About Image

Objectives

Our model has several objectives as follows:
1. Test the plausibility of the design of one-cell production of tyrian purple. By combining design of a novel ligand-gated repressor involved in enzyme production control through directed evolution and product protection measures through glycosylation and deglycosylation, we demonstrated the feasibility of using one-cell system to produce relatively purified tyrian purple at an industrial scale.
2. Interpret and guide the experimental process. We continuously revised the model using experimental data and again compared the results predicted by the model with the data obtained experimentally. For example, in the model, we expect to understand the effect of different efficiencies of tryptophan repressor (TrpR) binding with tryptophan (Trp) and bromotryptophan (6-Br-W) on the final product by modeling. We used the experimental data to correct the parameters. Finally we gave feedback to our experiment part of analysis of the combination efficiency.


Design

Here we present the design of the most important Trp repressor (TrpR) for the realization of one-cell systems. TrpR undergoes transcription, mRNA of TrpR translation and Trp dimerization eventually forming a dimer TrpR2. The directionally evolved TrpR2 can only inhibit the reaction concerning tryptophan (Trp), but not Br-Trp. The dimeric forms of TrpR2 each have a Trp binding site. After binding to Trp, TrpR2 undergoes conformational change and binds to the operational sequence of the Trp promoter, repressing gene expression of TnaA-FL-FMO (TLF) (Figure 1). Only when all tryptophan in solution is halogenated to bromotryptophan (6-Br-Trp), TLF is translated and catalyzes 6-Br-Trp for the next reaction (Figure 2).

Blog One Blog One

Model

Reaction I: Bromination of tryptophan

Tryptophan (Trp) is converted to bromotryptophan (Br-Trp) by the action of Trp halogenase Fre-L-SttH, which follows Michaelis-Menten kinetics. Hence, the rate of Br-Trp synthesis from Trp is represented by equation (1):


$$ \frac{\text{d}\left[ Br-Trp \right]}{\text{dt}}=\frac{V_{Br}\left[ Trp \right]}{K_{Br}+\left[ Trp \right]} $$

where [Br-Trp] and [Trp] represent the concentrations of bromotryptophan and tryptophan, respectively; \(K_Br\) is the Michaelis-Menten constant of Fre-L-SttH.


Since Br-Trp is oxidized to Br-Indo by Michaelis-Menten enzyme TnaA-FL-FMO (TLF), equation (1) is corrected by adding a consumption term:


$$ \frac{\text{d}\left[ Br-Trp \right]}{\text{dt}}=\frac{V_{Br}\left[ Trp \right]}{K_{Br}+\left[ Trp \right]}-\frac{V_{TLF}\left[ Br-Trp \right] \left[ TLF \right]}{K_{TLF}+\left[ Trp \right]} $$

where [TLF] is the concentration of TnaA-FL-FMO; \(K_TLF\) is the Michaelis-Menten constant of TnaA-FL-FMO.


On the other hand, Trp is consumed by Fre-L-SttH catalyzed bromination reaction and TLF-catalyzed oxidation reaction. Trp consumption rate is represented in equation (3):


$$ \frac{\text{d}\left[ Trp \right]}{\text{dt}}=-\frac{V_{Br}\left[ Trp \right]}{K_{Br}+\left[ Trp \right]}-\frac{V_{TLF}\left[ Trp \right] \left[ TLF \right]}{K_{TLF}+\left[ Trp \right]} $$
Reaction II TrpR synthesis

The synthesis process of tryptophan repressor (TrpR2) is divided into three steps: transcription, translation and dimerization.
Equation (4) represents the transcription process of TrpR2. [\(mRNA_{Trp-R}\)] is the concentration of mRNA of TrpR2. k_TC1 is the transcription rate of TrpR2 and k_DegM is the rate of mRNA degradation.


$$ \frac{\text{d}\left[ mRNA_{TrpR} \right]}{\text{dt}}=k_{TC1}DNA_{TrpR}-k_{DegM}\left[ mRNA_{TrpR} \right] $$

Equation (5) represents the translation process of TrpR2. k_TL1 is the rate of TrpR2 translation and k_DegP is the rate of protein degradation.


$$ \frac{\text{d}\left[ TrpR \right]}{\text{dt}}=k_{TL1}\left[ mRNA_{TrpR} \right] -k_{DegP}\left[ TrpR \right] $$

In addition to this, TrpR monomer concentration decreases due to dimerization while increases due to TrpR2 monomerization. Therefore, correcting the above equation, we obtain the equation describing TrpR translation as


$$ \frac{\text{d}\left[ TrpR \right]}{\text{dt}}=k_{TL1}\left[ mRNA_{TrpR} \right] -k_{DegP}\left[ TrpR \right] -k_{Di}\left[ TrpR \right] ^2+k_{Sepe1}\left[ TrpR2 \right] $$

where k_Di is the parameter for TrpR dimerization and k_Sepe1 is the TrpR2 separation number.


The third equation is used to describe the dimerization process and represents the concentration of TrpR2. Firstly, as mentioned above, TrpR2 undergoes dimerization and separation.


$$ \frac{\text{d}\left[ TrpR2 \right]}{\text{dt}}=k_{Di}\left[ TrpR \right] ^2-k_{Sepe1}\left[ TrpR2 \right] $$

In addition, by binding to Trp or Br-Trp, TrpR2 can form TrpR2-Trp (binding to two Trp) or TrpR2-BT (binding to two Br-Trp) , while Trp2-Trp , TrpR2-BT can both repress the transcription process of TLF. where k_AR_T is the association rate of TrpR2 and Trp. Therefore, we corrected the equation as follows:


$$ \frac{\text{d}\left[ TrpR2 \right]}{\text{dt}}=k_{Di}\left[ TrpR \right] ^2-k_{Sepe1}\left[ TrpR2 \right] -k_{AR\_T}\left[ TrpR2 \right] \left[ Trp \right] ^2-k_{AR\_BT}\left[ TrpR2 \right] \left[ Br-Trp \right] ^2 $$

Since TrpR2-Trp, and TrpR2-BT also dissociate and thus affect the concentration of TrpR2, we added the last term and obtained the final equation describing the concentration of TrpR2:


$$ \frac{\text{d}\left[ TrpR2 \right]}{\text{dt}}=k_{Di}\left[ TrpR \right] ^2-k_{Sepe1}\left[ TrpR2 \right] $$
Reaction III TrpR binding to Trp, Br-Trp

Dimerization leads to a conformational change of active site of each TrpR, enabling each monomer to bind to a molecule of either Trp or Br-Trp. Assuming that TrpR2 can bind with one type of molecule one time, hence TrpR2 can bind to two Trp or Br-Trp molecules, forming TrpR2-Trp or TrpR2-BT (Figure 3).


$$ \left[ TrpR2 \right] +2\left[ Trp \right] \left[ TrpR2-T \right] $$
$$ \left[ TrpR2 \right] +2\left[ Br-Trp \right] \left[ TrpR2-TB \right] $$
Blog One

Considering both association and dissociation of between TrpR2 and Trp or between TrpR2 and Br-Trp, we have the following equation:


$$ \frac{\text{d}\left[ TrpR2-Trp \right]}{\text{dt}}=k_{AR\_T}\left[ TrpR2 \right] \left[ Trp \right] ^2-k_{sepe2}\left[ TrpR2-Trp \right] $$ $$ \frac{\text{d}\left[ TrpR2-TB \right]}{\text{dt}}=k_{AR\_BT}\left[ TrpR2 \right] \left[ Br-Trp \right] ^2-k_{sepe2}\left[ TrpR2-TB \right] $$

Where the association and the dissociation rate of between TrpR2 and Trp (or between TrpR2 and Br-Trp) are k_AR_T (or k_AR_BT) and k_sepe2 respectively.


While during the formation of TrpR2-Trp or TrpR2-BT, the association between TrpR2 and Trp or Br-Trp only takes place when the Trp or Br-Trp concentration reaches a certain range. Therefore, a constant term [Trp_0] or [Br-Trp_0] is added. Hence we get the corrected equations:


$$ \frac{\text{d}\left[ TrpR2-T \right]}{\text{dt}}=k_{AR\_T}\left[ TrpR2 \right] \frac{\left[ Trp \right] ^2}{\left[ Trp \right] ^2+\left[ Trp_0 \right] ^2}-k_{sepe2}\left[ TrpR2-Trp \right] $$ $$ \frac{\text{d}\left[ TrpR2-TB \right]}{\text{dt}}=k_{AR\_BT}\left[ TrpR2 \right] \frac{\left[ Br-Trp \right] ^2}{\left[ Br-Trp \right] ^2+\left[ Br-Trp_0 \right] ^2}-k_{sepe2}\left[ TrpR2-TB \right] $$
Reaction IV TLF transcription

As mentioned before, TLF refers to TnaA-FL-FMO, which catalyzes Reaction V presented at the following part. The transcription function of TLF is shown as follows:


$$ \frac{\text{d}\left[ mRNA_{TLF} \right]}{\text{dt}}=k_{TC2}DNA_{TLF}-k_{DegM}\left[ mRNA_{TLF} \right] $$

When two molecules of Trp or Br-Trp are bound to TrpR2, TrpR2’s repression activity becomes activated. Trp-bound or Br-Trp-bound TrpR2 binds to the promoter of TLF and represses TLF transcription. Assuming that the repression efficiency of TrpR2-Trp and TrpR2-BT is the same, the transcription efficiency could be modified by a gene expression repression efficiency term (equation 17). Repression efficiency follows a Hill equation in relation to repressor concentration.


$$ \frac{\text{d}\left[ mRNA_{TLF} \right]}{\text{dt}}=\frac{k_{TC2}}{1+\left( \frac{\left[ TrpR2-T \right] +\left[ TrpR2-TB \right]}{K_{Hill}} \right) ^n}DNA_{TLF}-k_{DegM}\left[ mRNA_{TLF} \right] $$

Finally, the amount of TLF is described in the following ODE equation, where k_TL2 and k_DegP are the parameter of TLF translation and TLF degradation respectively.


$$ \frac{\text{d}\left[ TLF \right]}{\text{dt}}=k_{TL2}\left[ mRNA_{TLF} \right] -k_{DegP}\left[ TLF \right] $$
Reaction V TLF-catalyzed substrate

TLF indicates TnaA-Flexible Linker-FMO, which can catalyze Br-Trp transforming to Br-Indole in our design. As one of the by-products, indigo can be transformed from Trp by TLF. In equation (19), [I] represents the concentration of indigo. We also used Michaelis-Menten equation to model the production of indigo, where V_TLF1 is the rate of indigo production at which TLF is saturated with Trp and K_TLF1 is the Michaelis-Menten constant of TLF.


$$ \frac{\text{d}\left[ I \right]}{\text{dt}}=\frac{V_{TLF1}\left[ Trp \right] \left[ TLF \right]}{K_{TLF1}+\left[ Trp \right]} $$

The main function of TLF is to catalyze Br-Trp to transform to Br-Indole, which is the precursor of our target product TP-Indican.


$$ \frac{\text{d}\left[ Br-Indo \right]}{\text{dt}}=\frac{V_{TLF2}\left[ Br-Trp \right] \left[ TLF \right]}{K_{TLF2}+\left[ Trp \right]} $$

Taking the consumption of Br-Indole into consideration, Br-Indole is transformed to TP-Indican by UGT, the enzyme that add a glucose moiety to tyrian purple as a biochemical protecting group. The equation (20) is modified as follows:


$$ \frac{\mathrm{d}\left[ Br-Indo \right]}{\mathrm{dt}}=\frac{V_{TLF2}\left[ Br-Trp \right] \left[ TLF \right]}{K_{TLF2}+\left[ Trp \right]}-\frac{V_{UGT}\left[ Br-Indo \right]}{K_{UGT}+\left[ Br-Indo \right]}-k_{O_2}\left[ Br-Indo \right] ^2 $$
Reaction VI UGT-catalyzed competition with O2

The final reaction is about the production of our target product Br-Indi, which is catalyzed from Br-Indo by the enzyme UTG in equation (23). With the formation of Br-Indi, the byproduct TP which denotes the unmodified insoluble tyrian purple will also be producted as shown in equation (22).


$$ \frac{\text{d}\left[ TP \right]}{\text{dt}}=k_{O_2}\left[ TP-Indo \right] ^2 $$ $$ \frac{\text{d}\left[ TP-Indi \right]}{\text{dt}}=\frac{V_{UGT}\left[ Br-Indo \right]}{K_{UGT}+\left[ Br-Indo \right]} $$

Outcome

Results

We used the "deSolve" package in R to solve the above equations for the one-cell production of tyrian purple reaction and “ggplot2” package to visualise the time-dynamics of proteins and compounds of interest.
Blog One Blog One Blog One

According to Figure 3.4A, in the initial stage of the reaction, TrpR is continuously produced and reaches saturation (0-36h) at 18μm. TrpR dimerization occurs alongside TrpR production and TrpR2 reaches saturation of about 9μm at also at around 36h.


In the early stage when the Trp content is high, TrpR2 binds with two molecules of Trp to form TrpR2-Trp rapidly and reaches the peak point (5μm) at 23h. At 24h, after most of Trp is converted to Br-Trp, a few amount of Trp become available for TrpR2 to bind with, while Trp dissociation from TrpR2 still occurs. Therefore, TrpR2-Trp concentration gradually declines and becomes negligible at around 36h.


With relatively little amount of TrpR2-Trp repressor available in the beginning (0-2h), TLF is rapidly translated and peaked (14 μm).As TrpR2-Trp gradually accumulates after 2h, the TLF gene expression becomes inhibited, which subsequently leads to a decline in TLF concentration. Finally, with the depletion of TrpR2-Trp at around 36h, TLF expression restores and TLF gradually accumulates.


According to Figure 3.4B, Trp gradually decreases from the beginning and reduces almostly to 0 at 36h from the consumption by Fre-F-SttH and TnaA-FL-FMO. While the 6-Br-Trp concentration increases continuously and reaches a plateau of roughly 2400 μm before being consumed by TnaA-FL-FMO (TLF).


As for Figure 3.4C, Br-Indo and Br-Indi (our target product) accumulation follows the dynamics of TLF, the enzyme that catalyses their production. Initial accumulation of TLF before around 13h leads to production of Br-Indi to a level of 120μm, while subsequent TLF accumulation after depletion of Trp2-Trp raises Br-Indi to around 2300μm. During the whole process, little by-product TP (tyrian purple without modified) is producted.

Sensitivity Analysis

We use the package "Pheatmap" in R to describe the effect of the difference in the rate of binding of TrpR2 to Trp, Br-Trp and the target product product Br-Indi with the by-product TP. As is discussed before, the binding rate has great influence on the yield of our target product Br-Indi. Hence we apply the method of sensitivity analysis to quantify how much it is affected. To standardize the influence, we use the ratio of target-product/byproduct amount.


We define:
ratio1=log ( Br-Indi/Br-Trp), indicating the relative output of the target products Br-Indi and Br-Trp.
ratio2=log ( Br-Indi/Indo), denoting the relative output of the target products Br-Indi and Indo.


Blog One Blog One

According to Figure 5A, the binding efficiency of TrpR2 with Trp has relatively little effect on the final defined Ratio1. When the binding efficiency of TrpR2 with Br-Trp is less than 5*10^3, the final value of Ratio1 is greater than 10^3. However, when the binding efficiency is greater than 5*10^-3, the final value of Ratio1 is less than 10^1.


According to Figure 5B, when the binding efficiency of TrpR2 with Br-Trp is greater than 10^-2, the value of ratio2 is less than 1, representing that the products have similar amounts of Indo and Br-Indo; when the binding efficiency of TrpR2 with Br-Trp is less than 10^-2, the value of ratio2 is greater than 1, representing that the products have similar amounts of Indo and Br-Indo; TrpR2 When the binding efficiency between TrpR2 with Br-Trp is less than 10^-2, the value of ratio2 is greater than 1, and along with the increase of the binding efficiency between TrpR2 and Trp, the value of ratio2 increases continuously, which represents the increasing amount of Br-Indo in the product.


The effect of kO2 on the productivity

\(k_{O2}\) denotes the oxygen reaction rate with indoxy and 6-Br-trp Indoxy, which functions as a parameter in Model-Fermentation Reaction VI, equation (22) shown below.


$$ \frac{\text{d}\left[ TP \right]}{\text{dt}}=k_{O_2}\left[ TP-Indo \right] ^2 $$
Blog One

To standardize the productivity of Br-Indi, we construct the ratio:
Ratio=log(Br-Indi/Tp).
We plot in Figure 5 how ratio changes with the value of k_O2. And it is found out that as k_O2 increasing, the productivity of Br-Indi goes up along with it.


Discussion

One-cell reaction

As shown in the Figure 4C, our model demonstrates that the one single-cell system is capable of producing relatively pure tyrian purple. At the beginning of the reaction, the system is rapidly saturated with Trp and Trp2, and the presence of Trp2-Trp inhibits the expression of TnaA-FL-Fmo (TLF) when large amounts of Trp are present. However, when Trp2-Trp is gradually depleted, TLF is expressed normally.

In order to reduce the production of Indo and increase the concentration of the final product, we need to saturate TrpR and TrpR2 in the single-cell reaction system before the reaction starts, and the polymer of TrpR2 and Trp is formed rapidly, thus reducing the production of Indo at the initial moment due to TLF expression; at the same time, we need to increase the rate of degradation of the polymer of TrpR2 and Trp, and thus rapidly start the transcription and translation of TLF.


The differential rate of binding between Br-Trp and Trp/Br-Trp

Also, in order to calculate the effect of different TrpR2 binding rates to Trp, Br-Trp, we quantitatively analyzed the ratio1 and ratio2. we combined the two heat maps and quantitatively obtained that in order to ensure the purity of the product as well as to proceed properly, we need to increase the binding efficiency of TrpR2 to Trp (greater than 10^-2), and the larger the value, the better the result. Also keeping the binding efficiency of TrpR2 to Trp at a lower level.


The effect of kO2 on the productivity

As shown in the Figure 4C, our model demonstrates that oxygen concentration ‘s influence (directly related ot the reaction rate with Indoxyl and 6-Br-Trp) on the final production. As oxygen concentration increase, the product Br-Indi that we want, its purity still increase. It tells us to keep our fermentation process anaerobic or hypoxia in order to increase final product’s purity.