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<div class="righttitle"> | <div class="righttitle"> | ||
− | <h6 class="subtitle"> | + | <h6 class="subtitle">From Bench To Business</h6> |
</div> | </div> | ||
<div class="navbar-example"> | <div class="navbar-example"> | ||
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<p class="pcontent">The two questions above were the main concern of CSC. Basically, the best condition for engineered <i>E. coli</i> to capture CO<sub>2</sub> have to be lower, without too much SOx and NOx particles. | <p class="pcontent">The two questions above were the main concern of CSC. Basically, the best condition for engineered <i>E. coli</i> to capture CO<sub>2</sub> have to be lower, without too much SOx and NOx particles. | ||
However, we won’t be able to provide an ideal culture condition in industrial application. | However, we won’t be able to provide an ideal culture condition in industrial application. | ||
− | After researching the tolerance of <i>E. coli</i>, we concluded that <i>E. coli</i> is possible to survive in factory condition while the concentration of SOx and NOx were much lower than CO<sub>2</sub>. Besides, we will dilute the concentration with gas that the small fraction of SOx NOx can only effect the expression of<i>E. coli</i>. | + | After researching the tolerance of <i>E. coli</i>, we concluded that <i>E. coli</i> is possible to survive in factory condition while the concentration of SOx and NOx were much lower than CO<sub>2</sub>. Besides, we will dilute the concentration with gas that the small fraction of SOx NOx can only effect the expression of <i>E. coli</i>. |
In other words, it may not capture as much CO<sub>2</sub> as culture in the lab. | In other words, it may not capture as much CO<sub>2</sub> as culture in the lab. | ||
</p> | </p> | ||
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That’s the point that ITRI will adopt our project into their lab. | That’s the point that ITRI will adopt our project into their lab. | ||
</p> | </p> | ||
− | <p class="pcontent">Dr. | + | <p class="pcontent">Dr. Shen suggested us to think more about the bioproduct after our |
<i>E. coli</i> uptake CO<sub>2</sub>. We can easily transgene <i>E. coli</i> | <i>E. coli</i> uptake CO<sub>2</sub>. We can easily transgene <i>E. coli</i> | ||
to let <i>E. coli</i> metabolized CO<sub>2</sub> and produce amino acid. | to let <i>E. coli</i> metabolized CO<sub>2</sub> and produce amino acid. | ||
The highest value of bioproduct will be the health food. | The highest value of bioproduct will be the health food. | ||
However, we could hardly make the health food which made from industrial flue gas into the market. There are still many valuable products we can achieve with less limitation when applying to the market, | However, we could hardly make the health food which made from industrial flue gas into the market. There are still many valuable products we can achieve with less limitation when applying to the market, | ||
− | such as electronic material solvent, biocytoculture, agricultural | + | such as electronic material solvent, biocytoculture, agricultural chemicals, etc. |
Besides, the last choice will be biofuel. We should try to reuse our product again and | Besides, the last choice will be biofuel. We should try to reuse our product again and | ||
again to maximize the value before converting it into biofuel. | again to maximize the value before converting it into biofuel. | ||
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<h5 class="boldh5">Process</h5> | <h5 class="boldh5">Process</h5> | ||
<p class="pcontent">In order to obtain more information about CO<sub>2</sub>. | <p class="pcontent">In order to obtain more information about CO<sub>2</sub>. | ||
− | biofixation, we visited microalgae cultivation in An- | + | biofixation, we visited microalgae cultivation in An-nan Campus of National Cheng Kung University |
which is a biofixation project managed by Professor Jo-Shu Chang. | which is a biofixation project managed by Professor Jo-Shu Chang. | ||
The research fellows showed us different scale of microalgae culture system, | The research fellows showed us different scale of microalgae culture system, | ||
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we calculate how much the cost it would be when capturing 1 ton of CO<sub>2</sub>. | we calculate how much the cost it would be when capturing 1 ton of CO<sub>2</sub>. | ||
</p> | </p> | ||
+ | <br> | ||
<h5 class="boldh5">Volume</h5> | <h5 class="boldh5">Volume</h5> | ||
− | <p class="pcenter" id="closep"> Table 1 Volume required in | + | <p class="pcenter" id="closep"> Table 1 Volume required in utilizing 1 ton of CO<sub>2</sub></p> |
<div class="card card-body"> | <div class="card card-body"> | ||
<table> | <table> | ||
<tr> | <tr> | ||
<th colspan="1">Organisms</th> | <th colspan="1">Organisms</th> | ||
− | <th colspan="1">CO<sub>2</sub>- | + | <th colspan="1">CO<sub>2</sub>-utilization rate (mg/L*hr)</th> |
<th colspan="1">Biomass concentration (gDCW/L)</th> | <th colspan="1">Biomass concentration (gDCW/L)</th> | ||
− | <th colspan="1">Specific CO<sub>2</sub>- | + | <th colspan="1">Specific CO<sub>2</sub>-utilization rate</th> |
<th colspan="1">Volume requiredd (L)</th> | <th colspan="1">Volume requiredd (L)</th> | ||
</tr> | </tr> | ||
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</div> | </div> | ||
<p class="pcenter">Fig 6. Different volume required between micralgae and engineered <i>E. coli</i> </p> | <p class="pcenter">Fig 6. Different volume required between micralgae and engineered <i>E. coli</i> </p> | ||
+ | <p class="pcontent"> | ||
+ | For capturing 1kg of CO<sub>2</sub> in one hour, 51000 L is required with engineered <i>E. coli</i> carbon utilization. It seems that the difference volume required for utilizing same amount of CO<sub>2</sub> is disadvantage of <i>E. coli</i> carbon utilization system. At this situation, we have to look into the design of the different bioreactor. For microalgae culture, it requires a large surface area to increase light intensity. As usual, the height of the microalgae culture pond cannot exceed 0.5 m. In other words, we have to build a 7 m diameter culture pond with the volume of 19000L. In constrast, engineered <i>E. coli</i> is not limited by light. The bioreactor of <i>E. coli</i> can be built with any height in the indoor or outdoor. To scale up the bioreactor, a 5.8 m diameted with 1.9 m height equals to 51000 L which has lower floor area required. | ||
+ | </p> | ||
+ | <p class="pcontent">As a result,the bioreactor of engineered <i>E. coli</i> can save more than 30% floor area compared with micoralgae culture pond. Take the floor area of Taiwan as an example, we can build 94 billions of microalgae culture pond to uilize 10% of annual emission with 12 operation hours. However, 1 over 3 of floor area will be save if we replace them with <i>E. coli</i> bioreactor. <i>E. coli</i> bioreactor is more flexible on spacing using, and is less sensitive to weather effect. | ||
+ | </p> | ||
+ | <br> | ||
</div> | </div> | ||
<h5 class="boldh5">Cost</h5> | <h5 class="boldh5">Cost</h5> | ||
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<tr> | <tr> | ||
<td colspan="1">CO<sub>2</sub> utilizing rate</td> | <td colspan="1">CO<sub>2</sub> utilizing rate</td> | ||
− | <td colspan="1">250 g/m | + | <td colspan="1">250 g/m<sup>3</sup>/day</td> |
<td colspan="1">19.6 mg/g (DRY cell weight)</td> | <td colspan="1">19.6 mg/g (DRY cell weight)</td> | ||
</tr> | </tr> | ||
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<tr> | <tr> | ||
<th colspan="1">Industrial</th> | <th colspan="1">Industrial</th> | ||
+ | <th colspan="1">Annual emission</th> | ||
<th colspan="1">1 % of CO<sub>2</sub> emission per hour</th> | <th colspan="1">1 % of CO<sub>2</sub> emission per hour</th> | ||
<th colspan="1">Number of required device</th> | <th colspan="1">Number of required device</th> | ||
<th colspan="1">Area required</th> | <th colspan="1">Area required</th> | ||
− | <th colspan="1">Operation cost</th> | + | <th colspan="1">Operation cost (USD)</th> |
− | + | ||
</tr> | </tr> | ||
<tr> | <tr> | ||
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<td colspan="1">4555</td> | <td colspan="1">4555</td> | ||
<td colspan="1">11.3875 hectare</td> | <td colspan="1">11.3875 hectare</td> | ||
− | <td colspan="1">150.4 thousands | + | <td colspan="1">150.4 thousands </td> |
</tr> | </tr> | ||
<tr> | <tr> | ||
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<td colspan="1">537</td> | <td colspan="1">537</td> | ||
<td colspan="1">1.34 hectare</td> | <td colspan="1">1.34 hectare</td> | ||
− | <td colspan="1">17.3 thousands | + | <td colspan="1">17.3 thousands </td> |
</tr> | </tr> | ||
<tr> | <tr> | ||
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<td colspan="1">29</td> | <td colspan="1">29</td> | ||
<td colspan="1">0.0713 hectare</td> | <td colspan="1">0.0713 hectare</td> | ||
− | <td colspan="1">1 thousands | + | <td colspan="1">1 thousands </td> |
</tr> | </tr> | ||
</table> | </table> | ||
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for 1 % of industrial CO<sub>2</sub> emission. | for 1 % of industrial CO<sub>2</sub> emission. | ||
</p> | </p> | ||
− | + | <br> | |
<h5 class="boldh5">Energy consumption</h5> | <h5 class="boldh5">Energy consumption</h5> | ||
<p class="pcontent">Our bioreactor applies in the industry, | <p class="pcontent">Our bioreactor applies in the industry, |
Latest revision as of 13:51, 3 November 2018