Difference between revisions of "Team:IIT Kanpur/TestPage"

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<h1 class="subtitle text-center">Model: Background</h1>
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<p>Simple growth models of bacterial populations are based on two interdependent factors: the concentration of bacteria (<em>X</em>) and concentration of a growth limiting substrate (<em>S</em>) (Monod, 1949)(Figure 1A). Bacteria-phage model can be considered as an extended version of a simple model that includes a third dynamic factor: the phage (<em>P</em>)(Figure 1B). The first model was presented as a set of ordinary differential equations (ODDs) by Campbell (1961). In this model, the change rate of the bacterial population is dependent on the concentration of bacteria and substrate, as well as the rate of phage-induced lysis, which in turn is also dependent on the bacterial concentration (Figure 1B).</p>
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<div class="div-fig" style="width: 800px;">
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<p><strong>Figure 1.</strong> Schematic diagram showing interactions in (A) a two-factor model containing bacteria and substrate, and (B) an extended three-factor model also containing a lytic phage as proposed by Campbell (1961). Taken from Krysiak-Baltyn <em>et al.</em> (2016).</p>
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<h2>Lytic and lysogenic cycles of phage replication</h2>
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<p>In order to model phage-bacteria interactions it is important to understand a step-by-step process of phage infection. Figure 2 shows a lytic life cycle of a lytic phage in a simplified five-step process: from diffusion and attachment to the bacterial cell membrane to cell lysis. The lysogenic life cycle of a temperate phage starts in a similar way to the lytic phage, however following the infection the phage genome either integrates itself into the host genome (&lambda; phage) or forms a circularized plasmid-like structure (P1 phage)(Howard-Varona <em>et al.</em>, 2017). The phage genome that has been integrated into the bacterial chromosome is also known as a prophage. Once integrated, temperate phage replicates together with the bacterial genome upon bacterial cell division. However, either spontaneously at low frequency (10-8&ndash;10-5) or due to unfavourable stress conditions, such as exposure to UV light, antibiotics, hydrogen peroxide and changes in temperature, nutrients or pH, can lead to a phage induction. Once induced, lytic-lysogenic switch gets activated leading to expression of viral genes, a switch to lytic life cycle and cell lysis.</p>
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<img src="https://static.igem.org/mediawiki/2017/c/cf/T--Edinburgh_OG--model_bg_Picture2.png">
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<p><strong>Figure 2.</strong> A simplified diagram of lytic and lysogenic life cycles of the phage. (1) diffusion of the phage particle to the bacterial cell; (2) phage attachment to the receptors along the bacterial membrane; (3) injection of phage genome into the cell; (3a) replication via cell division during lysogenic cycle; (3b) induction of lytic cycle; (4) replication of phage genome and assembly of capsid proteins; (5) cell lysis followed by the release of phage particles outside the cell. The burst size (<em>b</em>) shows the number of released phage particles. Adapted from Krysiak-Baltyn <em>et al. </em>(2016).</p>
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<table>
        <h1 class="Up">Modelling</h1>
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<tbody>
        <p class="Up">Britain's Next Top Model</p>
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<tr>
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<td>
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<p><em>b</em></p>
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</td>
      <p class="lead Up">
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        Our team produced two main models to inform on the design of our project and to simulate areas that we could not test practically. The ambitious nature of our project meant that there were a number of areas that can be supported by modelling, as we did
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<p>Burst size</p>
        not set out to have a fully working prototype pod over the short summer, and these models will be of use to any future work on our project. The modelling aspect of our project was also one of the most interdisciplinary, with the engineers working
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        with the biologists on a directly overlapping subject. This required a lot of learning on both sides, as well as compromises (with the engineers encountering just how limited biologists are by the vast unknown at the biochemical level, and the
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<td>
        biologists learning just how much engineers love numbers)!
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<p><em>P</em></p>
        <br>
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        <br>
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<td>
        <a href="https://github.com/BristolIGEM2017/modelling" target="_blank">
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<p>Concentration of phage</p>
          <p class="lead">Our code is on Github</p>
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<p><em>C</em></p>
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<td>
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<p>Carrying capacity</p>
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</td>
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<p><em>q</em></p>
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</td>
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<td>
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<p>Induction rate</p>
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<td>
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<p><em>D</em></p>
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</td>
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<td>
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<p>Dilution rate
</p>
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</td>
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<td>
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<p><em>S</em></p>
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</td>
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<td>
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<p>Concentration of substrate
</p>
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</td>
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<td>
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<p><em>d</em></p>
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</td>
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<td>
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<p>Rate of decay of cells or phages
</p>
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</td>
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<td>
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<p><em>T</em></p>
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</td>
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<td>
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<p>Latency time
</p>
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</td>
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<tr>
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<td>
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<p><em>K</em><sub><em>i</em></sub></p>
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</td>
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<td>
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<p>Adsorption rate of phages to bacteria</p>
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</td>
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<td>
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<p><em>X</em><sub><em>S</em></sub></p>
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</td>
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<td>
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<p>Concentration of susceptible bacteria (here antibiotic resistant bacteria)</p>
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</td>
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</tr>
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<td>
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<p><em>K</em><sub><em>m</em></sub></p>
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</td>
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<td>
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<p>Half-saturation constant
</p>
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</td>
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<td>
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<p><em>X</em><sub><em>I</em></sub></p>
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</td>
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<td>
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<p>Concentration of infected bacteria
</p>
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</td>
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<p><em>&mu;</em><sub><em>max</em></sub></p>
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<td>
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<p>Maximum specific growth rate</p>
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</td>
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<td>
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<p><em>Y</em></p>
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</td>
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<td>
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<p>Bacterial yield, or bacterial cells per unit substrate</p>
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</td>
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</tbody>
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</table>
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<p><strong>Table 1.</strong> Parameters used in models of populations of phage and bacteria.</p>
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<h2>Basic model</h2>
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<p>Modelling of the processes described in Figure 2. involves developing and solving expressions for the concentrations of phages, infected and non-infected bacteria as well as the substrate. The key parameters involved into equations are listed in Table 1. Following the approach documented in Campbell (1961), the rate of infection is proportional to the concentration of bacteria, lytic phage and the absorption rate (<em>K</em><em>i</em>). The latter is the rate at which phage particles attach to the bacterial surface and it is dependent on (1) the concentrations of both bacteria and phage, (2) the time required for diffusion and attachment of the phage, and (3) the number of phage particles, which upon attachment to the bacterial cell, do not lead to infection.</p>
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<div class="div-eq">
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<img src="https://static.igem.org/mediawiki/2017/3/32/T--Edinburgh_OG--model_bg_eq1.png">
  
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<p>Oppositely, the growth rate of phage population decreases due to attachment of phage particles onto bacterial cells:</p>
    <div class="row align-items-center justify-content-center col-md-12">
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<div class="div-eq">
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<img src="https://static.igem.org/mediawiki/2017/c/c4/T--Edinburgh_OG--model_bg_eq2.png">
        <a href="#singlecellmodel">
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          <p class="model-button">Single Cell<br>Model</p>
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<p>And increases due to cell lysis and release of newly produced phage particles:</p>
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<img src="https://static.igem.org/mediawiki/2017/f/f9/T--Edinburgh_OG--model_bg_eq3.png">
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<p>The <em>latency time </em>(<em>T</em>) is caused by the time delay between the infection and cell lysis (steps 3 and 5 in Figure 2).</p>
          <p class="model-button">Atmospheric Pollution Model</p>
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<p>The growth of bacterial population was represented as a logistic kinetic expression that is independent from the concentration of the growth limiting substrate, but dependent on the total <em>carrying capacity</em> (<em>C</em>) <em>i.e. </em>the maximum bacterial concentration after which bacteria cease cell division. Thus, the growth rate of bacteria slows down once it approaches the carrying capacity value.</p>
        </a>
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<div class="div-eq">
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<img src="https://static.igem.org/mediawiki/2017/f/f9/T--Edinburgh_OG--model_bg_eq4.png">
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<p>Campbell&rsquo;s model was describing continuous culture in a chemostat, which is a bioreactor with a continuous inflow of fresh medium and outflow of liquid culture with phage particles and bacteria. Therefore, a washout rate of both phages and bacteria was also taken into account as simple first-order kinetics, where <em>D</em> is the <em>dilution rate</em>:</p>
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        <h2 class="featurette-heading">Single Cell Model</h2>
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<p>In order to simulate real life environment, bacterial (<em>d</em><em>X</em>) and phage decay (<em>d</em><em>P</em>) rates were introduced. It has been shown that UV light can have a significant negative impact on phage infectivity by altering its DNA, which is does not necessarily destroy the virion particles (Suttle and Chen, 1992; Rastogi <em>et al.</em>, 2010). In nature phage decay is also associated with absorption by heat-labile particles or direct consumption by flagellates (Suttle and Chen, 1992; Deng <em>et al.</em>, 2014). Bacterial cells are more robust compared to the phages, but are subject to endogenous decay, which is caused by oxidation of internal cell components for production of energy and life maintenance whilst being limited by the availability of the growth substrate (Droste, 1998).</p>
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        <h2 class="featurette-heading">Atmospheric Pollution Model</h2>
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<img style="height: 130px;" src="https://static.igem.org/mediawiki/2017/f/f6/T--Edinburgh_OG--model_bg_eq6.png">
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<p>Arguably, one of the most important aspects of mathematical modelling is the initial set of assumptions that are used to build a model. The very first model of phage-bacterial interactions published by Campbell (1961) was based on the following assumptions:</p>
 
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<ol>
    <a name="singlecellmodel"></a>
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<li>1. A single bacterial cell can be infected only by one phage.</li>
    <hr class="featurette-divider">
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<li>2. Both rates of phage attachment and infection are dependent on bacterial and phage concentrations.</li>
 
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<li>3. The burst size does not change and is the same for each infection.</li>
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<li>4. The latency time does not change and is the same for each infection.</li>
      <div class="Up">
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<li>5. The bacterial growth rate is expressed as a logistic function.</li>
        <h2 class="featurette-heading">Single Cell Model</h2>
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<p>Based on these assumptions, he came up with the following set of delayed differential equations (DDEs):</p>
          <p class="lead Up">The single cell model incorporated a gene regulatory network (GRN) and the kinetics of our enzymes Nap and Nrf. Thus, we were able to obtain rates for the conversion of nitrite and nitrate (i.e. dissolved NOx) to ammonia specifically within
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<div class="div-eq">
            our system containing bacteria that are overexpressing the enzymes. An overview of this model is given below:</p>
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<img style="height: 130px;" src="https://static.igem.org/mediawiki/2017/6/68/T--Edinburgh_OG--model_bg_eq7.png">
        </div>
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</div>
 
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<p>Notably, most of these assumptions are nowadays considered false by the community working on bacteria-phage interaction. Firstly, there are multiple binding sites to which phage particles can attach to on the bacterial membrane. Thus, many of them can be occupied at the same time, leading to multiple simultaneous infections (Figure 3). Secondly, the burst size is affected by a number of variables, including the cell size of the bacterium, its metabolic activity and particular phage-bacteria relationship (Parada, Herndl and Weinbauer, 2006). Similarly, the latency time depends on the cell density, selecting for a shorter latency time upon high cell density and opting for longer latency upon low density (Wang, Dykhuizen and Slobodkin, 1996). Lastly, the bacterial growth is naturally dependent on the availability of resources to feed on, therefore the logistic equation for the bacterial growth has been replaced for the Monod equation, which takes availability of the substrate into account.</p>
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<div class="div-fig" style="width: 350px;">
          <img class="Pop centreimage" width=70% src="https://static.igem.org/mediawiki/2017/b/bb/T--Bristol--Modelling.png">
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<img src="https://static.igem.org/mediawiki/2017/c/cd/T--Edinburgh_OG--model_bg_Picture3.png">
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<p><strong>Figure 3.</strong> Multiple phages attached to the bacterial membrane via phage binding sites. Taken from Smith and Trevino (2009).</p>
 
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<p>To tackle some of these limitations, Levin <em>et al. </em>(1977) proposed a new generalized model, that could include any number of phages and bacterial species, as well as substrates. The change rate of the concentration of substrate depends on its consumption by both non-infected and infected bacteria, multiplied by the inverse value of the bacterial yield (<em>Y</em>), and concentration of inflow and outflow medium:</p>
          <p class="lead Up">The GRN enabled us to model the production rates and extent of Nrf and Nap. The concentrations of both enzymes are able to be predicted when the rates of transcription, translation and degradation (of both mRNA and protein) are known. Because
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<div class="div-eq">
            our construct included an IPTG-inducible promoter, the concentration of IPTG was relevant and therefore also had to be considered.</p>
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<img src="https://static.igem.org/mediawiki/2017/7/7f/T--Edinburgh_OG--model_bg_eq8.png">
          <p class="lead Up">Having obtained enzyme concentrations from our GRN or estimating them, the next step was to model the kinetics of these enzymes within a cell. Modelling the enzyme kinetics involved understanding of differential equations, and the derivations
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</div>
            are listed in the <a target="_blank" href="https://static.igem.org/mediawiki/2017/e/eb/T--Bristol--ModellingSupplement.pdf">modelling supplement PDF</a>. This model takes initial concentrations of all substances present and rate constants as inputs;
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<p>The growth of non-infected bacteria is described by the Monod equation:</p>
            a sample result is given below (note the values are arbitrary).</p>
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<div class="div-eq">
        </div>
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<img src="https://static.igem.org/mediawiki/2017/4/42/T--Edinburgh_OG--model_bg_eq9.png">
 
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<p>They also included a separate equation to track the change in population of infected bacteria as well as its removal from the chemostat, which had a negative impact on the number of phage particles generated from lysis and has not been included into Campbell&rsquo;s (1961) model.</p>
              <img class="Pop centreimage" width=70% src="https://static.igem.org/mediawiki/2017/1/15/T--Bristol--Velocity.png">
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<div class="div-eq">
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<img style="height: 130px;" src="https://static.igem.org/mediawiki/2017/8/83/T--Edinburgh_OG--model_bg_eq10.png">
 
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<p>Although Levin&rsquo;s model predicted the concentrations at steady-state within an order of magnitude from experimental values, it also predicted a total extinction of either phage or bacteria, or both, whereas this was not observed experimentally. Ultimately, the model was labelled not complex enough to accurately describe the interactions of phage and bacteria (Levin, Stewart and Chao, 1977). Since then, the model has been extended by others to include variable absorption rate and burst size (Smith and Thieme, 2012), multiple binding sites (Smith and Trevino, 2009), bacterial resistance to phages (Lenski and Levin, 1985; Cairns <em>et al.</em>, 2009) and spatial heterogeneity (Jones and Smith, 2011). Detailed description of these extensions is beyond the scope of this study.</p>
              <img class="Pop centreimage" width=70% src="https://static.igem.org/mediawiki/2017/d/d0/T--Bristol--Enzymes.png">
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<p>In 2007 Qiu augmented Levin&rsquo;s model by adding lysogenic cycle to it in order to study the dynamic mechanisms of the lytic-lysogeny decision. In contrast to Levin, <em>lysogenic bacteria</em>, that is bacteria infected with temperate phages, were able to grow by consuming substrate. He also introduced an <em>induction rate</em> (<em>q</em>) &ndash; that is the rate at which lysogenic bacteria enter lytic cycle either spontaneously or due to environmental factors discussed previously. The concentration of free phage particles (<em>P</em><em>T</em>) only increased due to induction of lysogenic bacteria (<em>X</em><em>L</em>).</p>
            </div>
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<p>It is worth noting that Qiu&rsquo;s model did not account for time latency between infection and lysis, thus presenting a system of ODEs rather than DDEs (Qiu, 2007).</p>
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<div><a class="btn-result" style="width:90%;" data-wow-delay=".9s" href="https://2017.igem.org/Team:Edinburgh_OG/Model" style="visibility: visible; animation-delay: 0.9s;">Model Homepage</a></div>
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<div style="clear:both;"><a class="btn-result btn-active" data-wow-delay=".9s" href="https://2017.igem.org/Team:Edinburgh_OG/Model:Background" style="visibility: visible; animation-delay: 0.9s;">Background</a>
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<a class="btn-result" data-wow-delay=".9s" href="https://2017.igem.org/Team:Edinburgh_OG/Model:Methodology" style="visibility: visible; animation-delay: 0.9s;">Methodology</a></div>
            <img src="https://static.igem.org/mediawiki/2017/d/d0/T--Bristol--Enzymes.png">
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<div style="clear:both;" class="btn-row"><a class="btn-result" data-wow-delay=".9s" href="https://2017.igem.org/Team:Edinburgh_OG/Model:Results" style="visibility: visible; animation-delay: 0.9s;">Results</a>
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<a class="btn-result" data-wow-delay=".9s" href="https://2017.igem.org/Team:Edinburgh_OG/Model:References" style="visibility: visible; animation-delay: 0.9s;">References</a></div>
          <div class="col-md-6 centreimage">
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                <a target="_blank"href="https://static.igem.org/mediawiki/2017/e/eb/T--Bristol--ModellingSupplement.pdf">
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                  <p class="design-button">Modelling Supplement</p>
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          <p class="lead Up"><br>Given this model, we then searched the literature extensively for all the constants we required. With valuable correspondence with Professor Julea Butt (of the University of East Anglia) we were able to obtain some values for the required
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            constants (Kcat, Kd and Km) for both enzymes, however we found that these values came from conflicting sources using very different measurement techniques, rendering them of little use for our modelling. Equally, we were unable find any values
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            for the Kcat and Kd of Nap. Listed below, however, are the values we were able to find:</p>
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          <p class="lead team"><i>*Value obtained is in Paracoccus pantotrophus, E. coli values being absent in the literature</i></p>
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          <p class="lead Up"><br>There are a number of factors that could influence the system that we have not incorporated in the model. These include the rate of uptake of nitrate/nitrite into the periplasm by the cells, but E. coli are equipped to do this and we assume
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            that this will not be rate limiting. We are also assuming that ammonia produced will diffuse out of the cell and not be toxic; E. coli are tolerant of fairly high ammonia concentrations. If the ammonia did begin to be toxic to the cells, a
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            future amendment to pod design could be to actively remove ammonia from the bacterial component to be fed into the fuel cell.</p>
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          <p class="lead Up">The combination of the GRN (giving us enzyme concentrations) and the enzyme kinetics (giving us the rates at which our substrates (nitrite and nitrate) are converted to product (ammonia) provides the information required to establish the capacity
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            of an E. coli cell to metabolise NOx, i.e. the single cell model.</p>
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        </div>
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        <h2 class="featurette-heading">Future work</h2>
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          <p class="lead Up">In future the single-cell model could be scaled up to a population model, such as Bristol iGEM 2008’s software BSim. Within such an agent-based model, each "agent" would represent a bacterium overexpressing our enzymes, which degrade NOx as
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            per the enzyme kinetics equations. Rules can be added to each cell to define its viability in the presence of the overexpressed enzymes or of ammonia, as well as longevity and random efficiency.</p>
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          <p class="lead Up">This population model can be fed with data from the atmospheric model – i.e. accurate NOx concentrations in the city of Bristol - to enable us to simulate the entire system that would be contained within a pod, assessing efficiency, nutrient
+
            requirements and other factors that would influence pod design, such as the necessary size of the pod, as well as the prediction of problems that may arise. This enabled a more realistic simulation of how efficient our pods would be in a real-world
+
            setting.
+
          </p>
+
          <br>
+
        </div>
+
 
+
        <div class="row align-items-center justify-content-center col-md-12">
+
          <div class="col-sm-12 col-md-6 col-lg-6 medal-link Pop">
+
            <a target="_blank" href="https://static.igem.org/mediawiki/2017/e/eb/T--Bristol--ModellingSupplement.pdf">
+
              <p class="design-button">Modelling Supplement</p>
+
            </a>
+
          </div>
+
        </div>
+
 
+
        <div class="row fadeIn">
+
          <div class="col-md-12">
+
            <h4>References</h4>
+
            <p>
+
              1. Lockwood, C. W. J. et al. Resolution of key roles for the distal pocket histidine in cytochrome c nitrite reductases. J. Am. Chem. Soc. 137, 3059–3068 (2015).
+
            </p>
+
            <p>
+
              2. Gates, A. J., Butler, C. S., Richardson, D. J. & Butt, J. N. Electrocatalytic reduction of nitrate and selenate by NapAB. Biochem. Soc. Trans. 39, 236–42 (2011).
+
            </p>
+
          </div>
+
        </div>
+
 
+
      </div>
+
    </div>
+
 
+
    <a name="atmosphericpollutionmodel"></a>
+
    <hr class="featurette-divider">
+
    <h2 class="featurette-heading">Atmospheric Modelling</h2>
+
    <div class="row fadeIn">
+
      <div class="col-lg-6 Up">
+
        <h2 class="featurette-heading">Motivation</h2>
+
        <p class="lead">The BREATHE project aims to reduce NOx pollution levels around Bristol and other urban areas by placing pods with genetically engineered E. coli bacteria that convert NOx into Ammonia. In order to make the biggest impact whilst minimising costs
+
          it is crucial to have pods placed in strategic areas of high pollution. To achieve this we have developed a simple atmospheric model to predict the pollution levels in Bristol city.</p>
+
      </div>
+
 
+
      <div class="col-lg-6 Up">
+
        <h2 class="featurette-heading">Aim</h2>
+
        <p class="lead">The aims of this model are:</p>
+
        <p class="lead">
+
          &#8226; Predict levels of NOx pollution to a reasonable accuracy.<br> &#8226; Find areas of high NOx concentration in Bristol City depending on the wind conditions.<br> &#8226; Use real traffic flow and car engine data to generate inputs.<br>          &#8226; Predict the effectiveness of placing Pods in strategic points.
+
        </p>
+
      </div>
+
    </div>
+
 
+
    <div class="row align-items-center fadeIn">
+
      <div class="col-md-12 Up">
+
        <h2 class="featurette-heading">Model</h2>
+
        <p class="lead">We need to be able to model the behaviour of NOx molecules in the atmosphere and predict how they propagate over time. The main considerations for the model are to capture the effects caused by wind, diffusion and the sources of NOx pollution.
+
          An appropriate equation for this is the advection-diffusion equation shown here.</p>
+
 
+
        <div style="text-align:center;">
+
          <img src="https://static.igem.org/mediawiki/2017/9/92/T--Bristol--AD-Equation.png" style="height:70px;max-width:100%;">
+
        </div>
+
 
+
        <p class="lead">where:</p>
+
        <p class="lead">
+
          <ul class="list-group">
+
            <li class="list-group-item" style="border:none;">&#8226; f is the concentration of NOx. ug/m&sup2;</li>
+
            <li class="list-group-item" style="border:none;">&#8226; u is the velocity field. m/s</li>
+
            <li class="list-group-item" style="border:none;">&#8226; c is the diffusion constant. m&sup2;/s</li>
+
            <li class="list-group-item" style="border:none;">&#8226; S is the source value of the production of NOx. ug/m&sup2;s </li>
+
          </ul>
+
        </p>
+
 
+
        <p class="lead">This is the underlying equation used in the model and is solved numerically by taking a Forward Time Central Space (FTCS) finite difference scheme, derived using a Taylor series expansion. Further details regarding the model and describing how
+
          this equation is derived can be found in the modelling supplement document.</p>
+
        <a href="https://static.igem.org/mediawiki/2017/e/eb/T--Bristol--ModellingSupplement.pdf" target="_blank"><button type="button" class="btn btn-info">Supplement Document</button></a>
+
      </div>
+
 
+
      <div class="col-md-12 Up">
+
        <h2 class="featurette-heading">Parameters</h2>
+
        <p class="lead">In order to run the simulation and achieve realistic results we required real input data and parameters. The diffusion coefficient of NO<sub>2</sub> was used and found to be approximately 1.36&times;10&#8315;&#8309;m&sup2;s&#8315;&sup1; [1]. Realistic
+
          wind conditions in Bristol could be found from the Met Office [2] however, as the weather varies throughout the year in the UK a range of wind conditions could be used.
+
          <br> <br>Data for the NO<sub>2</sub> sources is not something that is available for the entire Bristol city area or for any city as a matter of fact. Therefore, a plan was devised in order to estimate what the rate of pollution production would
+
          be for a given type of road. This was done by aggregating data from different databases together to come up with an approximation. The steps involved are shown in the diagram below.
+
        </p>
+
 
+
        <img src="https://static.igem.org/mediawiki/2017/0/06/T--Bristol--InputData.svg" style="width:100;">
+
      </div>
+
 
+
      <div class="col-md-12">
+
        <h3>Traffic Flow Data</h3>
+
      </div>
+
      <div class="col-md-12">
+
        <p class="lead">Data from the UK Department for Transport on the Annual Average Daily Flow (ADDF) on A roads and Motorways in Bristol City [3] was used to estimate traffic flow statistics. The database consists of actual and estimated data for a large amount
+
          of A Roads/Motorways in Bristol. The data was aggregated into the different road types and their respective means calculated. A histogram showing the distribution of the data and the mean values are shown below.</p>
+
 
+
        <div class="row">
+
          <div class="col-md-6">
+
            <img src="https://static.igem.org/mediawiki/2017/2/21/T--Bristol--avgaroad.svg" style="width:100%;">
+
          </div>
+
          <div class="col-md-6">
+
            <img src="https://static.igem.org/mediawiki/2017/8/85/T--Bristol--avgmroad.svg" style="width:100%;">
+
          </div>
+
          <p class="lead">
+
            <i>Figure 1: Two plots showing the distribution of traffic flow for A Roads (Left) and Motorways(Right) in Bristol City with the mean value shown for both..</i>
+
          </p>
+
        </div>
+
        <div class="row align-items-center">
+
          <div class="col-lg-8">
+
            <p class="lead">The means were normalised against a 24 hour period and the road distances to get the following values representing the traffic flow for every metre second.</p>
+
 
+
          </div>
+
          <div class="col-lg-4">
+
            <p class="lead">
+
              <i>Table 1: Average traffic flow values based on AADF traffic data for different road types.</i>
+
            </p>
+
            <table class="table table-hover table-bristol">
+
              <thead class="thead-inverse table-striped">
+
                <tr>
+
                  <th>Road Type</th>
+
                  <th>Average Traffic Flow (1/ms) 1&times;10&#8315;&sup3;</th>
+
                </tr>
+
              </thead>
+
              <tbody>
+
                <tr>
+
                  <th scope="row">Motorway</th>
+
                  <td>1.0436</td>
+
                </tr>
+
              </tbody>
+
              <tbody>
+
                <tr>
+
                  <th scope="row">A Road</th>
+
                  <td>0.4891</td>
+
                </tr>
+
              </tbody>
+
              <tbody>
+
                <tr>
+
                  <th scope="row">&#42;B Road</th>
+
                  <td>0.2445</td>
+
                </tr>
+
              </tbody>
+
            </table>
+
          </div>
+
        </div>
+
        <i><p class="lead">&#42;No data was available for B Roads in Bristol and so it was grossly assumed that it would be half of an A road traffic flow.</p></i>
+
      </div>
+
 
+
      <div class="col-md-12">
+
        <h3>Petrol to Diesel Ratio</h3>
+
      </div>
+
      <div class="col-lg-8">
+
        <p class="lead">NOx pollution varies dramatically between petrol and diesel with the latter being the bigger source of pollution. In order to account for this it was important to get data regarding the distribution of different car fuel types currently being
+
          used in the UK. This data came from UK Department for Transport Vehicle Licensing Statistics [4] on the car fuel type distribution for the UK.</p>
+
        <p class="lead">The database included data for Gas, Hybrid, Electric and Other vehicle fuel types. Because these were in such small percentages, some of which don't produce NOx pollution, so they were ignored in the simulation.</p>
+
      </div>
+
      <div class="col-lg-4">
+
        <p class="lead">
+
          <i>Table 2: Percentage of UK cars based on engine fuel type.</i>
+
        </p>
+
        <table class="table table-hover table-bristol">
+
          <thead class="thead-inverse table-striped">
+
            <tr>
+
              <th>Fuel Type</th>
+
              <th>Percentage of UK cars</th>
+
            </tr>
+
          </thead>
+
          <tbody>
+
            <tr>
+
              <th scope="row">Petrol</th>
+
              <td>59.7</td>
+
            </tr>
+
          </tbody>
+
          <tbody>
+
            <tr>
+
              <th scope="row">Diesel</th>
+
              <td>39.1</td>
+
            </tr>
+
          </tbody>
+
          <tbody>
+
            <tr>
+
              <th scope="row">Gas</th>
+
              <td>1.0</td>
+
            </tr>
+
          </tbody>
+
          <tbody>
+
            <tr>
+
              <th scope="row">Electric</th>
+
              <td>0.1</td>
+
            </tr>
+
          </tbody>
+
          <tbody>
+
            <tr>
+
              <th scope="row">Other</th>
+
              <td>0.1</td>
+
            </tr>
+
          </tbody>
+
        </table>
+
      </div>
+
 
+
      <div class="col-md-12">
+
        <h3>Engine Pollution Statistics</h3>
+
      </div>
+
 
+
      <div class="col-md-12">
+
        <p class="lead">Data was required in order to quantify how much NOx pollution one car emits. This data was available from the UK Department for Environment, Food &amp; Rural Affairs [5].
+
        </p>
+
        <p class="lead">
+
          Engines have improved over the years and produce less and less pollutants with each new generation. As it was not possible to get data regarding the distribution of emission standards for all the cars in the UK, it was assumed all cars emit at the level
+
          of the Euro IV standard.
+
        </p>
+
      </div>
+
      <div class="col-md-12">
+
        <p class="lead">
+
          <i>Table 3: Car NO<sub>2</sub> emission levels based on fuel type and engine emissions standard for different environmental areas.</i>
+
        </p>
+
        <table class="table table-hover table-bristol">
+
          <thead class="thead-inverse">
+
            <tr>
+
              <th>gNOx/km</th>
+
              <th>Emissions Standard</th>
+
              <th>Urban</th>
+
              <th>Rural</th>
+
              <th>Motorway</th>
+
            </tr>
+
          </thead>
+
          <tbody>
+
            <tr>
+
              <th>Petrol</th>
+
              <td>Euro I</td>
+
              <td>0.257</td>
+
              <td>0.368</td>
+
              <td>0.663</td>
+
            </tr>
+
          </tbody>
+
          <tbody>
+
            <tr>
+
              <th>Petrol</th>
+
              <td>Euro II</td>
+
              <td>0.229</td>
+
              <td>0.245</td>
+
              <td>0.370</td>
+
            </tr>
+
          </tbody>
+
          <tbody>
+
            <tr>
+
              <th>Petrol</th>
+
              <td>Euro III</td>
+
              <td>0.137</td>
+
              <td>0.147</td>
+
              <td>0.222</td>
+
            </tr>
+
          </tbody>
+
          <tbody>
+
            <tr>
+
              <th>Petrol</th>
+
              <td><b>Euro IV</b></td>
+
              <td><b>0.073</b></td>
+
              <td><b>0.078</b></td>
+
              <td><b>0.118</b></td>
+
            </tr>
+
          </tbody>
+
          <tbody>
+
            <tr>
+
              <th>Diesel</th>
+
              <td>Euro I</td>
+
              <td>0.537</td>
+
              <td>0.465</td>
+
              <td>0.693</td>
+
            </tr>
+
          </tbody>
+
          <tbody>
+
            <tr>
+
              <th>Diesel</th>
+
              <td>Euro II</td>
+
              <td>0.547</td>
+
              <td>0.505</td>
+
              <td>0.815</td>
+
            </tr>
+
          </tbody>
+
          <tbody>
+
            <tr>
+
              <th>Diesel</th>
+
              <td>Euro III</td>
+
              <td>0.547</td>
+
              <td>0.505</td>
+
              <td>0.815</td>
+
            </tr>
+
          </tbody>
+
          <tbody>
+
            <tr>
+
              <th>Diesel</th>
+
              <td><b>Euro IV</b></td>
+
              <td><b>0.273</b></td>
+
              <td><b>0.253</b></td>
+
              <td><b>0.407</b></td>
+
            </tr>
+
          </tbody>
+
        </table>
+
      </div>
+
 
+
      <div class="col-md-12">
+
        <h3>Ordnance Survey Maps of Bristol</h3>
+
      </div>
+
 
+
      <div class="col-md-12">
+
        <p class="lead">An important part of the simulation is knowing where to place the source values. This was calculated by obtaining shapefile data from the Ordnance Survey (OS) [6] for all the roads in Bristol and converting it to a set of grid points using the
+
          Bresenham’s line algorithm.
+
        </p>
+
        <p class="lead">
+
          This presented itself with the issue that the traffic flow data and engine pollution statistics don’t match directly to all the road types given in the OS road data. The data was matched depending on which data was the most relevant and are shown in the
+
          table below along with the calculated source values.
+
        </p>
+
        <div class="col-md-12">
+
          <p class="lead">
+
            <i>Table 4: Calculated source values for different OS road types based on other aggregated pollution and traffic data.</i>
+
          </p>
+
          <table class="table table-hover table-bristol">
+
            <thead class="thead-inverse">
+
              <tr>
+
                <th>OS Road Type</th>
+
                <th>Average No. Cars [1/ms 1&times;10&#8315;&sup3;]</th>
+
                <th>Engine Emissions Environment (Petrol/Diesel) [&micro;g/m]</th>
+
                <th>Source Value [&micro;g/m&sup2;s]</th>
+
              </tr>
+
            </thead>
+
            <tbody>
+
              <tr>
+
                <th>A Road</th>
+
                <td>0.4891</td>
+
                <td>0.078 / 0.253</td>
+
                <td>0.2360</td>
+
              </tr>
+
            </tbody>
+
            <tbody>
+
              <tr>
+
                <th>B Road</th>
+
                <td>0.2445</td>
+
                <td>0.073 / 0.273</td>
+
                <td>0.0791</td>
+
              </tr>
+
            </tbody>
+
            <tbody>
+
              <tr>
+
                <th>Local Street</th>
+
                <td>0.2445</td>
+
                <td>0.073 / 0.273</td>
+
                <td>0.0791</td>
+
              </tr>
+
            </tbody>
+
            <tbody>
+
              <tr>
+
                <th>Minor Road</th>
+
                <td>0.2445</td>
+
                <td>0.073 / 0.273</td>
+
                <td>0.0791</td>
+
              </tr>
+
            </tbody>
+
            <tbody>
+
              <tr>
+
                <th>Motorway</th>
+
                <td>1.0436</td>
+
                <td>0.078 / 0.253</td>
+
                <td>0.5036</td>
+
              </tr>
+
            </tbody>
+
            <tbody>
+
              <tr>
+
                <th>Pedestrianised</th>
+
                <td>0</td>
+
                <td>0</td>
+
                <td>0</td>
+
              </tr>
+
            </tbody>
+
            <tbody>
+
              <tr>
+
                <th>Primary Road</th>
+
                <td>1.0436</td>
+
                <td>0.078 / 0.253</td>
+
                <td>0.5036</td>
+
              </tr>
+
            </tbody>
+
            <tbody>
+
              <tr>
+
                <th>Private Road</th>
+
                <td>0</td>
+
                <td>0</td>
+
                <td>0</td>
+
              </tr>
+
            </tbody>
+
          </table>
+
        </div>
+
      </div>
+
 
+
      <div class="col-md-12">
+
        <h3>Calculating Source Values</h3>
+
        <p class="lead">To calculate the rate of change of NOx concentration for a given road type an empirical formula was created based on the data gathered that satisfies dimensional homogeneity:
+
        </p>
+
        <div style="text-align:center;">
+
          <img src="https://static.igem.org/mediawiki/2017/e/eb/T--Bristol--Source-Equation.png" style="height:70px;max-width:100%;">
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      <div class="col-md-12 Up">
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        <h2 class="featurette-heading">Assumptions</h2>
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        <p class="lead">As with any modelling there are some assumptions made:</p>
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        <p class="lead">
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          &#8226; Although NO and NO<sub>2</sub> are unstable, this instability mostly arises from them switching between each other through atmospheric processes therefore, together they can be considered mostly stable.
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          <br> &#8226; Highly diffusive effects of turbulence are ignored.
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          <br> &#8226; There are no viscous effects experienced by NOx gases when travelling through the atmosphere.
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          <br> &#8226; Modelling the canopy above the streets as complex flows at street level are hard and expensive to model.
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          <br> &#8226; All engine emissions are similar to that of the Euro IV standard.
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          <br> &#8226; B Roads in Bristol see on average half as much traffic as A roads.
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        </p>
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        <h2 class="featurette-heading">Results</h2>
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        <p class="lead">The simulation was computationally expensive to run due to the small resolution used to capture road details whilst looking at an entire city area. In the end the simulation was only run for a zoomed in section of the city center. Five runs were
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          completed in total with varying wind speeds and directions and the results of the simulations are shown below. Surrounding building, roads, and rovers were included in the background of the plot to give those unfamiliar with Bristol an idea
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          of how the pollution looks over the city area.</p>
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      <p class="lead">
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        <i>Figures 4, 5, 6, 7, 8: Five plots showing the NOx concentration levels around the city of Bristol for winds varying from 5-15mph in varying directions.</i>
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        <h2 class="featurette-heading">Conclusion</h2>
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        <p class="lead">The simple advection diffusion equation captures the plume behaviour of the pollution adequately, as it is progated across the city. Currently there are no citywide NOx measurements to compare this data with but, there are a couple air quality
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          measurement stations in Bristol. Overall the results from the atmospheric modelling were surprising, with the level of NOx concentrations being similar to levels recorded at the Bristol, St. Pauls measuring station [7]. The concentrations are
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          still on the low side with only some areas reaching the levels that have been recorded previously in Bristol. It can be seen that the pollution builds up when there are many neighbouring roads. This means that NOx concentrations from outside
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          the computation area is being neglected and the calculated levels are going to be lower that they should be.</p>
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        <p class="lead">The diffusion coefficient caused a lot of issues regarding the stability of the numerical solution therefore, the timestep and change in distances had to be altered to provide stability at the loss of smoothness in the solution.</p>
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        <p class="lead">The model was able to satisfy most of the original aims set out in the beginning. The NOx levels were predicted to within a reasonable accuracy compared to measured data. Real traffic data along with engine emissions data were used to create succesful
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          estimates of the source values used in the simulation inputs. Results also show areas of high NOx concentrations depending on the wind conditions which can be used to strategically place pods with the aim of reducing pollution. We were not able
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          to assess the impact our pods would have in removing pollution. This was due to not having sufficient modelling and lab data to accurately predict how much the pods would clean up.</p>
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        <p class="lead">In going forward with these results there are a couple of things we would like to address in the future. The most important is getting data for our pods and inputting it into the simulation so we can build a picture of how effective these pods
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          will be once placed in strategic areas. In order to create a more accurate model it would be good to refine the data used to create the source values. Instead of generalising the traffic data it would be better to apply it to each individual
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          road seperately. As well as having a distribution of different engines with different emissions standards instead of solely choosing the Euro IV standard. This would require a lot more time and data processing which is why it was not covered
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          during this project. Lastly the computational area needs to be increased to capture the entire Bristol area. This will require more computing power or the grid resolution will have to be lowered in order to run the simulation in a reasonable
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          amount of time.</p>
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        <h4>References</h4>
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          1. Cape, J. N., Review of the use of passive diffusion tubes for measuring concentrations of nitrogen dioxide in air. <a href="https://uk-air.defra.gov.uk/assets/documents/reports/cat05/0810141025_NO2_review.pdf">Retrieved from</a> [accessed
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          01/11/2017].
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          2. Met Office., UK Weather Forecasts <a href="https://www.metoffice.gov.uk/public/weather/forecast/gcnhtnumz">Retrieved from</a> [accessed 01/11/2017]
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        </p>
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          3. Department for Transport., Traffic Data, Annual Average Daily Flows <a href="https://www.dft.gov.uk/traffic-counts/cp.php?la=Bristol%2C+City+of">Retrieved from</a> [accessed 01/11/2017]
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        </p>
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          4. Department for Transport., Licensed cars by propulsion or fuel type: Great Britain and United Kingdom <a href="https://www.dft.gov.uk/traffic-counts/cp.php?la=Bristol%2C+City+of">Retrieved from</a> [accessed 01/11/2017]
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        </p>
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          5. UK Department for Environment, Food &amp; Rural Affairs., Nitrogen Dioxide in the UK, Chapter 2, p[40-41] <a href="https://www.dft.gov.uk/traffic-counts/cp.php?la=Bristol%2C+City+of">Retrieved from</a> [accessed 01/11/2017]
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        </p>
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        <p>
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          6. Ordnance Survey., CDRC 2015 OS Geodata Pack - Bristol, City of (E06000023).
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        </p>
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        <p>
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          7. OpenAQ., The Open Source Air Quality database., <a href="https://openaq.org/">Retrieved from</a> [accessed 01/11/2017]
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Revision as of 11:32, 17 October 2018

Model: Background

  • Simple growth models of bacterial populations are based on two interdependent factors: the concentration of bacteria (X) and concentration of a growth limiting substrate (S) (Monod, 1949)(Figure 1A). Bacteria-phage model can be considered as an extended version of a simple model that includes a third dynamic factor: the phage (P)(Figure 1B). The first model was presented as a set of ordinary differential equations (ODDs) by Campbell (1961). In this model, the change rate of the bacterial population is dependent on the concentration of bacteria and substrate, as well as the rate of phage-induced lysis, which in turn is also dependent on the bacterial concentration (Figure 1B).

    Figure 1. Schematic diagram showing interactions in (A) a two-factor model containing bacteria and substrate, and (B) an extended three-factor model also containing a lytic phage as proposed by Campbell (1961). Taken from Krysiak-Baltyn et al. (2016).

    Lytic and lysogenic cycles of phage replication

    In order to model phage-bacteria interactions it is important to understand a step-by-step process of phage infection. Figure 2 shows a lytic life cycle of a lytic phage in a simplified five-step process: from diffusion and attachment to the bacterial cell membrane to cell lysis. The lysogenic life cycle of a temperate phage starts in a similar way to the lytic phage, however following the infection the phage genome either integrates itself into the host genome (λ phage) or forms a circularized plasmid-like structure (P1 phage)(Howard-Varona et al., 2017). The phage genome that has been integrated into the bacterial chromosome is also known as a prophage. Once integrated, temperate phage replicates together with the bacterial genome upon bacterial cell division. However, either spontaneously at low frequency (10-8–10-5) or due to unfavourable stress conditions, such as exposure to UV light, antibiotics, hydrogen peroxide and changes in temperature, nutrients or pH, can lead to a phage induction. Once induced, lytic-lysogenic switch gets activated leading to expression of viral genes, a switch to lytic life cycle and cell lysis.

    Figure 2. A simplified diagram of lytic and lysogenic life cycles of the phage. (1) diffusion of the phage particle to the bacterial cell; (2) phage attachment to the receptors along the bacterial membrane; (3) injection of phage genome into the cell; (3a) replication via cell division during lysogenic cycle; (3b) induction of lytic cycle; (4) replication of phage genome and assembly of capsid proteins; (5) cell lysis followed by the release of phage particles outside the cell. The burst size (b) shows the number of released phage particles. Adapted from Krysiak-Baltyn et al. (2016).

    b

    Burst size

    P

    Concentration of phage

    C

    Carrying capacity

    q

    Induction rate

    D

    Dilution rate


    S

    Concentration of substrate


    d

    Rate of decay of cells or phages


    T

    Latency time


    Ki

    Adsorption rate of phages to bacteria

    XS

    Concentration of susceptible bacteria (here antibiotic resistant bacteria)

    Km

    Half-saturation constant


    XI

    Concentration of infected bacteria


    μmax

    Maximum specific growth rate

    Y

    Bacterial yield, or bacterial cells per unit substrate

    Table 1. Parameters used in models of populations of phage and bacteria.

    Basic model

    Modelling of the processes described in Figure 2. involves developing and solving expressions for the concentrations of phages, infected and non-infected bacteria as well as the substrate. The key parameters involved into equations are listed in Table 1. Following the approach documented in Campbell (1961), the rate of infection is proportional to the concentration of bacteria, lytic phage and the absorption rate (Ki). The latter is the rate at which phage particles attach to the bacterial surface and it is dependent on (1) the concentrations of both bacteria and phage, (2) the time required for diffusion and attachment of the phage, and (3) the number of phage particles, which upon attachment to the bacterial cell, do not lead to infection.

    Oppositely, the growth rate of phage population decreases due to attachment of phage particles onto bacterial cells:

    And increases due to cell lysis and release of newly produced phage particles:

    The latency time (T) is caused by the time delay between the infection and cell lysis (steps 3 and 5 in Figure 2).

    The growth of bacterial population was represented as a logistic kinetic expression that is independent from the concentration of the growth limiting substrate, but dependent on the total carrying capacity (C) i.e. the maximum bacterial concentration after which bacteria cease cell division. Thus, the growth rate of bacteria slows down once it approaches the carrying capacity value.

    Campbell’s model was describing continuous culture in a chemostat, which is a bioreactor with a continuous inflow of fresh medium and outflow of liquid culture with phage particles and bacteria. Therefore, a washout rate of both phages and bacteria was also taken into account as simple first-order kinetics, where D is the dilution rate:

    In order to simulate real life environment, bacterial (dX) and phage decay (dP) rates were introduced. It has been shown that UV light can have a significant negative impact on phage infectivity by altering its DNA, which is does not necessarily destroy the virion particles (Suttle and Chen, 1992; Rastogi et al., 2010). In nature phage decay is also associated with absorption by heat-labile particles or direct consumption by flagellates (Suttle and Chen, 1992; Deng et al., 2014). Bacterial cells are more robust compared to the phages, but are subject to endogenous decay, which is caused by oxidation of internal cell components for production of energy and life maintenance whilst being limited by the availability of the growth substrate (Droste, 1998).

    Arguably, one of the most important aspects of mathematical modelling is the initial set of assumptions that are used to build a model. The very first model of phage-bacterial interactions published by Campbell (1961) was based on the following assumptions:

    1. 1. A single bacterial cell can be infected only by one phage.
    2. 2. Both rates of phage attachment and infection are dependent on bacterial and phage concentrations.
    3. 3. The burst size does not change and is the same for each infection.
    4. 4. The latency time does not change and is the same for each infection.
    5. 5. The bacterial growth rate is expressed as a logistic function.

    Based on these assumptions, he came up with the following set of delayed differential equations (DDEs):

    Notably, most of these assumptions are nowadays considered false by the community working on bacteria-phage interaction. Firstly, there are multiple binding sites to which phage particles can attach to on the bacterial membrane. Thus, many of them can be occupied at the same time, leading to multiple simultaneous infections (Figure 3). Secondly, the burst size is affected by a number of variables, including the cell size of the bacterium, its metabolic activity and particular phage-bacteria relationship (Parada, Herndl and Weinbauer, 2006). Similarly, the latency time depends on the cell density, selecting for a shorter latency time upon high cell density and opting for longer latency upon low density (Wang, Dykhuizen and Slobodkin, 1996). Lastly, the bacterial growth is naturally dependent on the availability of resources to feed on, therefore the logistic equation for the bacterial growth has been replaced for the Monod equation, which takes availability of the substrate into account.

    Figure 3. Multiple phages attached to the bacterial membrane via phage binding sites. Taken from Smith and Trevino (2009).

    To tackle some of these limitations, Levin et al. (1977) proposed a new generalized model, that could include any number of phages and bacterial species, as well as substrates. The change rate of the concentration of substrate depends on its consumption by both non-infected and infected bacteria, multiplied by the inverse value of the bacterial yield (Y), and concentration of inflow and outflow medium:

    The growth of non-infected bacteria is described by the Monod equation:

    They also included a separate equation to track the change in population of infected bacteria as well as its removal from the chemostat, which had a negative impact on the number of phage particles generated from lysis and has not been included into Campbell’s (1961) model.

    Although Levin’s model predicted the concentrations at steady-state within an order of magnitude from experimental values, it also predicted a total extinction of either phage or bacteria, or both, whereas this was not observed experimentally. Ultimately, the model was labelled not complex enough to accurately describe the interactions of phage and bacteria (Levin, Stewart and Chao, 1977). Since then, the model has been extended by others to include variable absorption rate and burst size (Smith and Thieme, 2012), multiple binding sites (Smith and Trevino, 2009), bacterial resistance to phages (Lenski and Levin, 1985; Cairns et al., 2009) and spatial heterogeneity (Jones and Smith, 2011). Detailed description of these extensions is beyond the scope of this study.

    In 2007 Qiu augmented Levin’s model by adding lysogenic cycle to it in order to study the dynamic mechanisms of the lytic-lysogeny decision. In contrast to Levin, lysogenic bacteria, that is bacteria infected with temperate phages, were able to grow by consuming substrate. He also introduced an induction rate (q) – that is the rate at which lysogenic bacteria enter lytic cycle either spontaneously or due to environmental factors discussed previously. The concentration of free phage particles (PT) only increased due to induction of lysogenic bacteria (XL).

    It is worth noting that Qiu’s model did not account for time latency between infection and lysis, thus presenting a system of ODEs rather than DDEs (Qiu, 2007).