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<div id="Carbon_fixation"> | <div id="Carbon_fixation"> | ||
− | < | + | <div class="row"> |
− | + | <a class="btn col-md-12" data-toggle="collapse" href="#Estimation_Carbon_fixation" role="button" aria-expanded="false" aria-controls="multiCollapseExample1"> | |
− | <div id=" | + | Estimation of the amount of the carbon fixation |
− | <p class="pcontent"> | + | <i class="fa fa-arrow-down fa-10" aria-hidden="true"></i> |
− | + | </a> | |
− | + | </div> | |
− | + | <div class="collapse multi-collapse" id="Estimation_Carbon_fixation"> | |
− | + | <div class="card card-body"> | |
− | + | <div id="pt"> | |
− | + | <p class="pcontent"> | |
+ | To find out how much and how efficient genetically engineered <i>E. coli</i> | ||
+ | can fix | ||
+ | carbon dioxide, we use the material balance concept to evaluate the | ||
+ | heterotrophic CO<sub>2</sub> fixation process. Consider a system composed of a | ||
+ | single | ||
+ | component, the general material balance can be written as: | ||
− | + | $${\{Input\ to\ the\ system\}\ –\ \{Output\ to\ the\ system\}\ =\ | |
− | + | \{Accumulation\ in\ the\ syste\}}$$ | |
− | + | A system can be defined as an arbitrary portion of a process considered for | |
− | + | analysis, in which in this case, is an engineered carbon capturing <i>E. coli</i>. | |
− | + | </p> | |
− | + | </div> | |
− | + | <img class="contentimg" src=""> | |
− | + | <div id="pt"> | |
− | + | <p class="pcontent"> | |
− | + | The engineered <i>E. coli</i> BL21 (DE3) are cultured in M9 medium with formula | |
− | + | adjusted so that xylose is the sole carbon source. The aforementioned M9 Medium | |
− | + | contains | |
− | + | 0.4% xylose and 1/1000 LB medium (the carbon consumed from LB medium can be | |
− | + | ignored). By applying the law of conservation of mass, which states that mass | |
− | + | may neither be created nor destroyed, the material balance for carbon in an | |
− | + | engineered <i>E. coli</i> may simply be written as | |
− | + | $${\{C_{CO_2}\ in\}\ +\ \{C_{xylose}\}\ -\ \{C_{CO_2}\ out\}\ -\ \{C_{waste}\}\ | |
− | + | =\ \{C_{biomass}\}...(1)}$$ | |
− | + | Considering the difficulties in measuring carbon in <i>E. coli</i> metabolic | |
− | + | waste and | |
− | + | that C<sub>waste</sub> would be positive, the equation reduces to | |
− | + | $${\{C_{CO_2}\ in\}\ -\ \{C_{CO_2}\ out\}\ ≥\ \{C_{biomass}\}\ -\ | |
− | + | \{C_{xylose}\}...(2)}$$ | |
− | + | Let {C<sub>CO<sub>2</sub></sub> net}= {C<sub>CO<sub>2</sub></sub> in} - {C<sub>CO<sub>2</sub></sub> | |
− | + | out}, equation (2) further simplifies to | |
− | + | $${\{C_{CO_2}\ net\}\ ≥\ \{C_{biomass}\}\ -\ \{C_{xylose}\}...(3)}$$ | |
− | + | If C<sub>waste</sub> is very small and negligible, we can obtain the net amount | |
− | + | of carbon | |
− | + | dioxide fixed over time. If, on the contrary, C<sub>waste</sub> cannot be | |
− | + | neglected, | |
− | + | equation (3) allows us to estimate the minimum net amount of carbon dioxide | |
− | + | fixed. | |
− | + | </p> | |
− | + | <p class="pcontent"> | |
− | + | C<sub>biomass</sub> can be calculate by multiplying O.D. 600 to DCW and mass | |
− | + | percent of carbon in <i>E. coli</i> biomass. The O.D. 600 of engineered <i>E. | |
− | + | coli</i> is | |
− | + | measured after a 12-hour cultivation and the result obtained is 0.45O.D. . Yin | |
− | + | Li et al. reported that dry cell weight (DCW) of <i>E. coli</i> is | |
− | + | $${0.35g\over L ∙ 𝑂.𝐷. 600}$$ | |
− | + | , determined by experiment. <i>E. coli</i> biomass contains 48% of carbon by | |
− | + | mass. | |
− | + | $${C_{biomass}\ =\ 0.45\ ×\ 0.35\ ×\ 48\%}$$ | |
− | + | $${=\ 0.0756\ g/L}$$ | |
− | + | </p> | |
− | + | <p class="pcontent"> | |
− | + | On the other hand, C<sub>xylose</sub> can be calculated by multiplying the | |
− | + | amount of | |
− | + | xylose consumed per unit volume of broth to the mass percent of carbon in | |
− | + | xylose. Xylose consumption is calculated by using a DNS kit that measures the | |
− | + | concentration of reducing sugar and the result obtained is 0.172324g of xylose | |
− | + | consumed per liter of M9 medium. Carbon mass percentage of xylose | |
− | + | is 40%. | |
− | + | $${C_{xylose}\ =\ 0.172324\ ×\ 40\%\ =\ 0.0689296\ g/L}$$ | |
− | + | By equation (3) | |
− | + | $${C_{CO_2\ net}\ =\ 0.0756\ -\ 0.0689296}$$ | |
− | + | $${=\ 0.0066704\ g/L}$$ | |
− | + | Since the <i>E. coli</i> has been cultured for 12 hours, we can calculate the | |
− | + | rate of | |
− | + | carbon fixation by | |
− | + | $${Rate\ of\ carbon\ fixation\ =\ {𝐶_{𝐶𝑂_2\ 𝑛𝑒𝑡}\over 12}}$$ | |
− | + | $${=\ {0.0066704\over 12}}$$ | |
− | + | $${=\ 0.5558\ {mg\over L ∙hr}}$$ | |
− | + | To find out how much carbon in biomass comes from the carbon in CO<sub>2</sub> | |
− | + | captured by | |
− | + | the heterotrophic microbes, divide the net amount of carbon fixed by the mass | |
− | + | percent of carbon in biomass. | |
− | + | ||
− | + | ||
− | + | ||
− | + | ||
− | + | ||
− | + | ||
+ | $${Ratio\ of\ carbon\ in\ CO_2\ fixed\ to\ carbon\ in\ biomass\ =\ | ||
+ | {0.0066704\over 0.0756}}$$ | ||
+ | $${=\ 8.82\%}$$ | ||
+ | </p> | ||
+ | </div> | ||
+ | </div> | ||
</div> | </div> | ||
− | |||
− | |||
</div> | </div> | ||
− | |||
<div id="pH_Senesing"> | <div id="pH_Senesing"> | ||
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<p class="pcontent"> | <p class="pcontent"> | ||
− | Fig | + | Fig 20. The data shows the fluorescence intensity (absorbance: 485 nm, |
excitation: 535 nm) expressed by P<sub>gadA</sub> in different pH. | excitation: 535 nm) expressed by P<sub>gadA</sub> in different pH. | ||
</p> | </p> |
Revision as of 16:01, 17 October 2018
Results