing pad regions.[6] </p></br>  
 
<p>For genes knockout, we adopted a effective, easy-to-use two-step system in which the cell is first transformed with a helper plasmid harboring genes encoding the λ-Red enzymes, I-SceI endonuclease, and RecA. λ-Red enzymes expressed from the helper plasmid are used to recombineer a small ‘landing pad’, a tetracycline resistance gene (<span style="font-style: italic">tetA</span>) flanked by I-SceI recognition sites and landing pad regions, into the desired location in the chromosome. After tetracycline selection for successful landing pad integrants, the cell is transformed with a donor plasmid carrying the desired insertion fragment; this fragment is excised by I-SceI and incorporated into the landing pad via recombination at the landing pad regions.[6] </p></br>  
  
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</br><a href="https://static.igem.org/mediawiki/2015/4/48/Lambda_red.png" target="_blank" ><img src= "https://static.igem.org/mediawiki/2015/4/48/Lambda_red.png"  width="750"  alt=""/></a>
 
</br><a href="https://static.igem.org/mediawiki/2015/4/48/Lambda_red.png" target="_blank" ><img src= "https://static.igem.org/mediawiki/2015/4/48/Lambda_red.png"  width="750"  alt=""/></a>
 
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<div id="Enlarge">           
<p> <b>Figure 1.</b> <span style="font-size: 14px"> First step in the new two-step scar-less gene deletion using λ-Red recombineering method. Three rounds of PCR together with <span style="font-style: italic">tet</span> selection make up of our recombinant.</span>
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<p> <b>Figure 8.</b> <span style="font-size: 14px"> First step in the new two-step scar-less gene deletion using λ-Red recombineering method. Three rounds of PCR together with <span style="font-style: italic">tet</span> selection make up of our recombinant.</span>
 
<a href="https://static.igem.org/mediawiki/2015/4/48/Lambda_red.png"  target="_blank"><img src="https://static.igem.org/mediawiki/2013/9/90/Enlarge.jpg" width="20" height="20" align="right" alt="" /></a></p></div></div></br>
 
<a href="https://static.igem.org/mediawiki/2015/4/48/Lambda_red.png"  target="_blank"><img src="https://static.igem.org/mediawiki/2013/9/90/Enlarge.jpg" width="20" height="20" align="right" alt="" /></a></p></div></div></br>
 
   </br>
 
   </br>
 
      
 
      
    <h3>References</h3>
 
    <hr></br>
 
<p> <span style="font-weight: lighter ;font-size:14px;" > [1] Tang Y J, Meadows A L, Keasling J D. A kinetic model describing <span style="font-style: italic">Shewanella oneidensis</span> MR-1 growth, substrate consumption, and product secretion.[J]. Biotechnology & Bioengineering, 2007, 96(1):125–133.</br>
 
[2] Feng X, Xu Y, Chen Y, et al. Integrating Flux Balance Analysis into Kinetic Models to Decipher the Dynamic Metabolism of <span style="font-style: italic">Shewanella oneidensis</span> MR-1[J]. Plos Computational Biology, 2011, 8(2):e1002376-e1002376. </br>
 
[3] Highly efficient L-lactate production using engineered <span style="font-style: italic">Escherichia coli</span> with dissimilar temperature optima for L-lactate formation and cell growth. </br>
 
[4] Liu H, Kang J, Qi Q, et al. Production of lactate in <span style="font-style: italic">Escherichia coli</span> by redox regulation genetically and physiologically.[J]. Appl Biochem Biotechnol, 2011, 164(2):162-169. </br>
 
[5] Zhu J, Shimizu K, Zhu J, et al. Effect of a single-gene knockout on the metabolic regulation in <span style="font-style: italic">Escherichia coli</span> for D-lactate production under microaerobic condition[J]. Metabolic Engineering, 2005, 7(2):104–115. </br>
 
[6] Thomas E, Kuhlman, Edward C, Cox. Site-specific chromosomal integration of large synthetic constructs.[J]. Nucleic Acids Research, 2010, 38(38). </br>
 
[7] Lin Z, Xu Z, Li Y, et al. Metabolic engineering of <span style="font-style: italic">Escherichia coli</span> for the production of riboflavin[J]. Microbial Cell Factories, 2014, 13(1):1-12.</span></p>
 
</br>
 
  
<a name="Flavins" id="Flavins"></a><h3> 2 Flavins producing system </h3> <hr></br>
 
  
<p><span style="font-style: italic">Shewanella oneidensis</span> MR-1, a facultative anaerobe, has been widely used as a model anode biocatalyst in microbial fuel cells (MFCs) due to its easiness of cultivation, adaptability to aerobic and anaerobic environment and both respiratory and electron transfer versatility. [1] </p></br>
+
<a name="Flavins producing system" id="Flavins producing system"></a><h3> 2 Flavins producing system </h3> <hr></br>
 +
 
 +
<p><span style="font-style: italic">Shewanella oneidensis</span> MR-1, a facultative anaerobe, has been widely used as a model anode biocatalyst in microbial fuel cells (MFCs) due to its easiness of cultivation, adaptability to aerobic and anaerobic environment and both respiratory and electron transfer versatility. [8] </p></br>
 +
 
  
 
<p>Particularly, EET pathway can be subdivided into direct EET and mediated EET and the latter one limits the efficiency of electron transfer between bacteria and electrode due to the deficiency of electron mediator. To regulate relations of energy and information in the consortium, flavins hold the key to success. </p></br>
 
<p>Particularly, EET pathway can be subdivided into direct EET and mediated EET and the latter one limits the efficiency of electron transfer between bacteria and electrode due to the deficiency of electron mediator. To regulate relations of energy and information in the consortium, flavins hold the key to success. </p></br>
  
<p>It is widely accepted that interfacial EET is the rate-limiting step in the EET processes which can be relieved by some redox active molecules such as quinines and metal-centered porphyrin-ring derivatives. However, those redox active molecules are generally costly and toxic to anodic electricigens. Besides, <span style="font-style: italic">Shewanella</span> is capable of utilizing self-secreted flavins like riboflavin (RF) to accelerate EET, which is much more efficiently than other exogenous active molecules. More specifically, riboflavin (RF) and flavin mononucleotide (FMN) enhance EET more than five times, with much lower concentrations than those needed for anthraquinone-2,6-disulfonate (AQDS) shuttling. So we choose flavins as one entry point to enhance the electricity output of MFCs. [2] </p></br>
+
<p>It is widely accepted that interfacial EET is the rate-limiting step in the EET processes which can be relieved by some redox active molecules such as quinines and metal-centered porphyrin-ring derivatives. However, those redox active molecules are generally costly and toxic to anodic electricigens. Besides, <span style="font-style: italic">Shewanella</span> is capable of utilizing self-secreted flavins like riboflavin (RF) to accelerate EET, which is much more efficiently than other exogenous active molecules. More specifically, riboflavin (RF) and flavin mononucleotide (FMN) enhance EET more than five times, with much lower concentrations than those needed for anthraquinone-2,6-disulfonate (AQDS) shuttling. So we choose flavins as one entry point to enhance the electricity output of MFCs. [9] </p></br>
  
 
<div class="kuang" style="width:620px">
 
<div class="kuang" style="width:620px">
 
</br><a href=" https://static.igem.org/mediawiki/2015/6/61/EET.png" target="_blank" ><img src= " https://static.igem.org/mediawiki/2015/6/61/EET.png"  width="600"  alt=""/></a>
 
</br><a href=" https://static.igem.org/mediawiki/2015/6/61/EET.png" target="_blank" ><img src= " https://static.igem.org/mediawiki/2015/6/61/EET.png"  width="600"  alt=""/></a>
 
<div id="Enlarge">           
 
<div id="Enlarge">           
<p> <b>Figure 1.</b> <span style="font-size: 14px"> comparison of co-factor EET model(a) and diffusion EET model(b), (b) also reveals the electron pathway by endogenous flavins </span>
+
<p> <b>Figure 9.</b> <span style="font-size: 14px"> Comparison of co-factor EET model(a) and diffusion EET model(b), (b) also reveals the electron pathway by endogenous flavins </span>
 
<a href=" https://static.igem.org/mediawiki/2015/6/61/EET.png"  target="_blank"><img src="https://static.igem.org/mediawiki/2013/9/90/Enlarge.jpg" width="20" height="20" align="right" alt="" /></a></p></div></div></br>
 
<a href=" https://static.igem.org/mediawiki/2015/6/61/EET.png"  target="_blank"><img src="https://static.igem.org/mediawiki/2013/9/90/Enlarge.jpg" width="20" height="20" align="right" alt="" /></a></p></div></div></br>
  
  
<p>In EET model, outward current flows from interior of cells to outer membrane (OM) and extracellular anodes through a metal-reducing conduit (Mtr pathway), where electrons (from NADH, the intracellular electron carrier) flow through the menaquinol pool, CymA (inner membrane [IM] tetraheme c-type cytochromes [c-Cyts]), MtrA (periplasmic decaheme c-Cyts), MtrB (β-barrel trans-OM protein) and finally to MtrC and OmcA (two OM decaheme c-Cyts). However, the principle of how flavins function still remains controversial. [3] </p></br>
+
<p>In EET model, outward current flows from interior of cells to outer membrane (OM) and extracellular anodes through a metal-reducing conduit (Mtr pathway), where electrons (from NADH, the intracellular electron carrier) flow through the menaquinol pool, CymA (inner membrane [IM] tetraheme c-type cytochromes [c-Cyts]), MtrA (periplasmic decaheme c-Cyts), MtrB (β-barrel trans-OM protein) and finally to MtrC and OmcA (two OM decaheme c-Cyts). However, the principle of how flavins function still remains controversial. [10] </p></br>
  
<p>Traditional model demonstrates that flavins carry the electrons from OM c-Cyts to electrode by diffusion, which has been in debate due to thermodynamic disproof. Recently, another interfacial EET model was proposed, where flavin may serve as a cofactor binding to OmcA or MtrC to dictate EET. Fully oxidized flavin (Ox) accepts one electron from reduced heme of OM c-Cyts, and binds to OM c-Cyts as a cofactor in the semiquinone (Sq) form with shifted potential. Ox/Sq redox cycling in OM c-Cyts donates electrons to electrodes in a one electron reaction mode via direct contact.[3] So by maximizing the amount of riboflavin and FMN, we may achieve a relatively high power generation and this inspired us to construct a high-yield module in the engineered bacteria. </p></br>
+
<p>Traditional model demonstrates that flavins carry the electrons from OM c-Cyts to electrode by diffusion, which has been in debate due to thermodynamic disproof. Recently, another interfacial EET model was proposed, where flavin may serve as a co-factor binding to OmcA or MtrC to dictate EET. Fully oxidized flavin (Ox) accepts one electron from reduced heme of OM c-Cyts, and binds to OM c-Cyts as a cofactor in the semiquinone (Sq) form with shifted potential. Ox/Sq redox cycling in OM c-Cyts donates electrons to electrodes in a one electron reaction mode via direct contact.[10] </p></br>
  
<div class="kuang" style="width:320px">
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<div class="kuang" style="width:420px">
</br><a href="https://static.igem.org/mediawiki/2015/2/29/Riboflavin_metabolism.png" target="_blank" ><img src= "https://static.igem.org/mediawiki/2015/2/29/Riboflavin_metabolism.png"  width="300"  alt=""/></a>
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</br><a href="https://static.igem.org/mediawiki/2015/2/29/Riboflavin_metabolism.png" target="_blank" ><img src= "https://static.igem.org/mediawiki/2015/2/29/Riboflavin_metabolism.png"  width="400"  alt=""/></a>
 
<div id="Enlarge">           
 
<div id="Enlarge">           
<p> <b>Figure 1.</b> <span style="font-size: 14px"> Pathway for engineered riboflavin and FMN production. We designed a strong RBS sequence in the path to FMN formation via riboflavin. In this way, we can generate a high yield both for riboflavin and FMN.</span>
+
<p> <b>Figure 10.</b> <span style="font-size: 14px"> Pathway for engineered riboflavin and FMN production <span style="font-style: italic">E. coli</span>. </span>
 
<a href=" https://static.igem.org/mediawiki/2015/2/29/Riboflavin_metabolism.png "  target="_blank"><img src=" https://static.igem.org/mediawiki/2013/9/90/Enlarge.jpg " width="20" height="20" align="right" alt="" /></a></p></div></div></br>
 
<a href=" https://static.igem.org/mediawiki/2015/2/29/Riboflavin_metabolism.png "  target="_blank"><img src=" https://static.igem.org/mediawiki/2013/9/90/Enlarge.jpg " width="20" height="20" align="right" alt="" /></a></p></div></div></br>
  
  
  
<p>Although <span style="font-style: italic">Shewanella</span> uses endogenous flavins to mediate electrons, the amount of its production is deficient and multi-tasks brought by self-engineering may also reduce the transfer efficiency. As a consequence, we introduce a series of genes for flavin production into <span style="font-style: italic">E.coli</span>. </p></br>
+
<p>Although <span style="font-style: italic">Shewanella</span> uses endogenous flavins to mediate electrons, the amount of its production is deficient and multi-tasks brought by self-engineering may also reduce the transfer efficiency. As a consequence, we had two strategies to construct the zymophyte and further improve the production. Firstly, we introduced flavin producing genes using the <span style="font-style: italic">E.coli</span> as chassis. Secondly, we get an engineered <span style="font-style: italic">B.subtilis</span> strain from the lab of Dr. Tao Chen [11](more detail in attribution) </p></br>
  
<p>The metabolic flux (figure 2) reveals the relevant pathways of riboflavin production and engineering strategies for riboflavin production. We adopted a strain with <span style="font-style: italic">pgi</span>, <span style="font-style: italic">edd</span> and <span style="font-style: italic">eda</span> deletion as well as a high-yield gene construction (<span style="font-style: italic">ribABDEC</span> with a weak RBS in <span style="font-style: italic">ribC</span> pathway) from previous research. (Tao, et al) Consequently, the result shows an accumulation for riboflavin(229.1mg/L), yet a relatively small amount for FMN. </p></br>
+
<p>Based on the EET pathway theory, we suggest that by maximizing the amount of flavins, we may significantly enhance the EET efficiency and achieve a relatively high power generation.</p></br>
  
<p>However, based on co-factor model, EET pathway points out that FMN plays a critical role in electron transfer as the same as riboflavin by combining with the OmcA protein which is an essential and indispensible part for power generation. Based on this viewpoint, we also construct <span style="font-style: italic">ribA</span>, <span style="font-style: italic">ribB</span>, <span style="font-style: italic">ribD</span>, <span style="font-style: italic">ribE</span>, and <span style="font-style: italic">ribC</span> into our engineered bacteria and more importantly, design a strong RBS sequence upstream of the <span style="font-style: italic">ribC</span>. The strong RBS before <span style="font-style: italic">ribC</span> sequence can lead to the FMN accumulation while riboflavin consumes a bit, which may in turn, result in increase both for riboflavin and FMN as a whole. Ultimately, our result shows a impressive amount of flavins that reaches xxx and power generation arrives at xxx. </p></br>
+
<p>We found a part BBa_K1172303 in Part Registry constructed by 2013 Team Bielefeld-Germany which was also aimed at producing riboflavins. However, the gene cluster showed a maximum output of 6 mg/L even with a strong promoter, which was insufficient to maintain a high and constant efficiency of EET pathway in our co-culture system. So we decided to optimize the part BBa_K1172303 to enhance the production of riboflavins. </p></br>
(核黄素表征描述和结果)
+
<h3>References</h3>
+
    <hr></br>
+
<p> <span style="font-weight: lighter ;font-size:14px;" > [1] Wang X, Tao L, Wang H, et al. Improving mediated electron transport in anodic bioelectrocatalysis[J]. Chemical Communications, 2015. </br>
+
[2] Okamoto A, Nakamura R, Nealson K H, et al. Bound Flavin Model Suggests Similar Electron‐Transfer Mechanisms in <span style="font-style: italic">Shewanella</span> and <span style="font-style: italic">Geobacter</span>[J]. Chemelectrochem, 2014, 1(11):1808-1812. </br>
+
[3] Yang Y, Ding Y, Hu Y, et al. Enhancing Bidirectional Electron Transfer of <span style="font-style: italic">Shewanella oneidensis</span> by a Synthetic Flavin Pathway[J]. Acs Synthetic Biology, 2015. </br>
+
[4] Lin Z, Xu Z, Li Y, et al. Metabolic engineering of <span style="font-style: italic">Escherichia coli</span> for the production of riboflavin[J]. Microbial Cell Factories, 2014, 13(1):1-12.</span></p></br>
+
  
<a name="Co-culture" id="Co-culture"></a><h3> 3 Co-culture MFC </h3> <hr></br>
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<div class="kuang" style="width:770px">
<p>Microorganisms rarely live in isolated niches. One reason is that the maintenance of viability of these microbes may need supplementary metabolites or other signaling chemicals provided by other microbes in the ecosystems and communities.[1] Conforming to the trend of revolution, we apply the bacterial consortium in our MFC for greater power generation and increased duration. </p></br>
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</br><a href="https://static.igem.org/mediawiki/2015/7/73/EC10_GENE改.png" target="_blank" ><img src= "https://static.igem.org/mediawiki/2015/7/73/EC10_GENE改.png"  width="750"  alt=""/></a>
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<div id="Enlarge">        
 +
<p> <b>Figure 11.</b> <span style="font-size: 14px"> Two different parts we designed to produce flavins.  </span>
 +
<a href="https://static.igem.org/mediawiki/2015/7/73/EC10_GENE改.png"  target="_blank"><img src="https://static.igem.org/mediawiki/2013/9/90/Enlarge.jpg" width="20" height="20" align="right" alt="" /></a></p></div></div></br>
  
<p>Apart from the universal trend of nature, the mixed culture shares some unique advantages particularly in our MFC. For example, <span style="font-style: italic">Shewanella</span> originally can merely use few simple carbon substrates like lactate, acetate, formate, pyruvate and some amino acid.[2] However, our consortium as a whole can expand the absorption range of carbon resources and develop a more complex diagram of carbon input for <span style="font-style: italic">Shewanella</span>. Also, our intention is able to achieve comprehensive functions through “Labor Division” that monoculture can hardly manage. For instance, if we use only <span style="font-style: italic">Shewanella</span> to supply electricity, the production of flavins as well as other related reaction will inhibit current creation. These are fundamental reasons that we adopt the “mix” strategy in our project.</p></br>
+
<p>As we learn from metabolic flux (figure 2), it reveals the relevant pathways of riboflavin production and engineering strategies for riboflavin production. In their previous research(Tao, et al) [7] ,they construct a high-yield <span style="font-style: italic">E.coli</span> strain with a yield of 229.1 mg/L. Based on their study, we constructed a flavin producing part (<span style="font-style: italic">ribABDEC</span> cluster) named EC10.(as shown in figure 11a). The part(<a href="http://parts.igem.org/Part:BBa_K1696011">BBa_K1696011</a>) we designed, compared with BBa_K117230, has been well optimized and the yield of that reached 17 mg/L.( as shown in figure 13). We can see from the results, the functionality of their parts has successfully improved. </p></br>
<p style="font-weight: bolder">3.1 First Trial</p>
+
<p>Our experiment started with monoculture of <span style="font-style: italic">Shewanella</span>, in which we have found several important conclusions that might be used in the later trials: </br>
+
(i) <span style="font-style: italic">Shewanella</span> alone cannot take good use of glucose as the mere carbon source to generate power. </br>
+
(ii) Voltage has been improved when we add flavins to the monoculture medium, which proved that flavins indeed would help the power enhance. </br>
+
(iii) As an attempt to choose a proper substance being used in the experiment, we put sodium lactate into service and found that <span style="font-style: italic">Shewanella</span> could achieve power output. </p></p></br>
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<div class="kuang" style="width:470px">
 
<div class="kuang" style="width:470px">
</br><a href="https://static.igem.org/mediawiki/2015/1/1b/TJU-design-2.png" target="_blank" ><img src= "https://static.igem.org/mediawiki/2015/1/1b/TJU-design-2.png"  width="450"  alt=""/></a>
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</br><a href="https://static.igem.org/mediawiki/parts/c/c2/Ribo-3.jpg" target="_blank" ><img src= "https://static.igem.org/mediawiki/parts/c/c2/Ribo-3.jpg"  width="450"  alt=""/></a>
 
<div id="Enlarge">           
 
<div id="Enlarge">           
<p> <b>Figure 1.</b> <span style="font-size: 14px"> XXXXXXXXXXXXXXXXXX</span>
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<p> <b>Figure 12.</b> <span style="font-size: 14px"> The production of EC10 in tubes.</span>
<a href="https://static.igem.org/mediawiki/2015/1/1b/TJU-design-2.png"  target="_blank"><img src=" https://static.igem.org/mediawiki/2013/9/90/Enlarge.jpg " width="20" height="20" align="right" alt="" /></a></p></div></div></br>
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<a href="https://static.igem.org/mediawiki/parts/c/c2/Ribo-3.jpg"  target="_blank"><img src=" https://static.igem.org/mediawiki/2013/9/90/Enlarge.jpg " width="20" height="20" align="right" alt="" /></a></p></div></div></br>
  
<p style="font-weight: bolder">3.2 Second Trial: </p>
 
<p>Since we’ve constructed the lactate producing strain (ldhE), the flavin producing strain (EC10) and an engineered strain bearing both ldhE and EC10, we initiated our co-culture experiment with different labor division. </p></br>
 
  
<div class="kuang" style="width:470px">
+
<p>In the meanwhile, based on co-factor model, EET pathway points out that FMN plays a critical role in electron transfer. Through the study by Dr. Tao Chen, they have weakened the RBS upstream of <span style="font-style: italic">ribC</span> to divert more of the material flux to RF production.[7] Based on their viewpoint, we got further to design a strong RBS sequence upstream of the <span style="font-style: italic">ribC</span> and we rename the new part as EC10*(<a href="http://parts.igem.org/Part:BBa_K1696010">BBa_K1696010</a>). The yield of EC10* reached 90 mg/L(as shown in figure 11b).  The strong RBS before <span style="font-style: italic">ribC</span> sequence can lead to the FMN accumulation while riboflavin consumes a bit, which may in turn, result in increasing both for riboflavin and FMN as a whole. </p></br>
</br><a href="https://static.igem.org/mediawiki/2015/3/3a/TJU-design-3.png" target="_blank" ><img src= "https://static.igem.org/mediawiki/2015/3/3a/TJU-design-3.png"  width="450"  alt=""/></a>
+
 
 +
<div class="kuang" style="width:590px">
 +
</br><a href="https://static.igem.org/mediawiki/2015/2/25/Ribo-4.png" target="_blank" ><img src= "https://static.igem.org/mediawiki/2015/2/25/Ribo-4.png"  width="570"  alt=""/></a>
 
<div id="Enlarge">           
 
<div id="Enlarge">           
<p> <b>Figure 1.</b> <span style="font-size: 14px"> XXXXXXXXXXXXXXXXXX</span>
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<p> <b>Figure 13.</b> <span style="font-size: 14px"> The yield of riboflavin in different strains :EC10, Rf02S (Δ<span style="font-style: italic">pgi</span>+EC10), EC10* </span>
<a href="https://static.igem.org/mediawiki/2015/3/3a/TJU-design-3.png" target="_blank"><img src=" https://static.igem.org/mediawiki/2013/9/90/Enlarge.jpg " width="20" height="20" align="right" alt="" /></a></p></div></div></br>
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<a href="https://static.igem.org/mediawiki/2015/2/25/Ribo-4.png  target="_blank"><img src=" https://static.igem.org/mediawiki/2013/9/90/Enlarge.jpg " width="20" height="20" align="right" alt="" /></a></p></div></div></br>
  
<p>From the figure above, we found that the co-culture system with three different strains has a higher electricity output than two-strain system before 20h, showing that a more complete labor division may have a better effect in the co-culture system. It is because that we can more accurately control the amount and ratio of lactate and flavins when they are produced in separated strains. </p></br>
+
<p>When we characterized our part, we were not able to detect the FMN for lacking proper equipments. However, we were surprised to find that the production of EC10* was even better with a larger output of riboflavins. For riboflavin measurements, culture samples were diluted with 0.05 M NaOH to the linear range of the spectrophotometer and the A444 was immediately measured, according to the Dr. Tao Chen’s method [7]. As for the reason of production improvement of RF, we speculate that the strengthening of <span style="font-style: italic">ribC</span> gene can improve both the RF and FMN yield through the flavin metabolic pathway. </p></br>
(2 ph试纸图)
+
<p>However, the electricity output dropped promptly after 30h. (as shown in figure 1). In the meanwhile, we took samples from anode finding that pH in anode was excessively low (lower than 6.2) which might not meet the survival requirement of <span style="font-style: italic">Shewanella</span>. </p></br>
+
  
<p>The reason of the acidity, based on our analysis, could be the overmuch glucose or the high ratio of fermentation bacteria in the system. Particularly, our medium consist of 10 g/L glucose as well as 5% LB and 95% M9 medium. Both of the possibilities above can lead to the overproduction of lactate and other acid metabolites like formic acid which are hard to consume. </p></br>
 
  
<p>So, in order to solve the pH problem, we have two strategies. Firstly, we can optimize the medium component by reducing ratio of C and N. Secondly, we would optimize the proportion of the fermentation bacteria. </p></br>
+
<a name="Co-culture MFC" id="Co-culture MFC"></a><h3> 3 Co-culture MFC -- <span style="font-style: normal; color:#ddbf73;">Division Of Labor</span> </h3> <hr></br>
 +
<p>Microorganisms rarely live in isolated niches. One reason is that the maintenance of viability of these microbes may need supplementary metabolites or other signaling chemicals provided by other microbes in the ecosystems and communities.[11] Conforming to the trend of revolution, we apply the bacterial consortium in our MFC for greater power generation and increased duration. </p></br>
  
<p>Apart from that, we also found that excessive portion of zymophyte would inhibit biofilm formation of <span style="font-style: italic">Shewanella</span> by zymophyte taking up the spaces in electrode. </p></br>
+
<p>Apart from the universal trend of nature, the mixed culture shares some unique advantages particularly in our MFC. For example, <span style="font-style: italic">Shewanella</span> originally can merely use few simple carbon substrates like lactate, acetate, formate, pyruvate and some amino acid.[1] However, our consortium as a whole can expand the absorption range of carbon resources and develop a more complex diagram of carbon input for <span style="font-style: italic">Shewanella</span>. Also, our intention is able to achieve comprehensive functions through <span style="font-style: normal;font-weight: bold; color:#ddbf73;">“Division Of Labor”</span> that monoculture can hardly manage. For instance, if we use only <span style="font-style: italic">Shewanella</span> to supply electricity, the production of flavins as well as other related reaction will inhibit current creation. These are fundamental reasons that we adopt the “mix” strategy in our project.</p></br>
 +
<p style="font-weight: bolder">3.1 First Trial</p>
 +
<p>Our experiment started with monoculture of <span style="font-style: italic">Shewanella</span>, in which we have found several important conclusions that might be used in the later trials: </br>
 +
(i) <span style="font-style: italic">Shewanella</span> alone cannot take good use of glucose as the mere carbon source to generate power. </br>
 +
(ii) Voltage has been improved when we add flavins to the monoculture medium, which proved that flavins indeed would help the power enhance. </br>
 +
(iii) As an attempt to choose a proper substance being used in the experiment, we put sodium lactate into service and found that <span style="font-style: italic">Shewanella</span> could achieve power output. </p></p></br>
  
<p style="font-weight: bolder">3.3 Third trial</p>
+
<div class="kuang" style="width:770px">
<p>When we have preliminarily optimized the bacterial proportion and medium compositions, we got a significant improvement of the electricity output in spite of the relatively short sustaining time.(shown as follows) </p></br>
+
</br><a href="https://static.igem.org/mediawiki/2015/c/c1/Result_5'.png" target="_blank" ><img src= "https://static.igem.org/mediawiki/2015/c/c1/Result_5'.png"  width="750"  alt=""/></a>
 
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<div class="kuang" style="width:470px">
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</br><a href="https://static.igem.org/mediawiki/2015/0/04/TJU-design-4.png" target="_blank" ><img src= "https://static.igem.org/mediawiki/2015/0/04/TJU-design-4.png"  width="450"  alt=""/></a>
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<div id="Enlarge">           
 
<div id="Enlarge">           
<p> <b>Figure 1.</b> <span style="font-size: 14px"> XXXXXXXXXXXXXXXXXX</span>
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<p> <b>Figure 14.</b> <span style="font-size: 14px"> The electrical output of MFCs of single strain <span style="font-style: italic">Shewanella oneidensis</span> MR-1 with different substrates</span>
<a href="https://static.igem.org/mediawiki/2015/0/04/TJU-design-4.png"  target="_blank"><img src=" https://static.igem.org/mediawiki/2013/9/90/Enlarge.jpg " width="20" height="20" align="right" alt="" /></a></p></div></div></br>
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<a href="https://static.igem.org/mediawiki/2015/c/c1/Result_5'.png"  target="_blank"><img src=" https://static.igem.org/mediawiki/2013/9/90/Enlarge.jpg " width="20" height="20" align="right" alt="" /></a></p></div></div></br>
  
 +
<p style="font-weight: bolder">3.2 Second Trial: </p>
 +
<p>Since we’ve constructed the lactate producing strain (ldhE), the flavin producing strain (EC10) and an engineered strain bearing both ldhE and EC10, we initiated our co-culture experiment with different division of labor. </p></br>
  
<p>We also attempted to put the fermentation bacteria into the system some time after <span style="font-style: italic">Shewanella</span>. However, the later joining of fermentation bacteria will the stability of the system so that the output oscillated for a period of time. We can see from the figure**, even though the lasting time was longer than before, the maximum electricity output was still limited. </p></br>
+
<div class="kuang" style="width:770px">
 
+
</br><a href="https://static.igem.org/mediawiki/2015/f/f9/Result_6.png" target="_blank" ><img src= "https://static.igem.org/mediawiki/2015/f/f9/Result_6.png"  width="750"  alt=""/></a>
<div class="kuang" style="width:470px">
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</br><a href="https://static.igem.org/mediawiki/2015/1/15/TJU-design-5.png" target="_blank" ><img src= "https://static.igem.org/mediawiki/2015/1/15/TJU-design-5.png"  width="450"  alt=""/></a>
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<div id="Enlarge">           
 
<div id="Enlarge">           
<p> <b>Figure 1.</b> <span style="font-size: 14px"> XXXXXXXXXXXXXXXXXX</span>
+
<p> <b>Figure 15.</b> <span style="font-size: 14px"> The electrical output of co-culture MFCs with preliminary division of labor</span>
<a href="https://static.igem.org/mediawiki/2015/1/15/TJU-design-5.png"  target="_blank"><img src=" https://static.igem.org/mediawiki/2013/9/90/Enlarge.jpg " width="20" height="20" align="right" alt="" /></a></p></div></div></br>
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<a href="https://static.igem.org/mediawiki/2015/f/f9/Result_6.png"  target="_blank"><img src=" https://static.igem.org/mediawiki/2013/9/90/Enlarge.jpg " width="20" height="20" align="right" alt="" /></a></p></div></div></br>
  
  
<p>Subsequently, we arranged variable mixture for three-strain system to determine the best proportion for electricity generation. Besides, we continued to optimize the culture condition (95%M9, 5%LB and glucose 2g/L), we can see from the figure that the three-strain system had a maximum output at around 350mV and had a significant advantage over the two-strain system. Additionally, the lasting time was over 80h without any supplementary glucose, which indicated the high utilization rate of carbon source and the relatively stable relationship among the three strains. </p></br> 
 
  
 
<div class="kuang" style="width:470px">
 
<div class="kuang" style="width:470px">
</br><a href="https://static.igem.org/mediawiki/2015/f/f1/TJU-design-6.png" target="_blank" ><img src= "https://static.igem.org/mediawiki/2015/f/f1/TJU-design-6.png"  width="450"  alt=""/></a>
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</br><a href="https://static.igem.org/mediawiki/2015/3/39/Shizhi.jpg" target="_blank" ><img src= "https://static.igem.org/mediawiki/2015/3/39/Shizhi.jpg"  width="450"  alt=""/></a>
 
<div id="Enlarge">           
 
<div id="Enlarge">           
<p> <b>Figure 1.</b> <span style="font-size: 14px"> XXXXXXXXXXXXXXXXXX</span>
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<p> <b>Figure 16.</b> <span style="font-size: 14px">  
<a href="https://static.igem.org/mediawiki/2015/f/f1/TJU-design-6.png"  target="_blank"><img src=" https://static.igem.org/mediawiki/2013/9/90/Enlarge.jpg " width="20" height="20" align="right" alt="" /></a></p></div></div></br>
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pH test of anode samples, with only sample 1 get reached above 6.5 </span>
 +
<a href="https://static.igem.org/mediawiki/2015/3/39/Shizhi.jpg"  target="_blank"><img src=" https://static.igem.org/mediawiki/2013/9/90/Enlarge.jpg " width="20" height="20" align="right" alt="" /></a></p></div></div></br>
  
  
  
<p style="font-weight: bolder">3.4 Fourth trial</p>
+
<p style="font-weight: bolder">3.3 Third trial</p>
<p>We innovatively introduced a third species, <span style="font-style: italic">Bacillus subtilis</span>, into our system. Considering <span style="font-style: italic">Bacillus subtilis</span> take KNO3 as the substrates instead of glucose in anaerobic condition, we could reduce the competition for carbon sources between two kinds of fermentation bacteria. Also it has been reported that engineered <span style="font-style: italic">B.subtilis</span> could get a high output of flavins which is exactly what we want. So, we choosed <span style="font-style: italic">Bacillus subtilis</span> as another kind of fermentation bacteria.  </p></br>
+
<p>When we have preliminarily optimized the bacterial proportion and medium compositions, we got a significant improvement of the electricity output in spite of the relatively short sustaining time.(shown as follows) </p></br>
 
+
<p>It can been seen from the figure**, the electricity output of three-strain co-culture system with <span style="font-style: italic">B.subtilis</span> could reach more than 500mV enduring around 80h, showing a great difference from the <span style="font-style: italic">Shewanella</span> single-strain system. Compared with two-strain system below, the three-strain system with <span style="font-style: italic">B.subtilis</span> also showed a visible advantage. </p></br>
+
  
<div class="kuang" style="width:470px">
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<div class="kuang" style="width:770px">
</br><a href="https://static.igem.org/mediawiki/2015/8/85/TJU-design-7.png" target="_blank" ><img src= "https://static.igem.org/mediawiki/2015/8/85/TJU-design-7.png"  width="450"  alt=""/></a>
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</br><a href="https://static.igem.org/mediawiki/2015/0/01/Result_00.png" target="_blank" ><img src= "https://static.igem.org/mediawiki/2015/0/01/Result_00.png"  width="750"  alt=""/></a>
 
<div id="Enlarge">           
 
<div id="Enlarge">           
<p> <b>Figure 1.</b> <span style="font-size: 14px"> XXXXXXXXXXXXXXXXXX</span>
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<p> <b>Figure 17.</b> <span style="font-size: 14px"> The electrical output of co-culture MFCs with optimized division of labor and bacteria proportion</span>
<a href="https://static.igem.org/mediawiki/2015/8/85/TJU-design-7.png"  target="_blank"><img src=" https://static.igem.org/mediawiki/2013/9/90/Enlarge.jpg " width="20" height="20" align="right" alt="" /></a></p></div></div></br>
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<a href="https://static.igem.org/mediawiki/2015/0/01/Result_00.png"  target="_blank"><img src=" https://static.igem.org/mediawiki/2013/9/90/Enlarge.jpg " width="20" height="20" align="right" alt="" /></a></p></div></div></br>
  
<div class="kuang" style="width:470px">
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</br><a href="https://static.igem.org/mediawiki/2015/1/1c/TJU-design-8.png" target="_blank" ><img src= "https://static.igem.org/mediawiki/2015/1/1c/TJU-design-8.png"  width="450"  alt=""/></a>
+
<p>We also attempted to put the fermentation bacteria into the system some time after <span style="font-style: italic">Shewanella</span>. However, the later joining of fermentation bacteria will the stability of the system so that the output oscillated for a period of time. We can see from the figure 18, even though the lasting time was longer than before, the maximum electricity output was still limited. </p></br>
 +
 
 +
<div class="kuang" style="width:770px">
 +
</br><a href="https://static.igem.org/mediawiki/2015/3/3b/Result_8%27.png" target="_blank" ><img src= "https://static.igem.org/mediawiki/2015/3/3b/Result_8%27.png"  width="750"  alt=""/></a>
 
<div id="Enlarge">           
 
<div id="Enlarge">           
<p> <b>Figure 1.</b> <span style="font-size: 14px"> XXXXXXXXXXXXXXXXXX</span>
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<p> <b>Figure 18.</b> <span style="font-size: 14px"> The electrical output of co-culture system with fermentation bacteria added 8 h later into the system</span>
<a href="https://static.igem.org/mediawiki/2015/1/1c/TJU-design-8.png"  target="_blank"><img src=" https://static.igem.org/mediawiki/2013/9/90/Enlarge.jpg " width="20" height="20" align="right" alt="" /></a></p></div></div></br>
+
  
 
 
  
  
  
  
<p style="font-weight: bolder">Future Work: </p>
+
 
<p>Although we made several innovative research in our project, there are still many other aspects to develop and optimize in the future. </br>
+
1. We plan to find out biofilm parts of <span style="font-style: italic">E.coli</span> and modify several key point to reduce adhesion effect. </br>
+
2. We need to further adjust ratio of our three-strain system to bring a quicker speed toward maximum. </br>
+
3. Keeping power generation unchanged, we can reduce the volume of our device so that it will increase current density. </br>
+
4. Making improvements in <span style="font-style: italic">Shewanella</span> for more electricity output. We intend to weaken any other unrelated functions except for power production in <span style="font-style: italic">Shewanella</span> and using co-culture system to produce necessary nutrition for its survival. </p></br>
+
<h3>References</h3>
+
    <hr></br>
+
<p> <span style="font-weight: lighter ;font-size:14px;" >[1] Song H, Ding M Z, Jia X Q, et al. Synthetic microbial consortia: from systematic analysis to construction and applications[J]. Chem.soc.rev, 2014, 43(20):6954-6981.</br>
+
[2] Tang Y J, Meadows A L, Keasling J D. A kinetic model describing <span style="font-style: italic">Shewanella oneidensis</span> MR-1 growth, substrate consumption, and product secretion.[J]. Biotechnology & Bioengineering, 2007, 96(1):125–133. </span></p>
+
  
<a name="Proteolysis" id="Proteolysis"></a><h3> 4 Proteolysis system </h3> <hr></br>
+
<p style="font-weight: bolder">MFC device—simple, convenient and high efficiency </p>
<p>During the experiment, our MFC in anaerobic condition has been found to reach an unexpected lower pH that showed harmful to bacterial consortium. On account of improving the rate of survival, we designed a “Sensing- Regulating” system to consume the accumulated lactate and keep the environment at a proper acid level. Our system belongs to proteomic regulation, which contains pH sensing system and orthogonal proteolysis system for self-regulating. The delayed effect within our sensing system brings us a more precise depict of possible result that the pH may oscillate at a certain range. </p></br>
+
  
<p style="font-weight: bolder">4.1  Sensing</p>
 
<p>Every genus of cell has an optimum range of pH to live and <span style="font-style: italic">Shewanella</span> along with <span style="font-style: italic">E.coli</span> is no exception. Previous research has identified that <span style="font-style: italic">Shewanella</span> can maintain a maximal population density when pH keeps above 6.2 while <span style="font-style: italic">E.coli</span> can survive in 5.6~8.1.[1] As an attempt to develop the superior sensing mechanism, we screen out promoter 170 (P170) and regulatory protein RcfB and introduce them into <span style="font-style: italic">E.coli</span> for adaption. </p></br>
 
  
<p>P170, a strongly acid-inducible promoter from <span style="font-style: italic">Lactococcus lactis</span>, is up-regulated at low pH during the transition to stationary phase.[2] The trans-acting protein RcfB, however, is involved in basal activity of P170 and is also essential for pH induction. The protein RcfB, upon activation by lactate, bind a DNA recognition motif within a promoter region and activates transcription.[3] When the cells are exposed to acid environments, the RcfB activation by an ‘acid’ signal allows its binding to the ACiD-box, resulting in transcription activation.[3] </p></br>
+
<div class="kuang" style="width:770px">
(酸感应原理图)
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</br><a href="https://static.igem.org/mediawiki/2015/7/75/666666.jpg" target="_blank" ><img src= "https://static.igem.org/mediawiki/2015/7/75/666666.jpg"  width="750"  alt=""/></a>
<p>To test the idea that P170 is sensitive to acidity under the regulation of RcfB, we construct RFP gene into circuit containing P170 and RcfB. The RFP is expressed on the basis of P170 activation and RcfB which functions as a novel regulatory protein however, is controlled by a constitutive promoter J23100. High level of P170 activity required both RcfB and acidic conditions. Therefore, with the constitutive expression of RcfB, once the pH reaches the threshold that usually ranges from pH 6.0 to pH 6.5, P170 will be induced so that RFP can reflect red fluorescence under UV detection. Although RFP verification test is well developed, other functional genes are also replace RFP gene as a strategy for application extension. In our later experiment, we substitute RFP for T7 polymerase for regulatory purpose. </p></br>
+
 
+
<div class="kuang" style="width:520px">
+
</br><a href="https://static.igem.org/mediawiki/2015/5/56/P170.png" target="_blank" ><img src= "https://static.igem.org/mediawiki/2015/5/56/P170.png"  width="500"  alt=""/></a>
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<div id="Enlarge">           
 
<div id="Enlarge">           
<p> <b>Figure 1.</b> <span style="font-size: 14px"> XXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXX</span><a href="https://static.igem.org/mediawiki/2015/5/56/P170.png"  target="_blank"><img src="https://static.igem.org/mediawiki/2013/9/90/Enlarge.jpg" width="20" height="20" align="right" alt="" /></a></p></div></div></br>
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<p> <b>Figure 22.</b> <span style="font-size: 14px"> Our prototype device for future application</span>
 +
<a href="https://static.igem.org/mediawiki/2015/7/75/666666.jpg"  target="_blank"><img src=" https://static.igem.org/mediawiki/2013/9/90/Enlarge.jpg " width="20" height="20" align="right" alt="" /></a></p></div></div></br>
  
<p style="font-weight: bolder">4.2  Regulating</p>
 
<p>After activated sensing system which determines the pH threshold to suppress bacterial population density, we need to figure out how to retrieve to the proper acidity for living. Here comes our regulating system for acid recovery. </p></br>
 
  
<p>The ssrA tag sequence (mf-ssrA tag) and the Lon protease (mf-Lon) from <span style="font-style: italic">Mesoplasma florum</span> are made up of the crucial elements of a protein degradation system. Experiments has been identified that mf-ssrA tag is efficiently recognized by mf-Lon where the tag appends to C terminus of native or denatured proteins resulted in their rapid proteolysis by mf-Lon.[4] Besides, degradation system based on the Gram-positive <span style="font-style: italic">M. florum</span> tmRNA system does not rely on host degradation systems and can function in a wide range of bacteria, which makes it an adaptive method in variety. Here, we use this proteolysis system for lactate regulation and keep it in a oscillatory value of acidity. </p></br>
 
  
<p>Specifically, we utilize the effect of mf-Lon as well as ldhE bearing with tag under the control T7 promoter and J2310 promoter respectively, to degrade the overmuch lactate. We also aware that T7 promoter activation requires the combination of T7 RNA polymerase which is extremely promoter-specific and transcribes only DNA downstream of a T7 promoter.[5] According to the extensive study of our ‘sensing’ system, we substitute the RFP for T7 polymerase hoping that lower pH stage can activate T7 polymerase activation which then combines with T7 promoter for acting and mf-Lon, in this way, also expresses. It turns out that <span style="font-style: italic">ldhE</span> togethered with mf-ssrA tag can be degraded by cytoplasmic mf-Lon. So the pH can maintain in a proper level for cells’ living. </p></br>
+
    <a name="References" id="References"></a><h3>References</h3>
(模块图)(实验表征结果和说明)
+
<p>Notably, the proteolysis system has potential to apply in many fields. As a strategy to make it a toolbox for further research, we use different tags to test the strength of its proteolysis. With the reflection of red fluorescence, we are able to detect mf-Lon activity on various tags based on the distinguish value of UV detection. This toolbox is intended to be a fast and convenient method for prospective proteolysis option and degradation research. </p></br>
+
 
+
<div class="kuang" style="width:520px">
+
</br><a href="https://static.igem.org/mediawiki/2015/d/db/TAG.png" target="_blank" ><img src= "https://static.igem.org/mediawiki/2015/d/db/TAG.png"  width="500"  alt=""/></a>
+
<div id="Enlarge">        
+
<p> <b>Figure 1.</b> <span style="font-size: 14px"> XXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXXX</span><a href="https://static.igem.org/mediawiki/2015/d/db/TAG.png"  target="_blank"><img src="https://static.igem.org/mediawiki/2013/9/90/Enlarge.jpg" width="20" height="20" align="right" alt="" /></a></p></div></div></br>
+
(实验表征结果和说明)
+
 
+
<h3>References</h3>
+
 
     <hr></br>
 
     <hr></br>
<p> <span style="font-weight: lighter ;font-size:14px;" > [1] Min C, Chung H, Choi W, et al. Linear correlation between inactivation of <span style="font-style: italic">E. coli</span> and OH radical concentration in TiO2 photocatalytic disinfection.[J]. Water Research, 2004, 38(4):1069–1077.  
+
<p> <span style="font-weight: lighter ;font-size:14px;" > [1] Tang Y J, Meadows A L, Keasling J D. A kinetic model describing <span style="font-style: italic">Shewanella oneidensis</span> MR-1 growth, substrate consumption, and product secretion.[J]. Biotechnology & Bioengineering, 2007, 96(1):125–133.</br>
[2] Madsen S M, Arnau J, Vrang A, et al. Molecular characterization of the pH-inducible and growth phase-dependent promoter P170 of <span style="font-style: italic">Lactococcus lactis</span>.[J]. Molecular Microbiology, 1999, 32(1):75-87.</br>
+
[2] Feng X, Xu Y, Chen Y, et al. Integrating Flux Balance Analysis into Kinetic Models to Decipher the Dynamic Metabolism of <span style="font-style: italic">Shewanella oneidensis</span> MR-1[J]. Plos Computational Biology, 2011, 8(2):e1002376-e1002376. </br>
[3] Madsen, Søren M, Hindré, Thomas, Le Pennec, Jean‐Paul, et al. Two acid‐inducible promoters from <span style="font-style: italic">Lactococcus lactis</span> require the cis‐acting ACiD‐box and the transcription regulator RcfB[J]. Molecular Microbiology, 2005, 56(3):735-746.</br>
+
[3] Highly efficient L-lactate production using engineered <span style="font-style: italic">Escherichia coli</span> with dissimilar temperature optima for L-lactate formation and cell growth. </br>
[4] Eyal G, Sauer R T. Evolution of the ssrA degradation tag in <span style="font-style: italic">Mycoplasma</span>: specificity switch to a different protease.[J]. Proceedings of the National Academy of Sciences, 2008, 105(42):16113-16118.</br>
+
[4] Liu H, Kang J, Qi Q, et al. Production of lactate in <span style="font-style: italic">Escherichia coli</span> by redox regulation genetically and physiologically.[J]. Appl Biochem Biotechnol, 2011, 164(2):162-169. </br>
[5] Martin C T, Esposito E A, Theis K, et al. Structure and function in promoter escape by T7 RNA polymerase.[J]. Prog Nucleic Acid Res Mol Biol, 2005, 80(80):323–347.</span></p>
+
[5] Zhu J, Shimizu K, Zhu J, et al. Effect of a single-gene knockout on the metabolic regulation in <span style="font-style: italic">Escherichia coli</span> for D-lactate production under microaerobic condition[J]. Metabolic Engineering, 2005, 7(2):104–115. </br>
 +
[6] Thomas E, Kuhlman, Edward C, Cox. Site-specific chromosomal integration of large synthetic constructs.[J]. Nucleic Acids Research, 2010, 38(38). </br>
 +
[7] Lin Z, Xu Z, Li Y, et al. Metabolic engineering of <span style="font-style: italic">Escherichia coli</span> for the production of riboflavin[J]. Microbial Cell Factories, 2014, 13(1):1-12.
 +
</br>
 +
[8] Wang X, Tao L, Wang H, et al. Improving mediated electron transport in anodic bioelectrocatalysis[J]. Chemical Communications, 2015. </br>
 +
[9] Okamoto A, Nakamura R, Nealson K H, et al. Bound Flavin Model Suggests Similar Electron‐Transfer Mechanisms in <span style="font-style: italic">Shewanella</span> and <span style="font-style: italic">Geobacter</span>[J]. Chemelectrochem, 2014, 1(11):1808-1812. </br>
 +
[10] Yang Y, Ding Y, Hu Y, et al. Enhancing Bidirectional Electron Transfer of <span style="font-style: italic">Shewanella oneidensis</span> by a Synthetic Flavin Pathway[J]. Acs Synthetic Biology, 2015. </br>
 +
[11]Shi S, Chen T, Zhang Z, et al. Transcriptome analysis guided metabolic engineering of Bacillus subtilis for riboflavin production[J]. Metabolic engineering, 2009, 11(4): 243-252.</br>
 +
[12] Song H, Ding M Z, Jia X Q, et al. Synthetic microbial consortia: from systematic analysis to construction and applications[J]. Chem.soc.rev, 2014, 43(20):6954-6981.</br>
 +
</span></p>
  
  

Latest revision as of 14:17, 16 November 2015


Design


Naturally, we can barely find microorganisms that live in isolated niches, instead, there are full of various material, energy and information communications. In our project, we have been aware that Shewanella can efficiently use lactate as carbon substrate for power production. Therefore, high-yield of lactate seems critical for current generation and also for a reliable interaction between different species. Moreover, flavins mediated EET pathway is able to directly affect the electrons transfer and output, which inspired us to adopt flavins as a factor to achieve information interaction. Based on the research above, we further developed and optimized a co-culture system with three strains of bacterium in the MFC to achieve a more robust and efficient system. Apart from that, we designed a pH sensing and proteolysis system as a practical tool for troubleshooting and an attempt to benefit the future researchers.



Figure 1. The overall relationship of bacteria in our co-culture system.


1 Lactate producing system



Generally material flow, information flow, together with energy flow are key factors to regulate relations among bacterial consortium. Material flow, in particular, known as the most reliable and convenient method, is adopted in our construction. Typically the substances of the flow are often necessary nutrition for bacterial survival such as essential amino acid and carbon sources.



Figure 2. The raletively narrow range of carbon source of Shewanella.


Shewanella oneidensis can generate electricity with a relatively narrow range of carbon substrates, including lactate, acetate, formate, pyruvate and some amino acid.[1] It has been shown that Shewanella oneidensis MR-1 prefers the utilization of lactate as an energy-favorable carbon substrate as lactate-based biomass yield was higher than that for either acetate or pyruvate. Similarly, the lactate-based growth rate was much higher as well.[2] Thus, lactate is the most suitable carbon source and also the key mediator for the material flow in our system.



Figure 3. Our design of broadening the spectrum of carbon sources for MFCs based on Shewanella. Through it, we will presents the prospect of its expanding application range.


In order to develop a proper mechanism for lactate supply, we use Escherichia coli, a well characterized bacterium, to produce lactate. Previously, researchers has developed a system that was able to produce 142.2 g/L of L-lactate with no more than 1.2 g/L of by-products accumulated by knocking out ldhA and lldD and inserting L-LDH.[3] Consequently, E.coli has many advantages as a host for production of lactic acid, including the ability to produce optically pure lactate, rapid growth under both aerobic and anaerobic conditions, and its simple nutritional requirements.[4]


Escherichia coli grows fermentatively in glucose-containing medium under anaerobic condition with formation of a mixture of organic acids (lactate, acetate, formate and succinate) and ethanol, and lactate only takes no more than 50% of the total metabolites.[4] Since we need to provide enough material support for the growth and metabolism of Shewanella under anaerobic condition, we decided to enhance the yield of lactate by genetic engineering through two strategies:


1.1 ldh- Lactate dehydrogenase(LDHE)

LDH is an enzyme found in nearly all living cells (animals, plants, and prokaryotes), which catalyzes the conversion of pyruvate to lactate with NADH serving as the coenzyme. Naturally, E.coli can produce D-lactate by itself but the amount and the activity of lactate dehydrogenase becomes the bottleneck. We found that those two factors of enzyme are hard to change dramatically in vivo. So in our project, we intend to introduce high-yield exogenous L-(+)-lactate dehydrogenase gene (ldhA) from Lactobacillus, which can convert the redundant pyruvate and subsequently provide even more sustenance for Shewanella. Similar metabolic pathway has been found in a variety of organisms, to distinguish the differences, we renamed the heterogenous L-lactate dehydrogenase gene ldhE while homogenous one keeps original ldhA.



Figure 4. The part we design to produce L-lactate(LB medium).


After we transferred our part into E.coli BL21, we found there was little difference between the experimental group and control group.



Figure 5. The yield of lactate in flask-shaking fermentation condition (LB medium)


In order to enhance the transformation efficiency from glucose to lactate, as well as improve the characterization of our ldhE part, we decided to knockout the the pflB and poxB.



Figure 6. Lactate metabolic pathway. The pflB and poxB knocking out and ldhE insertion will result in the accumulation of lactate.


1.2 pflB knockout

PFL is a crucial enzyme in the glucose metabolism under anaerobic condition, which can catalyze one molecule of pyruvate to one molecule of formicate and one molecule of acetylcoenzyme A (AcCoA). According to metabolic pathway, pyruvate is consumed both in the PFL and LDH reactions. In the wild type E. coli, LDH reaction is not as competitive as the reaction through PFL, and therefore, knockout of the PFL related genes will contribute to redistribute the metabolic flux. When the PFL pathway is blocked, E. coli will conceivably alter the distribution of these products to overcome the imbalanced reducing equivalents caused by the pathway knockout. Therefore, knockout of pflB not only decreased the carbon flow to acetyl-CoA under anaerobic condition but also reduced the anaerobic consumption of NADH through reductive TCA. [5]


After the knockout of pflB, though the growth rate was slightly slowed down, the yield of lactate of engineered strain was improved greatly and showed a significant difference from the wild type MG1655. From the result, we can see our part functioned as expected.



Figure 7. Comparison diagram of lactate production of three different strains. MG1655: wild type ; MG1655ΔpflB: pflB knockout, ldhE blank; MG1655ΔpflB+ldhE: containing the functional ldhE part we design


1.3 Knockout strategy

For genes knockout, we adopted a effective, easy-to-use two-step system in which the cell is first transformed with a helper plasmid harboring genes encoding the λ-Red enzymes, I-SceI endonuclease, and RecA. λ-Red enzymes expressed from the helper plasmid are used to recombineer a small ‘landing pad’, a tetracycline resistance gene (tetA) flanked by I-SceI recognition sites and landing pad regions, into the desired location in the chromosome. After tetracycline selection for successful landing pad integrants, the cell is transformed with a donor plasmid carrying the desired insertion fragment; this fragment is excised by I-SceI and incorporated into the landing pad via recombination at the landing pad regions.[6]


First round of recombineering consists of three rounds of PCR for the construction of recombinant genome cassettes which subsequently positively selected by selection markers such as Tetr. In the second step, TetA marker was released by simultaneous induction of I-SceI and Red recombinase expression which serves as a negative selection.[7] (More details in Method.)



Figure 8. First step in the new two-step scar-less gene deletion using λ-Red recombineering method. Three rounds of PCR together with tet selection make up of our recombinant.



2 Flavins producing system



Shewanella oneidensis MR-1, a facultative anaerobe, has been widely used as a model anode biocatalyst in microbial fuel cells (MFCs) due to its easiness of cultivation, adaptability to aerobic and anaerobic environment and both respiratory and electron transfer versatility. [8]


Particularly, EET pathway can be subdivided into direct EET and mediated EET and the latter one limits the efficiency of electron transfer between bacteria and electrode due to the deficiency of electron mediator. To regulate relations of energy and information in the consortium, flavins hold the key to success.


It is widely accepted that interfacial EET is the rate-limiting step in the EET processes which can be relieved by some redox active molecules such as quinines and metal-centered porphyrin-ring derivatives. However, those redox active molecules are generally costly and toxic to anodic electricigens. Besides, Shewanella is capable of utilizing self-secreted flavins like riboflavin (RF) to accelerate EET, which is much more efficiently than other exogenous active molecules. More specifically, riboflavin (RF) and flavin mononucleotide (FMN) enhance EET more than five times, with much lower concentrations than those needed for anthraquinone-2,6-disulfonate (AQDS) shuttling. So we choose flavins as one entry point to enhance the electricity output of MFCs. [9]



Figure 9. Comparison of co-factor EET model(a) and diffusion EET model(b), (b) also reveals the electron pathway by endogenous flavins


In EET model, outward current flows from interior of cells to outer membrane (OM) and extracellular anodes through a metal-reducing conduit (Mtr pathway), where electrons (from NADH, the intracellular electron carrier) flow through the menaquinol pool, CymA (inner membrane [IM] tetraheme c-type cytochromes [c-Cyts]), MtrA (periplasmic decaheme c-Cyts), MtrB (β-barrel trans-OM protein) and finally to MtrC and OmcA (two OM decaheme c-Cyts). However, the principle of how flavins function still remains controversial. [10]


Traditional model demonstrates that flavins carry the electrons from OM c-Cyts to electrode by diffusion, which has been in debate due to thermodynamic disproof. Recently, another interfacial EET model was proposed, where flavin may serve as a co-factor binding to OmcA or MtrC to dictate EET. Fully oxidized flavin (Ox) accepts one electron from reduced heme of OM c-Cyts, and binds to OM c-Cyts as a cofactor in the semiquinone (Sq) form with shifted potential. Ox/Sq redox cycling in OM c-Cyts donates electrons to electrodes in a one electron reaction mode via direct contact.[10]



Figure 10. Pathway for engineered riboflavin and FMN production E. coli.


Although Shewanella uses endogenous flavins to mediate electrons, the amount of its production is deficient and multi-tasks brought by self-engineering may also reduce the transfer efficiency. As a consequence, we had two strategies to construct the zymophyte and further improve the production. Firstly, we introduced flavin producing genes using the E.coli as chassis. Secondly, we get an engineered B.subtilis strain from the lab of Dr. Tao Chen [11](more detail in attribution)


Based on the EET pathway theory, we suggest that by maximizing the amount of flavins, we may significantly enhance the EET efficiency and achieve a relatively high power generation.


We found a part BBa_K1172303 in Part Registry constructed by 2013 Team Bielefeld-Germany which was also aimed at producing riboflavins. However, the gene cluster showed a maximum output of 6 mg/L even with a strong promoter, which was insufficient to maintain a high and constant efficiency of EET pathway in our co-culture system. So we decided to optimize the part BBa_K1172303 to enhance the production of riboflavins.



Figure 11. Two different parts we designed to produce flavins.


As we learn from metabolic flux (figure 2), it reveals the relevant pathways of riboflavin production and engineering strategies for riboflavin production. In their previous research(Tao, et al) [7] ,they construct a high-yield E.coli strain with a yield of 229.1 mg/L. Based on their study, we constructed a flavin producing part (ribABDEC cluster) named EC10.(as shown in figure 11a). The part(BBa_K1696011) we designed, compared with BBa_K117230, has been well optimized and the yield of that reached 17 mg/L.( as shown in figure 13). We can see from the results, the functionality of their parts has successfully improved.



Figure 12. The production of EC10 in tubes.


In the meanwhile, based on co-factor model, EET pathway points out that FMN plays a critical role in electron transfer. Through the study by Dr. Tao Chen, they have weakened the RBS upstream of ribC to divert more of the material flux to RF production.[7] Based on their viewpoint, we got further to design a strong RBS sequence upstream of the ribC and we rename the new part as EC10*(BBa_K1696010). The yield of EC10* reached 90 mg/L(as shown in figure 11b). The strong RBS before ribC sequence can lead to the FMN accumulation while riboflavin consumes a bit, which may in turn, result in increasing both for riboflavin and FMN as a whole.



Figure 13. The yield of riboflavin in different strains :EC10, Rf02S (Δpgi+EC10), EC10*


When we characterized our part, we were not able to detect the FMN for lacking proper equipments. However, we were surprised to find that the production of EC10* was even better with a larger output of riboflavins. For riboflavin measurements, culture samples were diluted with 0.05 M NaOH to the linear range of the spectrophotometer and the A444 was immediately measured, according to the Dr. Tao Chen’s method [7]. As for the reason of production improvement of RF, we speculate that the strengthening of ribC gene can improve both the RF and FMN yield through the flavin metabolic pathway.


3 Co-culture MFC -- Division Of Labor



Microorganisms rarely live in isolated niches. One reason is that the maintenance of viability of these microbes may need supplementary metabolites or other signaling chemicals provided by other microbes in the ecosystems and communities.[11] Conforming to the trend of revolution, we apply the bacterial consortium in our MFC for greater power generation and increased duration.


Apart from the universal trend of nature, the mixed culture shares some unique advantages particularly in our MFC. For example, Shewanella originally can merely use few simple carbon substrates like lactate, acetate, formate, pyruvate and some amino acid.[1] However, our consortium as a whole can expand the absorption range of carbon resources and develop a more complex diagram of carbon input for Shewanella. Also, our intention is able to achieve comprehensive functions through “Division Of Labor” that monoculture can hardly manage. For instance, if we use only Shewanella to supply electricity, the production of flavins as well as other related reaction will inhibit current creation. These are fundamental reasons that we adopt the “mix” strategy in our project.


3.1 First Trial

Our experiment started with monoculture of Shewanella, in which we have found several important conclusions that might be used in the later trials:
(i) Shewanella alone cannot take good use of glucose as the mere carbon source to generate power.
(ii) Voltage has been improved when we add flavins to the monoculture medium, which proved that flavins indeed would help the power enhance.
(iii) As an attempt to choose a proper substance being used in the experiment, we put sodium lactate into service and found that Shewanella could achieve power output.



Figure 14. The electrical output of MFCs of single strain Shewanella oneidensis MR-1 with different substrates


3.2 Second Trial:

Since we’ve constructed the lactate producing strain (ldhE), the flavin producing strain (EC10) and an engineered strain bearing both ldhE and EC10, we initiated our co-culture experiment with different division of labor.



Figure 15. The electrical output of co-culture MFCs with preliminary division of labor



Figure 16. pH test of anode samples, with only sample 1 get reached above 6.5


3.3 Third trial

When we have preliminarily optimized the bacterial proportion and medium compositions, we got a significant improvement of the electricity output in spite of the relatively short sustaining time.(shown as follows)



Figure 17. The electrical output of co-culture MFCs with optimized division of labor and bacteria proportion


We also attempted to put the fermentation bacteria into the system some time after Shewanella. However, the later joining of fermentation bacteria will the stability of the system so that the output oscillated for a period of time. We can see from the figure 18, even though the lasting time was longer than before, the maximum electricity output was still limited.



Figure 18. The electrical output of co-culture system with fermentation bacteria added 8 h later into the system

MFC device—simple, convenient and high efficiency


Figure 22. Our prototype device for future application


References



[1] Tang Y J, Meadows A L, Keasling J D. A kinetic model describing Shewanella oneidensis MR-1 growth, substrate consumption, and product secretion.[J]. Biotechnology & Bioengineering, 2007, 96(1):125–133.
[2] Feng X, Xu Y, Chen Y, et al. Integrating Flux Balance Analysis into Kinetic Models to Decipher the Dynamic Metabolism of Shewanella oneidensis MR-1[J]. Plos Computational Biology, 2011, 8(2):e1002376-e1002376.
[3] Highly efficient L-lactate production using engineered Escherichia coli with dissimilar temperature optima for L-lactate formation and cell growth.
[4] Liu H, Kang J, Qi Q, et al. Production of lactate in Escherichia coli by redox regulation genetically and physiologically.[J]. Appl Biochem Biotechnol, 2011, 164(2):162-169.
[5] Zhu J, Shimizu K, Zhu J, et al. Effect of a single-gene knockout on the metabolic regulation in Escherichia coli for D-lactate production under microaerobic condition[J]. Metabolic Engineering, 2005, 7(2):104–115.
[6] Thomas E, Kuhlman, Edward C, Cox. Site-specific chromosomal integration of large synthetic constructs.[J]. Nucleic Acids Research, 2010, 38(38).
[7] Lin Z, Xu Z, Li Y, et al. Metabolic engineering of Escherichia coli for the production of riboflavin[J]. Microbial Cell Factories, 2014, 13(1):1-12.
[8] Wang X, Tao L, Wang H, et al. Improving mediated electron transport in anodic bioelectrocatalysis[J]. Chemical Communications, 2015.
[9] Okamoto A, Nakamura R, Nealson K H, et al. Bound Flavin Model Suggests Similar Electron‐Transfer Mechanisms in Shewanella and Geobacter[J]. Chemelectrochem, 2014, 1(11):1808-1812.
[10] Yang Y, Ding Y, Hu Y, et al. Enhancing Bidirectional Electron Transfer of Shewanella oneidensis by a Synthetic Flavin Pathway[J]. Acs Synthetic Biology, 2015.
[11]Shi S, Chen T, Zhang Z, et al. Transcriptome analysis guided metabolic engineering of Bacillus subtilis for riboflavin production[J]. Metabolic engineering, 2009, 11(4): 243-252.
[12] Song H, Ding M Z, Jia X Q, et al. Synthetic microbial consortia: from systematic analysis to construction and applications[J]. Chem.soc.rev, 2014, 43(20):6954-6981.

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