Team:Bielefeld-CeBiTec/Project/Isobutanol/Isobutanol
From 2014.igem.org
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- | <h1>Isobutanol</h1> | + | <h1>Module III - Isobutanol production</h1> |
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- | <div id="main_menue" style="margin-left: | + | <div id="main_menue" style="margin-left:320px; height:80px"> |
<a href="https://2014.igem.org/Team:Bielefeld-CeBiTec/Project/Isobutanol/Theory"style="color:#000000"> | <a href="https://2014.igem.org/Team:Bielefeld-CeBiTec/Project/Isobutanol/Theory"style="color:#000000"> | ||
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<a href="https://2014.igem.org/Team:Bielefeld-CeBiTec/Project/Isobutanol/GeneticalApproach"style="color:#000000"> | <a href="https://2014.igem.org/Team:Bielefeld-CeBiTec/Project/Isobutanol/GeneticalApproach"style="color:#000000"> | ||
<div class="main_menueButton" style="width:180px"> | <div class="main_menueButton" style="width:180px"> | ||
- | <p class="buttoncenter"><font color="#FFFFFF">Genetical | + | <p class="buttoncenter"><font color="#FFFFFF">Genetical Approach</font></p> |
</div> | </div> | ||
</a> | </a> | ||
- | <a href="https://2014.igem.org/Team:Bielefeld-CeBiTec/ | + | <br><br><a href="https://2014.igem.org/Team:Bielefeld-CeBiTec/Results/Isobutanol"style="color:#000000"> |
- | <div class="main_menueButton" style="width: | + | <div class="main_menueButton" style="width:90px; float:right;margin-right:330px"> |
- | <p class="buttoncenter"><font color="#FFFFFF"> | + | <p class="buttoncenter"><font color="#FFFFFF">Results</font></p> |
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- | + | <br> | |
<div class="element" style="margin:10px 10px 10px 10px; padding:10px 10px 10px 10px"> | <div class="element" style="margin:10px 10px 10px 10px; padding:10px 10px 10px 10px"> | ||
<div id="text"> | <div id="text"> | ||
<h6>Product Synthesis</h6> | <h6>Product Synthesis</h6> | ||
- | <p>The CO<sub>2</sub> fixation of <a href="https://2014.igem.org/Team:Bielefeld-CeBiTec/Project/CO2-fixation/CarbonDioxide">module II</a> | + | <p>The CO<sub>2</sub> fixation of <a href="https://2014.igem.org/Team:Bielefeld-CeBiTec/Project/CO2-fixation/CarbonDioxide">module II</a> generates 3-phosphoglycerate generated by the Calvin cycle. The 3-phosphoglycerate is transformed to pyruvate by glycolysis. The pyruvate is now used as the initial point for the product synthesis. Pyruvate is the starting point of the producing pathways of a variety of industrially relevant products like isobutanol, isoprene, putrescine or even antibiotics. We decided to introduce an isobutanol production pathway which starts with pyruvate (Figure 1). (<a href="#Atsumi2008">Atsumi et al., 2008</a>) This pathway is explained in more detail in the section <a href="https://2014.igem.org/Team:Bielefeld-CeBiTec/Project/Isobutanol/GeneticalApproach">Genetical Approach</a>. |
<br> | <br> | ||
- | For this we | + | For this we used and improved some of the BioBricks from iGEM Team NCTU Formosa 2011/2012, which were available at the parts registry. We used the gene coding sequences of four out of five required proteins for the isobutanol production. For further information about our cloning strategic, please check our <a href="https://2014.igem.org/Team:Bielefeld-CeBiTec/Project/Isobutanol/GeneticalApproach">Genetical Approach</a> section. |
+ | <br> | ||
+ | We used coding sequences for the following proteins: | ||
<ul> | <ul> | ||
<li>AlsS (α-acetolactate synthase)</li> | <li>AlsS (α-acetolactate synthase)</li> | ||
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<li>KivD (α-ketoisovalerate decarboxylase)</li> | <li>KivD (α-ketoisovalerate decarboxylase)</li> | ||
</ul> | </ul> | ||
- | Adh ( | + | Adh (alcohol dehydrogenase), the fifth required protein, was not available as a BioBrick but because of <a href="https://2014.igem.org/Team:Bielefeld-CeBiTec/Notebook/Organisms#E.coli" target="_blank"><i>Escherichia coli</i></a>'s own AdhE the pathway works. (<a href="#Atsumi2008">Atsumi et al., 2008</a>) |
<br><br> | <br><br> | ||
- | <center> | + | <table style="background-color:transparent; cellspacing=3;"> |
+ | <tr><td> | ||
+ | <div class="element" style="margin:10px; padding:10px; text-align:center; width:250px"> | ||
+ | <a href="https://static.igem.org/mediawiki/2014/a/a9/Bielefeld_CeBiTec_2014-10-17_Isobutanol_pathway_reduced.png" target="_blank"><img src="https://static.igem.org/mediawiki/2014/a/a9/Bielefeld_CeBiTec_2014-10-17_Isobutanol_pathway_reduced.png" width="250px"></a><br> | ||
+ | <font size="2" style="text-align:left;"><b>Figure 1:</b> Schematic illustration of the isobutanol pathway (<a href="#Atsumi2008">Atsumi et al., 2008</a>)</font> | ||
+ | </div> | ||
+ | </td><td> | ||
<div class="element" style="margin:10px; padding:10px; text-align:center; width:600px"> | <div class="element" style="margin:10px; padding:10px; text-align:center; width:600px"> | ||
<a href="https://static.igem.org/mediawiki/2014/e/ed/Bielefeld-CeBiTec_2014-10-12_module_III.png" target="_blank"><img src="https://static.igem.org/mediawiki/2014/e/ed/Bielefeld-CeBiTec_2014-10-12_module_III.png" width="600px"></a><br> | <a href="https://static.igem.org/mediawiki/2014/e/ed/Bielefeld-CeBiTec_2014-10-12_module_III.png" target="_blank"><img src="https://static.igem.org/mediawiki/2014/e/ed/Bielefeld-CeBiTec_2014-10-12_module_III.png" width="600px"></a><br> | ||
- | <font size="2" style="text-align:left;"><b>Figure | + | <font size="2" style="text-align:left;"><b>Figure 2:</b> Schematic illustration of module III - the production of isobutanol. 3-phosphoglycerate from the CO<sub>2</sub> fixation is converted to pyruvate in the glycolysis. In the implemented pathway pyruvate is then converted to isobutanol (<a href="#Atsumi2008">Atsumi et al., 2008</a>)</font> |
</div> | </div> | ||
- | </ | + | </td></tr> |
+ | </table> | ||
- | The product synthesis can be changed through the modularity of BioBricks so that variable high value products derived from pyruvate can be implemented in the future. </p> | + | The product synthesis can be changed through the modularity of BioBricks, so that variable high value products derived from pyruvate can be implemented in the future. </p> |
</div> | </div> | ||
</div> | </div> | ||
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<div id="text"> | <div id="text"> | ||
<h6>Isobutanol</h6> | <h6>Isobutanol</h6> | ||
- | <p>Isobutanol is an amino-acid-based alcohol | + | <p>Isobutanol is an amino-acid-based alcohol and consequently an organic substance.</p> |
<center> | <center> | ||
<div class="element" style="margin:10px; padding:10px; width:200px;"> | <div class="element" style="margin:10px; padding:10px; width:200px;"> | ||
- | <img src="https://static.igem.org/mediawiki/2014/6/64/Bielefeld-CeBiTec_2014-10-15_Isobutanol_structure.png" width="200px" align="center"><br> | + | <a href="https://static.igem.org/mediawiki/2014/6/64/Bielefeld-CeBiTec_2014-10-15_Isobutanol_structure.png"> |
- | <font size="2" style="text-align:left;"><b>Figure | + | <img src="https://static.igem.org/mediawiki/2014/6/64/Bielefeld-CeBiTec_2014-10-15_Isobutanol_structure.png" width="200px" align="center"></a><br> |
+ | <font size="2" style="text-align:left;"><b>Figure 3:</b> Chemical structure of isobutanol.</font> | ||
</div> | </div> | ||
</center> | </center> | ||
<p> | <p> | ||
- | It can be produced by the 2-keto-acid, or Ehrlich, pathway. In this pathway 2-ketoisovalerate is first decarboxylated into isobutyraldehyde by the | + | It can be produced by the 2-keto-acid, or Ehrlich, pathway. In this pathway 2-ketoisovalerate is first decarboxylated into isobutyraldehyde by the keto-acid decarboxylase and then reduced to an alcohol by an alcohol dehydrogenase. Keto-acids are immediate amino-acid precursors. By using this enzymatic conversion amino-acid-based alcohols can be produced in <i>E. coli</i>. These alcohols include <i>n</i>-butanol, <i>n-</i>propanol and isobutanol. Although the energy contents of isobutanol and <i>n</i>-butanol are similar, isobutanol is the closest to industrial use. Isobutanol has a better octane number because it is a branched-chain alcohol in comparison to straight-chain alcohols like ethanol. This indicates that isobutanol could be a possible alternative to ethanol as a fuel additive. In contrast to ethanol, the traditional biofuel respectively biofuel supplement, isobutanol as a higher alcohol has a lower hygroscopicity. |
+ | Implementation of these characteristics in one of our <a href="https://2014.igem.org/Team:Bielefeld-CeBiTec/HumanPractice/Synenergene/Applications#Isobutanol">application scenarios</a>. (<a href="#Atsumi2008">Atsumi et al., 2008</a>; <a href="#Pamela2012">Peralta-Yahya et al., 2012</a>) | ||
<br> | <br> | ||
- | In the following table you can find some general information about isobutanol. | + | In the following table 1 you can find some general information about isobutanol. |
<center> | <center> | ||
- | <table style="background-color:transparent; cellspacing= | + | <div class="element" style="margin:10px; padding:10px; width:450px;"> |
- | <tr> | + | <font size="2" style="text-align:left;"><b>Table 1:</b> General information about isobutanol (<a href="#INCHEM2004">INCHEM, 2004</a>)</font> |
- | <td>CAS Number</td><td>78-83-1</td> | + | <table style="background-color:transparent; cellspacing=3;"> |
- | </tr> | + | <tr><td>CAS Number</td><td>78-83-1</td></tr> |
- | <tr> | + | <tr><td>IUPAC Name</td><td>2-methyl-propan-1-ol </td></tr> |
- | <td>IUPAC Name</td><td>2-methyl-propan-1-ol </td> | + | <tr><td>Synonyms</td><td>isobutyl alcohol</td></tr> |
- | </tr> | + | <tr><td></td><td>IBA, IBOH </td></tr> |
- | <tr> | + | <tr><td></td><td>fermentation butyl alcohol</td></tr> |
- | <td>Synonyms</td><td>isobutyl alcohol</td> | + | <tr><td></td><td>1-hydroxymethylpropane</td></tr> |
- | </tr> | + | <tr><td></td><td>isobutanol </td></tr> |
- | < | + | <tr><td></td><td>isopropylcarbinol</td></tr> |
- | + | <tr><td></td><td>2-methylpropanol</td></tr> | |
- | <td></td><td>IBA, IBOH </td> | + | <tr><td></td><td>2-methyl-1-propanol</td></tr> |
- | </tr> | + | <tr><td></td><td>2-methylpropan-1-ol</td></tr> |
- | < | + | <tr><td></td><td>2-methylpropyl alcohol </td></tr> |
- | + | <tr><td>Molecular Formula</td><td>C4H10O </td></tr> | |
- | <td></td><td>fermentation butyl alcohol</td> | + | <tr><td>Structural Formula</td><td>(CH3)2-CH-CH2OH</td></tr> |
- | </tr> | + | <tr><td>Molecular Weight</td><td>74.12 g/mol </td></tr> |
- | < | + | <tr><td>density</td><td>802.00 kg/m<sup>3</sup> </td></tr> |
- | + | <tr><td>Physical state</td><td>Liquid</td></tr> | |
- | <td></td><td>1-hydroxymethylpropane</td> | + | <tr><td>Melting point</td><td>-108°C</td></tr> |
- | </tr> | + | <tr><td>Boiling point</td><td>108°C</td></tr> |
- | < | + | <tr><td>Water solubility</td><td>85.0 g/l at 25°C </td></tr> |
- | + | ||
- | <td></td><td>isobutanol </td> | + | |
- | </tr> | + | |
- | < | + | |
- | + | ||
- | <td></td><td>isopropylcarbinol</td> | + | |
- | </tr> | + | |
- | <tr> | + | |
- | <td></td><td>2-methylpropanol</td> | + | |
- | </tr> | + | |
- | <tr> | + | |
- | <td></td><td>2-methyl-1-propanol</td> | + | |
- | </tr> | + | |
- | <tr> | + | |
- | <td></td><td>2-methylpropan-1-ol</td> | + | |
- | </tr> | + | |
- | <tr> | + | |
- | <td></td><td>2-methylpropyl alcohol </td> | + | |
- | </tr> | + | |
- | <tr> | + | |
- | <td>Molecular Formula</td><td>C4H10O </td> | + | |
- | </tr> | + | |
- | <tr> | + | |
- | <td>Structural Formula</td><td>(CH3)2-CH-CH2OH</td> | + | |
- | </tr> | + | |
- | <tr> | + | |
- | <td>Molecular Weight</td><td>74.12 g/mol </td> | + | |
- | </tr> | + | |
- | </tr> | + | |
- | <tr> | + | |
- | <td>Physical state</td><td>Liquid</td> | + | |
- | </tr> | + | |
- | < | + | |
- | + | ||
- | <td>Melting point</td><td>-108°C</td> | + | |
- | </tr> | + | |
- | < | + | |
- | + | ||
- | <td>Boiling point</td><td>108°C</td> | + | |
- | </tr> | + | |
- | < | + | |
- | + | ||
- | <td>Water solubility</td><td>85.0 g/l at 25°C </td> | + | |
- | </tr> | + | |
</table> | </table> | ||
+ | </div> | ||
</center> | </center> | ||
</p> | </p> | ||
- | + | </div> | |
<br><br> | <br><br> | ||
- | + | <div class="element" style="margin:10px 10px 10px 10px; padding:10px 10px 10px 10px"> | |
+ | <div id="text"> | ||
<h4>Production</h4> | <h4>Production</h4> | ||
- | <p>In 1998 the U.S. EPA Inventory Update Report (IUR) listed 16 manufacturing facilities in the United States. | + | <p>In 1998 the U.S. EPA Inventory Update Report (IUR) listed 16 manufacturing facilities in the United States. Altogether these facilities produced between 100 and 500 million pounds of isobutanol per year, which are 45.4 – 227.3 thousand metric tons. Manufacturing facilities of other regions or countries in 2002 including their manufacturing capacities are listed in the following table 2. (<a href="#INCHEM2004">INCHEM, 2004</a>) |
+ | |||
<center> | <center> | ||
- | <table style="background-color:transparent; cellspacing= | + | <div class="element" style="margin:10px; padding:10px; width:650px;"> |
- | <tr> | + | <font size="2" style="text-align:left;"><b>Table 2:</b> Information about the producing facilities in various regions and countries including their manufacturing capacities in 2002 (<a href="#INCHEM2004">INCHEM, 2004</a>; <a href="#Bizzari2002">Bizzari, 2002</a>)</font> |
- | <th>Region or country</th><th>Number of producers</th><th>Manufacturing capacities [metric tons]</th> | + | <table style="background-color:transparent; cellspacing=3;"> |
- | </tr> | + | <tr><th>Region or country</th><th>Number of producers</th><th>Manufacturing capacities <br>[metric tons]</th></tr> |
- | <tr> | + | <tr><td>Western Europe</td><td>4</td><td>160,000</td></tr> |
- | <td>Western Europe</td><td>4</td><td>160,000</td> | + | <tr><td>Eastern Europe</td><td>3</td><td>69,000 (including some n-butyl alcohol)</td></tr> |
- | </tr> | + | <tr><td>Russia</td><td>3</td><td>48,000</td></tr> |
- | < | + | <tr><td>Iran</td><td>1</td><td>6,000</td></tr> |
- | + | <tr><td>Japan</td><td>3</td><td>43,000</td></tr> | |
- | <td>Eastern Europe</td><td>3</td><td>69,000 (including some n-butyl alcohol)</td> | + | <tr><td>China</td><td>2</td><td>14,000</td></tr> |
- | </tr> | + | <tr><td>India</td><td>n.a.</td><td>8,000 (including some n-butyl alcohol)</td></tr> |
- | < | + | <tr><td>Indonesia</td><td>1</td><td>10,000</td></tr> |
- | + | <tr><td>Korea</td><td>2</td><td>25,000</td></tr> | |
- | <td>Russia</td><td>3</td><td>48,000</td> | + | <tr><td>Brazil</td><td>1</td><td>19,000</td></tr> |
- | </tr> | + | |
- | < | + | |
- | + | ||
- | <td>Iran</td><td>1</td><td>6,000</td> | + | |
- | </tr> | + | |
- | < | + | |
- | + | ||
- | <td>Japan</td><td>3</td><td>43,000</td> | + | |
- | </tr> | + | |
- | < | + | |
- | + | ||
- | <td>China</td><td>2</td><td>14,000</td> | + | |
- | </tr> | + | |
- | < | + | |
- | + | ||
- | <td>India</td><td>n.a.</td><td>8,000 (including some n-butyl alcohol)</td> | + | |
- | </tr> | + | |
- | <tr> | + | |
- | <td>Indonesia</td><td>1</td><td>10,000</td> | + | |
- | </tr> | + | |
- | <tr> | + | |
- | <td>Korea</td><td>2</td><td>25,000</td> | + | |
- | </tr> | + | |
- | <tr> | + | |
- | <td>Brazil</td><td>1</td><td>19,000</td> | + | |
- | </tr> | + | |
</table> | </table> | ||
+ | </div> | ||
</center> | </center> | ||
</p> | </p> | ||
+ | </div> | ||
+ | </div> | ||
- | < | + | <div class="element" style="margin:10px 10px 10px 10px; padding:10px 10px 10px 10px"> |
- | + | <div id="text"> | |
- | <h4> | + | <h4>Applications</h4> |
- | <p>Isobutanol has many applications. In the following table you can find a list of | + | <p>Isobutanol has many applications. In the following table 3 you can find a list of the span of applications and how much isobutanol is applied for the various uses in the United States. |
<br> | <br> | ||
- | < | + | <center> |
- | < | + | <div class="element" style="margin:10px; padding:10px; width:550px;"> |
- | < | + | <font size="2" style="text-align:left;"><b>Table 3:</b> Industrial applications of isobutanol and their required amounts (<a href="#INCHEM2004">INCHEM, 2004</a>; <a href="#Bizzari2002">Bizzari, 2002</a>)</font> |
- | < | + | <table style="background-color:transparent; cellspacing=3;"> |
- | </tr> | + | <tr><th>Application</th><th>Amount [metric tons]</th></tr> |
- | <tr> | + | <tr><td>lube oil additives (in which isobutyl alcohol is an intermediate to produce the lube oil additive ZDDP)</td><td>19,000</td></tr> |
- | <td>(in which isobutyl alcohol is an intermediate | + | <tr><td>conversion to isobutyl acetate</td><td>10,000</td></tr> |
- | + | <tr><td>direct solvent</td><td>9,000</td></tr> | |
- | + | <tr><td>conversion to amino resins</td><td>7,000</td></tr> | |
- | + | <tr><td>conversion to isobutylamines</td><td>1,000</td></tr> | |
- | </tr> | + | <tr><td>conversion to acrylate and methacrylate esters</td><td>1,000</td></tr> |
- | <tr> | + | <tr><td>other uses</td><td>1,000</td></tr> |
- | <td>conversion to isobutyl acetate</td><td>10 | + | |
- | </tr> | + | |
- | <tr> | + | |
- | <td>direct solvent</td><td>9 | + | |
- | </tr> | + | |
- | <tr> | + | |
- | <td>conversion to amino resins</td><td>7 | + | |
- | </tr> | + | |
- | <tr> | + | |
- | <td>conversion to isobutylamines</td><td>1 | + | |
- | </tr> | + | |
- | <tr> | + | |
- | <td>conversion to acrylate and methacrylate esters</td><td>1 | + | |
- | </tr> | + | |
- | <tr> | + | |
- | <td>other uses</td><td>1 | + | |
- | + | ||
- | + | ||
- | + | ||
- | </tr> | + | |
</table> | </table> | ||
+ | </div> | ||
+ | </center> | ||
+ | <br> | ||
+ | As the table shows there are three big markets for isobutanol in the United States. The largest one is the production of zinc dialkyldithiophosphates (ZDDP). ZDDP is an additive for lube oils, greases and hydraulic fluids, which work as anti-wear and corrosion inhibitors. | ||
+ | <br>The conversion of isobutanol to isobutyl acetate is the second largest market. Applications of isobutyl acetate are for example coating, adhesives, or cosmetic/personal care solve (<a href="#DOW">DOW</a>).<br> | ||
+ | The use of isobutanol as a solvent is the third largest market. It is mainly used for surface coatings and adhesives. Hence it is used as a latent solvent in surface coatings or even as a processing solvent in the production of e.g. pesticides and pharmaceuticals.(<a href="#INCHEM2004">INCHEM, 2004</a>) | ||
+ | These tables show the importance of isobutanol for industrial use and large amounts are needed all over the world. | ||
<br> | <br> | ||
- | + | We thought about different additional applications of isobutanol during our lively policy and practices discussion. You can find our suggestions <a href="https://2014.igem.org/Team:Bielefeld-CeBiTec/HumanPractice/Synenergene/Applications#Isobutanol">here</a> | |
- | + | ||
- | + | ||
- | + | ||
</p> | </p> | ||
</div> | </div> | ||
+ | </div> | ||
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+ | <br> | ||
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+ | <!-- Button begin --> | ||
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+ | <div id="main_menue" style="margin-left:320px; height:80px"> | ||
+ | <a href="https://2014.igem.org/Team:Bielefeld-CeBiTec/Project/Isobutanol/Theory"style="color:#000000"> | ||
+ | <div class="main_menueButton" style="width:100px"> | ||
+ | <p class="buttoncenter"><font color="#FFFFFF">Overview</font></p> | ||
+ | </div> | ||
+ | </a> | ||
+ | <a href="https://2014.igem.org/Team:Bielefeld-CeBiTec/Project/Isobutanol/Isobutanol"style="color:#000000"> | ||
+ | <div class="main_menueButtonActual" style="width:100px"> | ||
+ | <p class="buttoncenter"><font color="#FFFFFF">Isobutanol</font></p> | ||
+ | </div> | ||
+ | </a> | ||
+ | <a href="https://2014.igem.org/Team:Bielefeld-CeBiTec/Project/Isobutanol/GeneticalApproach"style="color:#000000"> | ||
+ | <div class="main_menueButton" style="width:180px"> | ||
+ | <p class="buttoncenter"><font color="#FFFFFF">Genetical Approach</font></p> | ||
+ | </div> | ||
+ | </a> | ||
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<h6>References</h6> | <h6>References</h6> | ||
<ul> | <ul> | ||
- | <li id=" | + | </li> |
+ | <li id="Atsumi2008"> | ||
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- | + | Atsumi S, Hanai T, Liao JC., 2008. Non-fermentative pathways for synthesis of branched-chain higher alcohols as biofuels. In: <a href="http://www.nature.com/nature/journal/v451/n7174/full/nature06450.html" target="_blank">Nature 451</a>, 86–89. | |
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+ | Bizzari, S.N., R. Gubler, and A. Kishi., 2002. CEH Marketing Research Report for Plasticizer | ||
+ | Alcohols. In: <a href="http://www.ihs.com/products/chemical/planning/ceh/plasticizer-alcohols.aspx?pu=1&rd=chemihs" target="_blank">IHS Chemical</a> | ||
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+ | Dow Chemical (DOW): <a href="http://msdssearch.dow.com/PublishedLiteratureDOWCOM/dh_0119/0901b8038011961c.pdf?filepath=oxysolvents/pdfs/noreg/327-00023.pdf&fromPage=GetDoc" target="_blank">Isobutyl Acetate</a>, version: 10/2014 | ||
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INCHEM: <a href="http://www.inchem.org/documents/sids/sids/78831.pdf" target="_blank">SIDS Initial Assessment Report | INCHEM: <a href="http://www.inchem.org/documents/sids/sids/78831.pdf" target="_blank">SIDS Initial Assessment Report | ||
- | For SIAM 19</a>, version: | + | For SIAM 19</a>, version: 10/2014 |
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- | + | Pamela P. Peralta-Yahya, Fuzhong Zhang, Stephen B. del Cardayre & Jay D. Keasling, 2012. Microbial engineering for the production of advanced biofuels. In: <a href="http://www.nature.com/nature/journal/v488/n7411/full/nature11478.html" target="_blank">Nature 488</a>, 320–328 | |
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Latest revision as of 10:02, 2 December 2014
Module III - Isobutanol production
Product Synthesis
The CO2 fixation of module II generates 3-phosphoglycerate generated by the Calvin cycle. The 3-phosphoglycerate is transformed to pyruvate by glycolysis. The pyruvate is now used as the initial point for the product synthesis. Pyruvate is the starting point of the producing pathways of a variety of industrially relevant products like isobutanol, isoprene, putrescine or even antibiotics. We decided to introduce an isobutanol production pathway which starts with pyruvate (Figure 1). (Atsumi et al., 2008) This pathway is explained in more detail in the section Genetical Approach.
For this we used and improved some of the BioBricks from iGEM Team NCTU Formosa 2011/2012, which were available at the parts registry. We used the gene coding sequences of four out of five required proteins for the isobutanol production. For further information about our cloning strategic, please check our Genetical Approach section.
We used coding sequences for the following proteins:
- AlsS (α-acetolactate synthase)
- IlvC (Ketol-acid reductoisomerase)
- IlvD (Dihydroxyacid dehydratase)
- KivD (α-ketoisovalerate decarboxylase)
Figure 2: Schematic illustration of module III - the production of isobutanol. 3-phosphoglycerate from the CO2 fixation is converted to pyruvate in the glycolysis. In the implemented pathway pyruvate is then converted to isobutanol (Atsumi et al., 2008) |
Isobutanol
Isobutanol is an amino-acid-based alcohol and consequently an organic substance.
It can be produced by the 2-keto-acid, or Ehrlich, pathway. In this pathway 2-ketoisovalerate is first decarboxylated into isobutyraldehyde by the keto-acid decarboxylase and then reduced to an alcohol by an alcohol dehydrogenase. Keto-acids are immediate amino-acid precursors. By using this enzymatic conversion amino-acid-based alcohols can be produced in E. coli. These alcohols include n-butanol, n-propanol and isobutanol. Although the energy contents of isobutanol and n-butanol are similar, isobutanol is the closest to industrial use. Isobutanol has a better octane number because it is a branched-chain alcohol in comparison to straight-chain alcohols like ethanol. This indicates that isobutanol could be a possible alternative to ethanol as a fuel additive. In contrast to ethanol, the traditional biofuel respectively biofuel supplement, isobutanol as a higher alcohol has a lower hygroscopicity.
Implementation of these characteristics in one of our application scenarios. (Atsumi et al., 2008; Peralta-Yahya et al., 2012)
In the following table 1 you can find some general information about isobutanol.
CAS Number | 78-83-1 |
IUPAC Name | 2-methyl-propan-1-ol |
Synonyms | isobutyl alcohol |
IBA, IBOH | |
fermentation butyl alcohol | |
1-hydroxymethylpropane | |
isobutanol | |
isopropylcarbinol | |
2-methylpropanol | |
2-methyl-1-propanol | |
2-methylpropan-1-ol | |
2-methylpropyl alcohol | |
Molecular Formula | C4H10O |
Structural Formula | (CH3)2-CH-CH2OH |
Molecular Weight | 74.12 g/mol |
density | 802.00 kg/m3 |
Physical state | Liquid |
Melting point | -108°C |
Boiling point | 108°C |
Water solubility | 85.0 g/l at 25°C |
Production
In 1998 the U.S. EPA Inventory Update Report (IUR) listed 16 manufacturing facilities in the United States. Altogether these facilities produced between 100 and 500 million pounds of isobutanol per year, which are 45.4 – 227.3 thousand metric tons. Manufacturing facilities of other regions or countries in 2002 including their manufacturing capacities are listed in the following table 2. (INCHEM, 2004)
Region or country | Number of producers | Manufacturing capacities [metric tons] |
---|---|---|
Western Europe | 4 | 160,000 |
Eastern Europe | 3 | 69,000 (including some n-butyl alcohol) |
Russia | 3 | 48,000 |
Iran | 1 | 6,000 |
Japan | 3 | 43,000 |
China | 2 | 14,000 |
India | n.a. | 8,000 (including some n-butyl alcohol) |
Indonesia | 1 | 10,000 |
Korea | 2 | 25,000 |
Brazil | 1 | 19,000 |
Applications
Isobutanol has many applications. In the following table 3 you can find a list of the span of applications and how much isobutanol is applied for the various uses in the United States.
Application | Amount [metric tons] |
---|---|
lube oil additives (in which isobutyl alcohol is an intermediate to produce the lube oil additive ZDDP) | 19,000 |
conversion to isobutyl acetate | 10,000 |
direct solvent | 9,000 |
conversion to amino resins | 7,000 |
conversion to isobutylamines | 1,000 |
conversion to acrylate and methacrylate esters | 1,000 |
other uses | 1,000 |
As the table shows there are three big markets for isobutanol in the United States. The largest one is the production of zinc dialkyldithiophosphates (ZDDP). ZDDP is an additive for lube oils, greases and hydraulic fluids, which work as anti-wear and corrosion inhibitors.
The conversion of isobutanol to isobutyl acetate is the second largest market. Applications of isobutyl acetate are for example coating, adhesives, or cosmetic/personal care solve (DOW).
The use of isobutanol as a solvent is the third largest market. It is mainly used for surface coatings and adhesives. Hence it is used as a latent solvent in surface coatings or even as a processing solvent in the production of e.g. pesticides and pharmaceuticals.(INCHEM, 2004) These tables show the importance of isobutanol for industrial use and large amounts are needed all over the world.
We thought about different additional applications of isobutanol during our lively policy and practices discussion. You can find our suggestions here
References
-
Atsumi S, Hanai T, Liao JC., 2008. Non-fermentative pathways for synthesis of branched-chain higher alcohols as biofuels. In: Nature 451, 86–89.
-
Bizzari, S.N., R. Gubler, and A. Kishi., 2002. CEH Marketing Research Report for Plasticizer Alcohols. In: IHS Chemical
-
Dow Chemical (DOW): Isobutyl Acetate, version: 10/2014
-
INCHEM: SIDS Initial Assessment Report For SIAM 19, version: 10/2014
-
Pamela P. Peralta-Yahya, Fuzhong Zhang, Stephen B. del Cardayre & Jay D. Keasling, 2012. Microbial engineering for the production of advanced biofuels. In: Nature 488, 320–328