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Abstract

biological replicates more than 1000 curves Product inhibition, 75°C activity, many different things found out. kinetics modeling

Introduction

Enzyme kinetics is a widely studied field in biology as from the kinetic parameters one could make many different predictions about the preferences of a certain enzyme. Often knowledge about the structure of the enzymes reveals in models about the models for the kinetics of the enzyme. Our approach is the other way around. Often for extracting the enzyme kinetical parameters, the reaction rate is measured over a certain time and substrate concentration is varied. This would have been too much work for such a large screening and thus we decided to record the process curves for each lysozyme. From the ###link assays we have obtained over 1000 degradation curves from diferent kinds of lysozymes and want to make predictions about the thermal stability of the different enzymes. For nearly all of the ###10### different lysozymes not only two biological replicates from different inductions but also at least 4 technical replicates for each temperature the data was measured. Therefore a widespread approach has been made to extract the relevant information, starting with easy fitting of the data and ending with testing of different enzyme kinetics models, evaluation by profile likelihood analysis and in the end identifying the relevent parameters.

Lysozyme acting on M. lysodeicticus

As described in the linker-screening part we try to extract the loss of activity of $\lambda$-lysozyme due to heatshock, by observing the kinetic behavior on the degradation of M. lysodeikticus. The process that is finally making change in turbidity is very complex and has been widely discussed for more than 40 years now. On the other hand the activity of lysozyme is highly sensible on outer conditions as salt concentrations [-1] and the lysozyme concentration [0]. We have not only observed the non-enzymatic activity maximum of lysozyme described by Düring et al. [1] but also many observed effects can be explained by applying theory of product inhibition to the kinetics.[2] On the other hand lysozymes unfolding behavior from 37°C seems to be dominated by a rapid collapse when denaturating. [3] One of the main problems was that we could not define the amount of enzyme added to the reaction (fig. 1)( plot_of_3_axis2014_10_7_2.png ###Here one can easily see the effect of different enzyme concentrations added to the reaction). The effect of heat inactivation can be observed in (fig 2.) (plot_of_A_axis2014_10_7_2.png Different heatshock temperatures resulting in different kinetic behaviors. One can observe the changes in offset. These we could explain by product inhibition)

1. 1. 1. Theory about PLE, modeling###

Michaelis Menten theory

Michaelis Menten theory describes the catalytical behaviour of enzymes in simple reactions. It's basic reactions are assumed as

\[" E + S \, \overset{k_f}{\underset{k_r} \rightleftharpoons} \, ES \, \overset{k_\mathrm{cat}} {\longrightarrow} \, E + P "\] , with E the enzyme, S substrate, ES the enzyme-substrate complex and P the reaction product. $k_r, k_f and k_\mathrm{cat}$ are catalytical constants.  This means part of the enzyme is always bound in an enzyme substrate complex. This kinetic behavior can be simplified in the basic differential equation: \[\frac{d\left[S\right]}{dt} = \frac{- V _{max} \left[S\right]}{K_m + \left[S\right]} \]. V_{max} is the maximum reaction velocity, obtained from $V_{max} = k_{cat} * E$ and K_m being the michaelis-menten constant

Kompetitive product inhibition has the effect, that part of the Enzyme is also bound in the enzyme-product complex EP. This leads to an apparent increase of $K_m$ as: $K^\text{app}_m=K_m(1+[I]/K_i)$ Thus the differential equation changes as: \[\frac{d\left[S\right]}{dt} = \frac{- V _{max} \left[S\right]}{K_m \left( 1 + \frac{S_0 - S}{k_i} \right) + \left[S\right]} \] where $S_0$ means the substrate concentration at start of the reaction and $k_i$ an inhibitory constant.

Methods

In the beginning of the assays we needed to make certain calibrating measurements so that in the end we could model the enzyme kinetics, minimizing the influence of the measurement process.

Conditions

We established a standard protocol to process the protein mix, that is explained in the Linker_Screening part. It was stressed, that the reaction always took place at the same temperatures. Also another crucial part was the time after adding the enzyme to the substrate. This was minimized as good as possible and we tried to keep it constant. We always made the dilutions in buffer from the same stock, in order to keep salt concentrations fixed.

OD to concentration calibration

There was performed a measurement for calibrating the $OD_{600}$ to substrate concentration. We have seen that until a substrate concentration of 0.66 mg/ml in the 300 µl wells the behaviour is linear with an offset due to the protein mix and the well plate. We have concentrationdifferences result in an $OD_{600}$ difference of: $\delta \mathit{OD} = (1.160 +- 0.004 \frac {\mathtext{ml}} {\mathtext{mg}} * \delta \mathtext{concentration}}$. With this result one can easily calculate the concentration differences in each assay. Also the $OD_{600}$ of a well, where all the substrate was completely degraded needed to be measured. We found out, that the influence of the added protein mix on the $OD_{600}$ could be neglected.

Pipeting

One crucial part for the modeling is the time between when lysozyme was added to the substrate and the first measurement in the platereader. This was measured and assumed, that it nearly took the same time for each measurement with normally distributed errors. As the platereader took about 1s for measuring one well, this delay was also taken into account. ###Figure needed, where one can see the time delay###

Controls

We measured degradation curves for two different controls. One was E.coli lysate, processed in the same way as the protein mix, without any lysozyme expressed and the other was only the reaction buffer added to the substrate. We observed some slight decay in $OD_{600}$ in the curves, even if only potassium phosphate buffer was added. Nevertheless the curves of the non-lysozyme containing controls were always clearly distinguishable from samples, where lysozyme was in. Figure distinguish from lysozyme samples

PLE analysis

Often when fitting large models [10]

Final model

We have set up a model for the degradation of M. lysodeiktikus according to

Different models tested

-One model to whole data

  2 -kcat set to 1 for all
   3-KM, kcat, KI fixed for all temperatures
   4-KM, kcat, KI open for all temperatures
   5-E from Coomassies inserted
   

Model on single plate

  6 -VMax modeled, kI, KM open for all temperatures

Results

Figures:

1. Fits, Erklärung, dass unser Modell die Daten gut beschreibt

2. Profile likelihoods

3. Nichtidentifizierbarkeit von Parametern

4. Unsere interessanten Parameter

5 Leitmotive: Was wurde gemacht, warum wurde gemacht, wie wurde gemacht (kurz) Was ist rausgekommen.

resultsofscreening.png resultsaverageofscreening.png

Conclusion

The parameters that were interesting for us, were the decays in $V_{Max}$ with temperature of heat-shock. These were all identifiable for each plate.

Gels to fix enzyme concentration, and biological replicates -> kcat

Add from the beginning in different amounts -> $K_I$

Higher substrate concentrations -> $K_M$

The long way to the model

For long time we have thought it would be easy to extract the relevant data out of our lysozyme assays. But this though somehow perished one week before wiki freeze. For showing that science is always trying and failing, we wanted to explain how we came up with the upper model in the next part.

First try, easy fitting

The first thought when looking to the curves was that the reaction was clearly exponentially with some basal substrate decay and a small offset due to the different types of proteinmix added. The relevant parameter for us would be only the exponente which would be equal to some constant k times the enzyme concentration present. We would assume, that the constant doesn't change after heatshock, but the part of enzyme that survived. This assumption is based on a paper by Di Paolo et al., who claim that for pH denaturation of $\lambda$-lysozyme there are only two transition states, folded and unfolded. [3] This way curves for the temperature decay can be measured for each kind of lysozyme and finally compared to each other.

A basic problem of this method was, that it could never be excluded, that the temperature behaviour is not due to some initial concentration effects and that is why we chose to try Michaelis menten fitting, as in a perfect case, one could make an estimation on the amount of enzyme in the sample. As the exponential is just a special case of Michaelis Menten, one can always enlarge the model with this contribution.

Fitting Michaelis-Menten kinetics to the concentration data

1. 1. 1. Actually don't know, where to put that part, but want to keep it ###

As  we are screening different lysozymes in high-throughput we tried to use  the whole data obtained from substrate degredation over time by  applying integrated michaelis menten equation [4] But as  there is always an OD shift because of the plate and the cells lysate  we need to take this parameter into account while fitting.

The basic differential equation for Michaelis-Menten kinetics [5] is:

   \[\frac{d\left[S\right]}{dt} = \frac{- V _{max} \left[S\right]}{K_m + \left[S\right]} \]

Where $\left[S\right]$ means substrate concentration at time 0 or t respectively, $ V _{max}$ is the maximum enzyme reaction velocity, $K_m$ is Michaelis-Menten constant and t is time. This leads to:

   \[ \frac{K_m + \left[S\right]}{\left[S\right]}  \frac{d\left[S\right]}{dt} = -V_{max}\]

Which we can now solve by separation of variables and integration.

    \[ \int_{\left[S\right]_0}^{\left[S\right]_t} \left(\frac{K_m  }{\left[S\right]} + 1\right) d\left[S\right] = \int_{0}^{t}-V_{max}  dt'\]

This leads to,

   \[K_m \ln\left( \frac{\left[S\right]_t}{\left[S\right]_0} \right) + \left[S\right]_t - \left[S\right]_0  = -V_{max} t  \]

what we reform to a closed functional behaviour of time.

    \[t = - \frac{K_m \ln\left( \frac{\left[S\right]_t}{\left[S\right]_0}  \right) + \left[S\right]_t - \left[S\right]_0 } {V_{max}}  \]

As the functional behaviour is monotonous we can just fit this function to our data, which should directly provide us with $V_max$ which is the interesting parameter for us.

As OD in the range where we are measuring still is in the linear scope with some offset due to measurement circumstances and the absorption of the cells lysate we can use $\left[S\right] = m OD + a$, where a is the offset optical density, when all the substrate has been degraded, OD is the optical density at 600 nm and m is some parameter that needs to be calibrated.

So we can refine the functional behaviour as:

    \[t = - \frac{K_m \ln\left( \frac{ m ({\mathit{OD}}_t - a)}{ m  (\mathit{OD}_0 - a)} \right) +  m \mathit{OD}_t -  m \mathit{OD}_0 }  {V_{max}} \]

$OD_0$ is just the first measured OD we get, this parameter is not fitted.

But these fits did completely not converge so we needed to find another solution. Liao et al. proposed and compared different techniques for fitting integrated Michaelis-Menten kinetics, [7] which didn't work out for us, because starting substrate concentration was too low for us and thus the fits converged to negative $K_m$ and $V_Max$. Finally we fitted Michaelis-Menten kinetics using the method proposed by Goudar et al. [6] by directly fit the numerically solved equation, using lambert's $\omega$ function, which is the solution to the equation $ \omega (x) \exp (\omega(x)) = x$. So we fitted

\[ \left[S\right]_t = K_m \omega \left[ \left( \left[A\right]_0 / K_m \right) \exp \left( \left[A\right]_0 / K_m -V_{max} t / K_m \right) \right] \]

This worked well, the fits converged reliably, but sometimes produced huge errors for $K_m$ and $V_Max$ of the order of $10^5$ higher than the best fit for these values. This simply meant, that from most data, these parameters could not be identified. On the other hand simple exponential fit reproduced the data nearly perfectly, which made us concluding, that we're just working in the exponential regime, because $K_m$ is just much too high for the substrate concentrations we're working with, so that the differential equation from the beginning ###link### would transform into:

\[\frac{d\left[S\right]}{dt} = - V _{max} \left[S\right] \]

which is solved by a simple exponential equation

\[ \left[S\right]_{t} = \left[S\right]_0 e^{\left( - V_{max} t \right)} \]

As we're measuring OD function fitted to the data results in:

\[ \mathit{OD}_{t} = \left(\mathit{OD}_0 - a\right) e^{\left( - V_{max} t \right)} + a \]

with a a parameter for the offset in OD due to the plate and the proteinmix.

This method seemed to be the method of choice, as it also produced nice results. We have written a python skript [ ???Link???] that handled all the data, the plotting and the fitting and in the end produced plots with activities normalized to the 37°C activity. These results though had too large errorbars, so we tried to set up a framework to fit multiple datasets in one, with different parameters applied to different datasets. We chose to work with the widely used d2d arFramework developed by Andreas Raue [8] running on MATLAB. As all the datahandling had already happened in python we appended the script with the generation of work for the d2d framework, so that our huge datasets could be fitted at once. The fitting worked out quite well, but some strange results could not be explained yet with that.

Modeling product inhibition

We observed many different phenomena we could not explain properly. For example when the activity at 37°C started low, it seemed, that the protein doesn't loose it's activity after heatshock ###figure needed###. This meant that there was some kind of basal activity, independent of the enzyme concentration. On the other hand activity was not completely linear to enzyme concentration. But the most inexplicable part was, that some samples even after 1h of degradation stayed constant at an $OD_{600}$ level, nearly as high as the starting $OD_{600}$. This could only be due to the substrate not being degraded, so we checked this by adding fresh lysozyme to the substrate. We observed another decay in $OD_{600}$, which clearly meant, that not the substrate ran out, but the enzyme somehow lost activity during measurement. This meant, that our basic assumption from above was completely wrong and the results completely worthless, as we are only detecting a region of the kinetics, where already some enzyme has been lost due to inhibition. But therefore nothing about initial enzyme concentration in the sample could be said. We even found this based in a paper from 1961 written in french [2].

Grand model

We then tried to always fit one grand model to all the data we have obtained from all the different assays, with curves for different temperatures, biological replicates and technical replicates. In total these were about 100 000 data points we feeded in and up to 500 parameters we fitted. This did not work out, because the variation in starting amounts of enzyme was too large even between the technical replicates from different days. This might be due to the freeze thaw cycles, that the enzyme stock was subdued to. On the other hand this model was just way too complex to be handled easily, as it took hours only for the initial fits. Calculating the profile likelihoods took about one day. Therefore we chose to take another approach, always modeling the data of one single plate, as on that for sure the variations were much less. Of course thus different parameters would not be identifiable, for example the enzyme concentration would not be comparable between the different samples. On the other hand, the only parameters, that are interesting for our purpose, the bahavior after heatshock would still be identifiable.

References

[-1] Mörsky, P. Turbidimetric determination of lysozyme with Micrococcus lysodeikticus cells: reexamination of reaction conditions. Analytical biochemistry 128, 77-85 (1983).

[0] Friedberg, I. & Avigad G. High lysozyme concentration and lysis of Micrococcus lysodeikticus, Biochim. Biophys. Acta, 127 (1966) 532-535

[1] Düring, K., Porsch, P., Mahn, A., Brinkmann, O. & Gieffers, W. The non-enzymatic microbicidal activity of lysozymes. FEBS Letters 449, 93-100 (1999).

[2] Colobert, L. & Dirheimer G. Action du lysozyme sur un substrat glycopeptidique isolé du micrococcus lysodeiktikus. B1OCHIMICA ET BIOPHYSICA ACTA, 54, 455-468 (1961)

[3] Di Paolo, A., Balbeur, D., De Pauw, E., Redfield, C. & Matagne, A. Rapid collapse into a molten globule is followed by simple two-state kinetics in the folding of lysozyme from bacteriophage λ. Biochemistry 49, 8646-8657 (2010).

[4] Hommes, F. A. "The integrated Michaelis-Menten equation." Archives of biochemistry and biophysics 96.1 (1962): 28-31.

[5] Purich, Daniel L. Contemporary Enzyme Kinetics and Mechanism: Reliable Lab Solutions. Academic Press, 2009.

[6] Liao, Fei, et al. "The comparison of the estimation of enzyme kinetic parameters by fitting reaction curve to the integrated Michaelis–Menten rate equations of different predictor variables." Journal of biochemical and biophysical methods 62.1 (2005): 13-24.

[7] Goudar, Chetan T., Jagadeesh R. Sonnad, and Ronald G. Duggleby. "Parameter estimation using a direct solution of the integrated Michaelis-Menten equation." Biochimica et Biophysica Acta (BBA)-Protein Structure and Molecular Enzymology 1429.2 (1999): 377-383.

[8] Raue, A. et al. Lessons Learned from Quantitative Dynamical Modeling in Systems Biology. PLoS ONE 8, (2013).

[9] Raue, a et al. Structural and practical identifiability analysis of partially observed dynamical models by exploiting the profile likelihood. Bioinformatics 25, 1923–9 (2009).

[10] Raue, A. et al. Lessons Learned from Quantitative Dynamical Modeling in Systems Biology. PLoS ONE 8, (2013).