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1. For passive diffusion:</br> | 1. For passive diffusion:</br> | ||
− | <img src="https://static.igem.org/mediawiki/2016/3/3d/T--Vilnius-Lithuania--mod1.png" class="image-box" style="height: | + | <img src="https://static.igem.org/mediawiki/2016/3/3d/T--Vilnius-Lithuania--mod1.png" class="image-box" style="height: 100px; width: 30%"> </br> |
2. For facilitated diffusion: </br> | 2. For facilitated diffusion: </br> | ||
− | <img src="https://static.igem.org/mediawiki/2016/3/30/T--Vilnius-Lithuania--mod2.png" class="image-box" style="height: | + | <img src="https://static.igem.org/mediawiki/2016/3/30/T--Vilnius-Lithuania--mod2.png" class="image-box" style="height: 100px; width: 30%"> </br> |
The PheP coding genes are expressed constantly, reaching a steady state of the transporter in the membrane, which can be described by the following equation: | The PheP coding genes are expressed constantly, reaching a steady state of the transporter in the membrane, which can be described by the following equation: | ||
</br> | </br> | ||
− | <img src="https://static.igem.org/mediawiki/2016/b/b0/T--Vilnius-Lithuania--mod3.png" class="image-box" style="height: | + | <img src="https://static.igem.org/mediawiki/2016/b/b0/T--Vilnius-Lithuania--mod3.png" class="image-box" style="height: 200px; width: 30%"> </br> |
where α is the translation rate, β is the degradation and dilution rate of PheP, K is the transcription rate and δ is the degradation and dilution rate of mRNA. </br> | where α is the translation rate, β is the degradation and dilution rate of PheP, K is the transcription rate and δ is the degradation and dilution rate of mRNA. </br> | ||
Together, PheP expression rate and the activity of the transporter dictates the rate of facilitated transport into the cells. Later, by combining both passive and facilitated diffusion rate equations we can determine the rate of phenylalanine uptake.</br> | Together, PheP expression rate and the activity of the transporter dictates the rate of facilitated transport into the cells. Later, by combining both passive and facilitated diffusion rate equations we can determine the rate of phenylalanine uptake.</br> | ||
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The rate of convertion of Phenylalanine to TCA for different concentrations of PAL can be calculated from the following equation:</br> | The rate of convertion of Phenylalanine to TCA for different concentrations of PAL can be calculated from the following equation:</br> | ||
− | <img src="https://static.igem.org/mediawiki/2016/9/92/T--Vilnius-Lithuania--mod4.png" class="image-box" style="height: | + | <img src="https://static.igem.org/mediawiki/2016/9/92/T--Vilnius-Lithuania--mod4.png" class="image-box" style="height: 100px; width: 30%"> </br> |
We have carried out experiments to acquire some of the constants regarding our model (see wet lab page). If the expression rate and activity of PAL and phenylalanine diffusion rate is known, the process of phenylalanine hydrolysis inside the cell can be discribed by the following equations: </br> | We have carried out experiments to acquire some of the constants regarding our model (see wet lab page). If the expression rate and activity of PAL and phenylalanine diffusion rate is known, the process of phenylalanine hydrolysis inside the cell can be discribed by the following equations: </br> | ||
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We first simulated the break down of phenylalanine by PAL being expressed within the cell. The steady state concentration of PAL inside the cell is assumed to be in the range between 10-4 and 10-7 M. Here the four versions of graphs for each magnitude of PheP steady state concentration, ranging from 10-3 to 10-6 M are shown. The amounts of phenylalanine inside the cell, outside the cell, and the amount of trans-cynnamic acid (in or out?) are presented in the graphs. </br> | We first simulated the break down of phenylalanine by PAL being expressed within the cell. The steady state concentration of PAL inside the cell is assumed to be in the range between 10-4 and 10-7 M. Here the four versions of graphs for each magnitude of PheP steady state concentration, ranging from 10-3 to 10-6 M are shown. The amounts of phenylalanine inside the cell, outside the cell, and the amount of trans-cynnamic acid (in or out?) are presented in the graphs. </br> | ||
− | <img src="https://static.igem.org/mediawiki/2016/1/1f/T--Vilnius-Lithuania--mod6.png" class="image-box" style="height: | + | <img src="https://static.igem.org/mediawiki/2016/1/1f/T--Vilnius-Lithuania--mod6.png" class="image-box" style="min-height: 700px; width: 70%"> |
<h1 class="Raleway" style="text-align:center;">Discussion</h1> | <h1 class="Raleway" style="text-align:center;">Discussion</h1> |
Revision as of 22:25, 18 October 2016
Modelling
Mathematical modelling of the natural systems is often a necessity in understanding the probabilities of certain outcomes or dependencies of certain factors on the whole system in experimental science. Such models have a vast application, as they can provide the information based on the interaction of multiple systems, which cannot be achieved in the laboratory conditions. It is essential, that mathematical modelling is of crucial importance in the field of synthetis biology, as it helps to predict all the possible outcomes of a particular novel approach. Mathematical models are useful not only in describing natural systems, but also in predicting the response of a system at various conditions. Here we present the mathematical and kinetic model of a part of our engineered system: a bacteria, which expresses a recombinant enzyme PAL (phenylalanine ammonia lyase) and phenylalanine channels. The purpose of the model is to define the efficiency of the system and the limits of its performance as it is crucial to ensure that the approach is prospective and liable.