Team:NCTU Formosa/Project-sub5
From 2012.igem.org
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<div id="project-s5" class="project-s"> | <div id="project-s5" class="project-s"> | ||
<h1 id="project-s5-title" class="project-s-title"><a name="sub5"> </a> <span>Future works</span></h1> | <h1 id="project-s5-title" class="project-s-title"><a name="sub5"> </a> <span>Future works</span></h1> | ||
+ | <h2 id="project-s5-0-title" class="project-s-title"><a name="sub5-0"> </a> <span>Cellulase experiment</span></h2> | ||
+ | <p>In order to realize our idea of changing agricultural waste into biofuel, we figured that we could try to obtain glucose from cellulose by cellulase. This simple idea could be carried out by several procedures. First, we did a pre-experiment by using quantitative filter paper (Advantec) as cellulose source which was made with highest quality alpha cotton cellulose, and was ashless(<0.1%). We cut the filter paper into the size of 0.5 cm square. Next, we weighed and put 3 grams of the filter paper chips in a 50ml centrifuge tube filled up to 50ml with 0.1M Na-citrate (ph5.3). We then added 375mg cellulase, which came from Trichoderma reesei (Sigma-Aldrich) and put it in 40℃ incubation(200rpm) for 96 hours. After that, we could get milk-like filter paper mash. Finally, 3.6% of glucose was measured by doing DNS assay! </p> | ||
+ | <p>The next challenge would be use E. coli we modified to yield isobutanol with the glucose medium made by cellulose. We filtered and transferred the glucose medium to another flask, and added our M9T9 formula except of adding glucose into it. Then we inoculated E. coli in it for 24 to 42 hours, 42℃, 200rpm. The GC result of the isobutanol yield was 25ppm. Though it wasn’t prominent, it proved that the whole procedures (from cellulose degradation to isobutanol production) were practical. However, we could infer that underneath the toxicity tolerance, we still might acquire isobutanol as much as possible. So we must modify every procedure to enhance the yield of isobutanol. In the future, we will try rice stalks from a farm as cellulose source, hoping that the outcome will give everyone a big surprise!</p> | ||
+ | <div id="project-s5-p0" class="pimg"><p class="imgcap"><b>Figure 27.</b>The simplificative procedures of degrading cellulose to glucose, and then E. coli utilized it to yield isobutanol.</p></div> | ||
<h2 id="project-s5-1-title" class="project-s-title"><a name="sub5-1"> </a> <span>Ingredient Production</span></h2> | <h2 id="project-s5-1-title" class="project-s-title"><a name="sub5-1"> </a> <span>Ingredient Production</span></h2> | ||
- | <div id="project-s5-p1" class="pimg"><p class="imgcap"><b>Figure | + | <div id="project-s5-p1" class="pimg"><p class="imgcap"><b>Figure 28.</b>Cell-surface display of Cex by means of PgsA anchor protein</p></div><p></p> |
- | <div id="project-s5-p2" class="pimg"><p class="imgcap"><b>Figure | + | <div id="project-s5-p2" class="pimg"><p class="imgcap"><b>Figure 29.</b></p></div> |
<p>In order to realize our idea to change trash into fuel, we did some research. Therefore, what we have to do is to figure out how to degrade the cellulose. First, we want to get xylose from cellulose through xylanase. Xylanase is a class of enzyme which degrades the linear polysaccharide beta-1,4-xylan into xylose, thus breaks down hemicellulose, one of the major components of plant cell walls. Xylose is a good carbon source. As such, xylanase plays a major role in micro-organisms thriving on plant sources (mammals, conversely, do not produce xylanase).</p> | <p>In order to realize our idea to change trash into fuel, we did some research. Therefore, what we have to do is to figure out how to degrade the cellulose. First, we want to get xylose from cellulose through xylanase. Xylanase is a class of enzyme which degrades the linear polysaccharide beta-1,4-xylan into xylose, thus breaks down hemicellulose, one of the major components of plant cell walls. Xylose is a good carbon source. As such, xylanase plays a major role in micro-organisms thriving on plant sources (mammals, conversely, do not produce xylanase).</p> | ||
- | <p>According to the Journal of Applied Microbiology ( Y.P. Chen et al. 2011), the cell-surface display of Cex, which encodes xylanase from Cellulomonas fimi, was constructed on <i>E.coli</i> using PgsA as the anchor protein.In <b>Figure | + | <p>According to the Journal of Applied Microbiology ( Y.P. Chen et al. 2011), the cell-surface display of Cex, which encodes xylanase from Cellulomonas fimi, was constructed on <i>E.coli</i> using PgsA as the anchor protein.In <b>Figure 29</b>, it shows that Cex do have the activity to catalyze xylan into xylose.</p> |
- | <div id="project-s5-p5" class="pimg"><p class="imgcap"><b>Figure | + | <div id="project-s5-p5" class="pimg"><p class="imgcap"><b>Figure 30.</b>Isobutanol production through consolidated bioprocessing(CBP). There’re 2 types of <i>E.coli</i> in the reactor. One contains Cex-PgsA, which degrades hemicellulose and produces xylose. Another contains BBa_K887002, which turns xylose to isobutanol.</p></div> |
<p>Another advantage of using PgsA fusion enzyme is that it can lead isobutanol-producing enzymes to catalysis through consolidated bioprocessing(CBP) , the CBP in converting cellulose into isobutanol requires combinations of biological events(production of xylanases, hydrolysis of the polysaccharides in the biomass, temperature controlling, and production of isobutanol) in one reactor. CBP has gained recognition as a potential breakthrough for low-cost biomass processing. So, if we incubate <i>E.coli</i> with this mechanism with our isobutanol-synthesis <i>E.coli</i>, we can cost down the expenses of enzyme purification. Finally, the reactor as a whole will be more like a biofuel production line!</p> | <p>Another advantage of using PgsA fusion enzyme is that it can lead isobutanol-producing enzymes to catalysis through consolidated bioprocessing(CBP) , the CBP in converting cellulose into isobutanol requires combinations of biological events(production of xylanases, hydrolysis of the polysaccharides in the biomass, temperature controlling, and production of isobutanol) in one reactor. CBP has gained recognition as a potential breakthrough for low-cost biomass processing. So, if we incubate <i>E.coli</i> with this mechanism with our isobutanol-synthesis <i>E.coli</i>, we can cost down the expenses of enzyme purification. Finally, the reactor as a whole will be more like a biofuel production line!</p> | ||
<h2 id="project-s5-2-title" class="project-s-title"><a name="sub5-2"> </a> <span>Cellulose Degradation</span></h2> | <h2 id="project-s5-2-title" class="project-s-title"><a name="sub5-2"> </a> <span>Cellulose Degradation</span></h2> | ||
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So in the future work, we can use an INP-β-glucosidase fusion (<a href="http://partsregistry.org/wiki/index.php?title=Part:BBa_K523008" target="_blank" class="partlink">BBa_K523008</a> + <a href="http://partsregistry.org/wiki/index.php?title=Part:BBa_K523004" target="_blank" class="partlink">BBa_K523004</a>),which INP(<a href="http://partsregistry.org/wiki/index.php?title=Part:BBa_K523008" target="_blank" class="partlink">BBa_K523008</a>, based on <a href="http://partsregistry.org/wiki/index.php?title=Part:BBa_K265008" target="_blank" class="partlink">BBa_K265008</a>), a carrier for displaying enzymes on cell surface, can be used to carry proteins to the cell surface, by constructing <a href="http://partsregistry.org/wiki/index.php?title=Part:BBa_K523013" target="_blank" class="partlink">BBa_K523013</a> with a new β-glucosidase (bglX) BioBrick, <a href="http://partsregistry.org/wiki/index.php?title=Part:BBa_K523002" target="_blank" class="partlink">BBa_K523002</a>.</p> | So in the future work, we can use an INP-β-glucosidase fusion (<a href="http://partsregistry.org/wiki/index.php?title=Part:BBa_K523008" target="_blank" class="partlink">BBa_K523008</a> + <a href="http://partsregistry.org/wiki/index.php?title=Part:BBa_K523004" target="_blank" class="partlink">BBa_K523004</a>),which INP(<a href="http://partsregistry.org/wiki/index.php?title=Part:BBa_K523008" target="_blank" class="partlink">BBa_K523008</a>, based on <a href="http://partsregistry.org/wiki/index.php?title=Part:BBa_K265008" target="_blank" class="partlink">BBa_K265008</a>), a carrier for displaying enzymes on cell surface, can be used to carry proteins to the cell surface, by constructing <a href="http://partsregistry.org/wiki/index.php?title=Part:BBa_K523013" target="_blank" class="partlink">BBa_K523013</a> with a new β-glucosidase (bglX) BioBrick, <a href="http://partsregistry.org/wiki/index.php?title=Part:BBa_K523002" target="_blank" class="partlink">BBa_K523002</a>.</p> | ||
<h2 id="project-s5-3-title" class="project-s-title"><a name="sub5-3"> </a> <span>Biofuel Industry</span></h2> | <h2 id="project-s5-3-title" class="project-s-title"><a name="sub5-3"> </a> <span>Biofuel Industry</span></h2> | ||
- | <div id="project-s5-p3" class="pimg"><p class="imgcap"><b>Figure | + | <div id="project-s5-p3" class="pimg"><p class="imgcap"><b>Figure 30.</b>We hope to make an automatic control instrument in the future.</p></div> |
<p>Next, we will focus on researching the reaction rate, intermediate, and by-products of mechanisms. For example, the retention time for producing a certain concentration of 2-ketoisovalerate per 300 ml culture medium under different processing parameters!</p> | <p>Next, we will focus on researching the reaction rate, intermediate, and by-products of mechanisms. For example, the retention time for producing a certain concentration of 2-ketoisovalerate per 300 ml culture medium under different processing parameters!</p> | ||
<p>With the data, we can optimize the Eco-line economic justification; design the flow rate, vessel capacity, the driving equipment and instrumentation for totally auto-controlled system. Thus, we can build a manufacturing automation technology to produce isobutanol inexhaustibly.</p> | <p>With the data, we can optimize the Eco-line economic justification; design the flow rate, vessel capacity, the driving equipment and instrumentation for totally auto-controlled system. Thus, we can build a manufacturing automation technology to produce isobutanol inexhaustibly.</p> | ||
- | <div id="project-s5-p4" class="pimg"><p class="imgcap"><b>Figure | + | <div id="project-s5-p4" class="pimg"><p class="imgcap"><b>Figure 31.</b>The primary thought about our project on an industrial scale.</p></div> |
<p>Furthermore, we wish we could apply our project in commercial way some other day.<br> | <p>Furthermore, we wish we could apply our project in commercial way some other day.<br> | ||
We use the cellulase to produce xylose as ingredient(cheaper resource of raw material) in the first drum (preparation stage); The biosynthetic production of isobutanol generated on our project pre-reactor and reactor (reaction stage, R-301& R-302); The last section is to purify isobutanol by azeotropic distillation (separation stage, T-401, D-401& D-402). Hopefully the enormous production could be an alternative of gasoline for future green life.</p> | We use the cellulase to produce xylose as ingredient(cheaper resource of raw material) in the first drum (preparation stage); The biosynthetic production of isobutanol generated on our project pre-reactor and reactor (reaction stage, R-301& R-302); The last section is to purify isobutanol by azeotropic distillation (separation stage, T-401, D-401& D-402). Hopefully the enormous production could be an alternative of gasoline for future green life.</p> |
Latest revision as of 21:05, 26 October 2012
Future works
Cellulase experiment
In order to realize our idea of changing agricultural waste into biofuel, we figured that we could try to obtain glucose from cellulose by cellulase. This simple idea could be carried out by several procedures. First, we did a pre-experiment by using quantitative filter paper (Advantec) as cellulose source which was made with highest quality alpha cotton cellulose, and was ashless(<0.1%). We cut the filter paper into the size of 0.5 cm square. Next, we weighed and put 3 grams of the filter paper chips in a 50ml centrifuge tube filled up to 50ml with 0.1M Na-citrate (ph5.3). We then added 375mg cellulase, which came from Trichoderma reesei (Sigma-Aldrich) and put it in 40℃ incubation(200rpm) for 96 hours. After that, we could get milk-like filter paper mash. Finally, 3.6% of glucose was measured by doing DNS assay!
The next challenge would be use E. coli we modified to yield isobutanol with the glucose medium made by cellulose. We filtered and transferred the glucose medium to another flask, and added our M9T9 formula except of adding glucose into it. Then we inoculated E. coli in it for 24 to 42 hours, 42℃, 200rpm. The GC result of the isobutanol yield was 25ppm. Though it wasn’t prominent, it proved that the whole procedures (from cellulose degradation to isobutanol production) were practical. However, we could infer that underneath the toxicity tolerance, we still might acquire isobutanol as much as possible. So we must modify every procedure to enhance the yield of isobutanol. In the future, we will try rice stalks from a farm as cellulose source, hoping that the outcome will give everyone a big surprise!
Figure 27.The simplificative procedures of degrading cellulose to glucose, and then E. coli utilized it to yield isobutanol.
Ingredient Production
Figure 28.Cell-surface display of Cex by means of PgsA anchor protein
Figure 29.
In order to realize our idea to change trash into fuel, we did some research. Therefore, what we have to do is to figure out how to degrade the cellulose. First, we want to get xylose from cellulose through xylanase. Xylanase is a class of enzyme which degrades the linear polysaccharide beta-1,4-xylan into xylose, thus breaks down hemicellulose, one of the major components of plant cell walls. Xylose is a good carbon source. As such, xylanase plays a major role in micro-organisms thriving on plant sources (mammals, conversely, do not produce xylanase).
According to the Journal of Applied Microbiology ( Y.P. Chen et al. 2011), the cell-surface display of Cex, which encodes xylanase from Cellulomonas fimi, was constructed on E.coli using PgsA as the anchor protein.In Figure 29, it shows that Cex do have the activity to catalyze xylan into xylose.
Figure 30.Isobutanol production through consolidated bioprocessing(CBP). There’re 2 types of E.coli in the reactor. One contains Cex-PgsA, which degrades hemicellulose and produces xylose. Another contains BBa_K887002, which turns xylose to isobutanol.
Another advantage of using PgsA fusion enzyme is that it can lead isobutanol-producing enzymes to catalysis through consolidated bioprocessing(CBP) , the CBP in converting cellulose into isobutanol requires combinations of biological events(production of xylanases, hydrolysis of the polysaccharides in the biomass, temperature controlling, and production of isobutanol) in one reactor. CBP has gained recognition as a potential breakthrough for low-cost biomass processing. So, if we incubate E.coli with this mechanism with our isobutanol-synthesis E.coli, we can cost down the expenses of enzyme purification. Finally, the reactor as a whole will be more like a biofuel production line!
Cellulose Degradation
Furthermore, we found another potential way on coverting cellulose into glucose by utilizing the Biobrick from 2008 and 2011 Edinburgh igem team. Edinburgh2008 iGEM team found out three Coding parts on cellulose degradation,cenA: BBa_K118023 (endoglucanase), cex: BBa_K118022 (exoglucanase), and bglX: BBa_K118028 (beta glucosidase). Edinburgh2011 iGEM team able to display bglX (a cryptic E.coli β-glucosidase gene) and the exoglucanase cex on cell surface. Therefore, through MUG assay and MUC assay, bglX and cex can be proven its effect. Because bglX is capable of degrading the substrate MUG, which has a β (1→4) bond, similar to that of cellobiose. So in the future work, we can use an INP-β-glucosidase fusion (BBa_K523008 + BBa_K523004),which INP(BBa_K523008, based on BBa_K265008), a carrier for displaying enzymes on cell surface, can be used to carry proteins to the cell surface, by constructing BBa_K523013 with a new β-glucosidase (bglX) BioBrick, BBa_K523002.
Biofuel Industry
Figure 30.We hope to make an automatic control instrument in the future.
Next, we will focus on researching the reaction rate, intermediate, and by-products of mechanisms. For example, the retention time for producing a certain concentration of 2-ketoisovalerate per 300 ml culture medium under different processing parameters!
With the data, we can optimize the Eco-line economic justification; design the flow rate, vessel capacity, the driving equipment and instrumentation for totally auto-controlled system. Thus, we can build a manufacturing automation technology to produce isobutanol inexhaustibly.
Figure 31.The primary thought about our project on an industrial scale.
Furthermore, we wish we could apply our project in commercial way some other day.
We use the cellulase to produce xylose as ingredient(cheaper resource of raw material) in the first drum (preparation stage); The biosynthetic production of isobutanol generated on our project pre-reactor and reactor (reaction stage, R-301& R-302); The last section is to purify isobutanol by azeotropic distillation (separation stage, T-401, D-401& D-402). Hopefully the enormous production could be an alternative of gasoline for future green life.
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