PedroAlmeida (Talk | contribs) |
PedroAlmeida (Talk | contribs) |
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{{USP-EEL-Brazil}} | {{USP-EEL-Brazil}} | ||
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<html> | <html> | ||
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</div> | </div> | ||
<img style="text-align:center;"src="https://static.igem.org/mediawiki/2018/0/08/T--USP-EEL-Brazil--eembbrazil.jpg"width=100% > | <img style="text-align:center;"src="https://static.igem.org/mediawiki/2018/0/08/T--USP-EEL-Brazil--eembbrazil.jpg"width=100% > | ||
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<div class="column full_size"> | <div class="column full_size"> | ||
− | < | + | <button class="tablink" onclick="openPage('Reactors', this, 'color')" id="">Reactors</button> |
− | < | + | <button class="tablink" onclick="openPage('DMT', this, '')" >Different Mediators Test</button> |
+ | <button class="tablink" onclick="openPage('OPT', this, '')">Optimun pH and Temperature</button> | ||
+ | <button class="tablink" onclick="openPage('SD', this, '')">Substrate Degradation</button> | ||
− | < | + | <div id="Reactors" class="tabcontent"> |
− | + | <h3 style="margin-left:10%;">Reactors</h3> | |
− | </p> | + | <p>To understand how our system would react to diferents inputs first we need to estabelecer um tipo de reactor.</p> |
+ | <h3>BATCH REACTORS </h3> | ||
− | </ | + | <p>For batch reactors we used the mass balance as the described by equation (5), when the data were based on removal ratio. Whenever the data was given in substrate concentration, the ordinary Michaelis-Menten was used, as above on equation (6)</p> |
+ | <img src="https://static.igem.org/mediawiki/2018/9/97/T--USP-EEL-Brazil--Equa%C3%A7%C3%A3o6.jpeg"> | ||
+ | <p>And the boundary condition considered was that at t=0, the removal was 0 too. </p> | ||
+ | <p>Using the software Wolfram Mathemathica, a non linear model was created to fit the data and find the km and the vmax¬¬. </p> | ||
+ | <h3>FED-BATCH REACTORS </h3> | ||
+ | <h3>ENZYMATIC MEMBRANE REACTOR </h3> | ||
− | <div | + | </div> |
− | + | ||
− | + | ||
− | + | ||
− | + | ||
− | + | ||
− | + | ||
+ | <div id="DMT" class="tabcontent"> | ||
+ | <h3>Different Mediators Test</h3> | ||
+ | <p>Some news this fine day!</p> | ||
+ | |||
</div> | </div> | ||
− | <div | + | <div id="OPT" class="tabcontent"> |
− | + | <h3>Optimun pH and Temperature</h3> | |
− | <h3> | + | <p>Get in touch, or swing by for a cup of coffee.</p> |
− | < | + | |
− | + | ||
− | + | ||
− | + | ||
− | + | ||
</div> | </div> | ||
+ | |||
+ | <div id="SD" class="tabcontent"> | ||
+ | <h3>Substrate Degradation</h3> | ||
+ | <p>Get in touch, or swing by for a cup of coffee.</p> | ||
+ | |||
+ | |||
+ | |||
</div> | </div> | ||
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</html> | </html> | ||
+ | |||
+ | {{USP-EEL-Brazil/footer}} |
Revision as of 12:04, 5 October 2018
Reactors
To understand how our system would react to diferents inputs first we need to estabelecer um tipo de reactor.
BATCH REACTORS
For batch reactors we used the mass balance as the described by equation (5), when the data were based on removal ratio. Whenever the data was given in substrate concentration, the ordinary Michaelis-Menten was used, as above on equation (6)
And the boundary condition considered was that at t=0, the removal was 0 too.
Using the software Wolfram Mathemathica, a non linear model was created to fit the data and find the km and the vmax¬¬.
FED-BATCH REACTORS
ENZYMATIC MEMBRANE REACTOR
Different Mediators Test
Some news this fine day!
Optimun pH and Temperature
Get in touch, or swing by for a cup of coffee.
Substrate Degradation
Get in touch, or swing by for a cup of coffee.