Team:ETH Zurich/Modeling/Reaction Diffusion OOHL

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<p align="justify">As can be seen, the model predicts that mine cells are able to generate a suitable gradient by synthesizing OHHL at a sufficient rate to overcome the decay. Additionally, the gradient is suitable because concentrations of OHHL that can be sensed by receiver cells are clearly different depending on the number of  adjacent mine cells. </p>
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<p align="justify">As can be seen, the model predicts that mine cells are able to generate a suitable gradient by synthesizing OHHL at a sufficient rate to overcome the decay and the active degradation; the gradient is suitable because receiver cells are exposed to different concentrations of OHHL, depending on the number of  adjacent mine colonies. </p>
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Revision as of 19:35, 15 October 2013

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OHHL: Reaction-diffusion equations

Modeling the OHHL diffusion is important to get insights about time scale and distances, which plays an important role in determining the geometric setup of the playing field.


Video: 2D gradient formation over 24 hours, starting from OHHL steady state concentration in the mine cells.
Display: OHHL concentration in mol/m3. Distance between colonies: 1.5 cm.

The change of OHHL concentration over time is influenced by two processes: (i) local chemical reactions and (ii) diffusion; which causes the molecule to spread radially through the agar. (Eq. 1).

Equation 1: General partial differential equation for OHHL reaction-diffusion in 2D (r=x,y). D(OHHL(r,t),r) is the diffusive term, R(OHHL(r,t)) is the reaction term.


For diffusion, we have a partial differential equation (Eq. 2) which describes density fluctuations over time and space (r=(x,y)). We do not model OHHL diffusion in and out cells explicitly; the underlying assumption is that this process is fast or that the molecule diffuses freely. In equation 2, DOHHL(OHHL(r,t),r) denotes the collective diffusion coefficient for OHHL at location r. However, we assume that the diffusion coefficient does not depend on the density, i.e., DOHHL is a constant. The value reported in the literature for the diffusion constant corresponds to measurements performed in water at 25oC. As the OHHL in our system diffuses in agar, we scaled the diffusion constant by a factor Cagar (Fatin-Rouge et al., 2004).

Equation 2: Diffusive term for OHHL. r =(x,y)


For the reaction component, the change of OHHL concentration over time is modeled by a set of ordinary differential equations (ODEs), that includes the production and linear degradation or decay. However, the types of reactions that take place depend on the localization, i.e. extracellular or cytoplasmic. In the case of cytoplasmic localization, we have to further distinguish between the two type of cells encountered in our system, sender cells and receiver cells. Mine cells synthesized the signalling molecule which depends on the product of luxI gene, while for the degradation we assumed a linear dependency of the molecule concentration. For the receiver cells only linear degradation take place, and we assume that is under the same rate as mine cells. However, for the extracellular decay we consider that OHHL degrades at a different rate, because the intracellular process is driven by enzymatic degradation, whereas the extracellular decay is a non active process. Furthermore, we include a dilution factor to account for cell growth modelled using the logistic equation (Eq. 3). It is important to point out that, the growth rate was obtained from experiments.

Equation 3: Reaction term for OHHL. DF is the dimensionless dilution factor, where N0 is the initial concentration and Nm is the carrying capacity (scaling factor, Nm = 1).


Finally, we need to specify initial conditions (at time t = 0) and boundary conditions. At the starting point there is no OHHL in the agar plate, thus the initial concentration is zero ([OHHL](r,t=0) = 0 M) for receiver cells and in the agar plate. However, the initial concentration in the mine cells was set to the steady state concentration. For the boundary condition, we take into account that there is not flux out of the agar plate.

Equation 4: Neumann Boundary Condition.


RESULTS: Simulation

In Figure 1 is displayed the time course of the averaged concentration of OHHL for colonies surrounded by 0, 1, 2 or 3 mine colonies. The steady state concentration versus distance for OHHL concentration is displayed in Figure 2.


Figure 1: Averaged OHHL concentration sensed by colonies with 0, 1 or 2 adjacent mines cells, in μ M. Distance between colonies: 1.5 cm.
Figure 2: 1D OHHL steady state concentration in radial direction, in mol/m3.


As can be seen, the model predicts that mine cells are able to generate a suitable gradient by synthesizing OHHL at a sufficient rate to overcome the decay and the active degradation; the gradient is suitable because receiver cells are exposed to different concentrations of OHHL, depending on the number of adjacent mine colonies.


Growth curve fitting

The estimation of the growth rate parameter was carried out using a mcmc variant, Delayed Rejection Adaptive Metropolis (DRAM).The optical density measurements were conducted in triplicate over 17 hours, results are shown in figure 3 and 4. This parameter was incorporated in the model.

Figure 3: Experimental data and fitted logistic curve (residuals = 0.033 on 62 degrees of freedom).
Figure 4: Histogram for the growth rate (k = 0.888 +/- 0.089)