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Team:TUDelft/Color modeling
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x<sub>1</sub> to x<sub>14</sub> are the subtrates. | x<sub>1</sub> to x<sub>14</sub> are the subtrates. | ||
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| - | We used hill type model for enzyme temperature relations where e<sub>1</sub> to e<sub>13</sub> are the enzymes. Afterwards the in '''CellDesigner™''' file was imported into Matlab. For this procedure many softwares were tested but finally the [http://www.sys-bio.org synthetic biology workbench] site used to convert the SBML model into m file. This m file was the base part for the modeling in Matlab. In this m file all the related differential equations were defined as a function with the time span and initial condition as the input. The reactions coefficients are defined by some not systemically acquired numbers to give an estimation for the reactions. These differential equations were solved by Matlab ODE function. Due to the weaknesses in CellDesigner for defining the SBML file the converted file had many problems. To solve these problems the m file was modified. | + | We used hill type model for enzyme temperature relations where e<sub>1</sub> to e<sub>13</sub> are the enzymes. Afterwards the in '''CellDesigner™''' file was imported into Matlab. For this procedure many softwares were tested but finally the [http://www.sys-bio.org synthetic biology workbench] site used to convert the SBML model into m file. This m file was the base part for the modeling in Matlab. In this m file all the related differential equations were defined as a function with the time span and initial condition as the input. The reactions coefficients are defined by some not systemically acquired numbers to give an estimation for the reactions. These differential equations were solved by Matlab ODE function. Due to the weaknesses in CellDesigner for defining the SBML file the converted file had many problems. To solve these problems the m file was modified. |
==Initial solution for ODEs== | ==Initial solution for ODEs== | ||
Revision as of 02:05, 28 October 2008
Contents |
The Model
The model of biothermometer is included an input and output. The input of the model is the enzyme synthesis controlled by the temperature and the output is color production. The challenges for the modeling part are:
- Finding a suitable model for a temperature dependence synthesis for the color producing enzymes.
- Solving the Michaelis-Menten kinetic equations to obtain the dynamics of pathway intermediates.
The procedure for modeling was started with the output part, color pathway, and continued to the enzyme synthesis which can be controlled by temperature.
Color Modeling
In the output we use [http://www.lbl.gov/Science-Articles/Archive/assets/images/2004/Mar-24/Engineering_terpenoids.pdf mevalonate] and [http://parts.mit.edu/igem07/index.php/Image:Zeaxanthin.jpg GPP] pathways together to produce red, orange and yellow colors. The biosynthetic model is built in CellDesigner™. There are 14 substrates and 13 enzymes in total. The first substrate is Acetyl-CoA which is provided to the pathway in a constant level. The last three substrates are the color products and are consuming so we have degradation links for them. Lycopene, B-carotene and Zeaxanthin give red, orange and yellow colors respectively.
Kinetic Equations
For the 14 reactions of enzyme-substrate the Michaelis-Menten kinetics is applied and we have the mass action kinetics for the three degradations. According to the kinetic laws there are 14 differential equations for enzyme-substrate reactions and three for degradations which could be constructed as:
x1 to x14 are the subtrates.
We used hill type model for enzyme temperature relations where e1 to e13 are the enzymes. Afterwards the in CellDesigner™ file was imported into Matlab. For this procedure many softwares were tested but finally the [http://www.sys-bio.org synthetic biology workbench] site used to convert the SBML model into m file. This m file was the base part for the modeling in Matlab. In this m file all the related differential equations were defined as a function with the time span and initial condition as the input. The reactions coefficients are defined by some not systemically acquired numbers to give an estimation for the reactions. These differential equations were solved by Matlab ODE function. Due to the weaknesses in CellDesigner for defining the SBML file the converted file had many problems. To solve these problems the m file was modified.
Initial solution for ODEs
The m file function, as mentioned before, was solved by the ode15s function of Matlab. To do this procedure some assumptions were applied. The first substrate, Acetyl-CoA, assumed to produced and consumed with the same ratio. Also for simplification the level of enzymes assumed to be constant. The reaction coefficients are defined the same for all reaction with some non-accurate numbers to give an overview about the reactions. The results for these assumptions and specific boundary condition and time span of 200 seconds were plotted. These results show the steady state situation for the last three products after 200 seconds. The plot is:
Effects of the temperature on enzymes
[http://student.ccbcmd.edu/biotutorials/proteins/enzyme.html Enzymes] are catalysts that breakdown or synthesize more complex chemical compounds. They allow chemical reactions to occur fast enough to support life. Anything that an enzyme normally combines with is called a substrate. Each enzyme has an [http://student.ccbcmd.edu/biotutorials/proteins/enzyme.html optimum temperature] at which it works best. A higher temperature generally results in an increase in enzyme activity. As the temperature increases, molecular motion increases resulting in more molecular collisions. If, however, the temperature rises above a certain point, the heat will denature the enzyme, causing it to lose its three-dimensional functional shape by denaturing its hydrogen bonds. Cold temperature, on the other hand, slows down enzyme activity by decreasing molecular motion. In the monitored model the effect of temperature is important for the last three enzymes.Moreover the last three enzymes are produced on a specific temperatures to active the last three products reaction. These last three products are [http://en.wikipedia.org/wiki/Lycopene Lycopene], [http://en.wikipedia.org/wiki/Beta-carotene B-Carotene] and [http://en.wikipedia.org/wiki/Zeaxanthin Zaxanthin] which are presenting red, orange and yellow color in the environment.
As mentioned before for the enzymes production the hill type model was used. As a result, the temperature is the main parameter in enzyme production rate. Due to degradation which is dependent on the enzyme concentration after a while the enzyme is in a stable situation.
Lab experiments for estimating parameters
In the model, there are many parameters that were estimated arbitrary to have an initial calculation and got a feeling about the model. However to have a good model it is necessary to have a good estimation for the parameters. To find these estimation the modeling crew decided to use the results from the lab. It means that the results from lab were used to estimate parameters that not available exactly in databases. Two experiments have been designed for this procedure. The first one was an experiment for steady state situation which has been done by using Luciferase. In this experiment the enzyme activity has been measured for a specific temperature in the steady state situation.As this experiment has been done in steady state situation it was named "static". The second experiment designed to measure enzyme activity in changing situation. It means that the enzyme activities were measured in changing temperature in different time spans. As this experiment has been done in a changing situation it was named "dynamic". The results of both experiments are used to help the modeling crew to find a good estimation for parameters.
Parameter calculation
In the first step, the results from steady state situation were used to calculate the parameters. In steady state situation the enzyme concentration ratio is zero. Therefore from the lab results it is possible to derive a equation that has enzyme concentration for specific temperature and temperature as known and m, V, Kd and K as unknown. To make the life easier it is assumed that m=2 therefore V, Kd and K are unknowns which have to be found through the set of non linear equations. The next step is using the dynamic results from lab to do a dynamic modeling.
Bifurcation analysis
To have a stable system it is important to do a bifurcation analysis to find the stable ranges for different reaction parameters. This procedure has been done by defining the parameters and substrates concentration as symbolic values in Matlab. Afterwards by these symbolic values the reactions are defined in symbolic format. By these symbolic reactions a vector for reaction ratios for different substrates can be derived. Afterwards by applying a specific steady state, which has been derived from previous step but by applying the initial parameters that have been found from the databases, and changing the reactions parameters in the range that has been found from the [http://www.brenda-enzymes.info/ data base] different reaction vectors were obtained. The changes in the parameter ranges has been define by a random selection in a normal distribution between 0.001 to 0.0374. Subsequently, different vectors for reactions can be derived from this step. The [http://en.wikipedia.org/wiki/Jacobian Jacobian] applied on each vector where the derivations were respect to the substrate and product concentrations. To conclude the stability for each situation it is necessary that all the [http://en.wikipedia.org/wiki/Eigenvalue,_eigenvector_and_eigenspace eigenvalues] of each Jacobian matrix be smaller than zero. If the condition is satisfied then the reactions and pathways are in the stable situation. By this method it is possible to find an approximate ranges for the reaction parameters.
As the last three products are important and to make the life easier, a lumped model has been designed for the pathway. Two approaches has been used for this procedure. The first one was calculating all the substrates concentration on the base of the first substrate concentration. This approach makes the model too complicated therefore it has been ignored. The second approach was combining all the substrates and enzymes before Phytoene as a single reaction. It means there is a reaction that has the Acetyl-CoA as input and Phytoene. With this lumped model it is easier to calculate the stability and do the sensitivity analysis for the model.
This pathway has been modeled in Matlab and the bifurcation analysis has been done. The model has been defined in Matlab symbolic therefore by substituting the parameters, enzymes concentrations and product concentrations with numbers the stability can be derived. On the other hand the Jacobian matrix with respect to the products and substrates eigenvalues are always negative therefore it can be concluded that the pathway is always stable for the different values for parameters.
To do the sensitivity analysis on the model, the hill type equation has been implemented into the model. As a result the sensitivity of the system against the temperature has been studied in the model.
The next step is to find the coefficients of V and K for the both set of equations.
In the subtrate equations we have Vmax=Kcat . E0 where Kcat is the turnover number and E0 is the enzyme's initial concentration.
Experiment Vs Theory
... to be continued
