Difference between revisions of "Team:Macquarie Australia/Modeling"

(Added the contentcontainer class back in)
 
(26 intermediate revisions by 4 users not shown)
Line 6: Line 6:
 
<body>
 
<body>
  
 
+
<div class="contentContainer">
  
 
<div class="centreStuffInline">
 
<div class="centreStuffInline">
<figure class="specialInline"><img src="https://static.igem.org/mediawiki/2015/7/71/MqAust_2Modelling_v05a-150dpi.png" width="220px" alt="Modelling page"></figure>
+
<img src="https://static.igem.org/mediawiki/2015/5/5b/NDModellingHead.jpeg">
 
</div>
 
</div>
  
Line 17: Line 17:
 
</div>
 
</div>
  
<h5> Basic Principle- </h5>
+
<h1> ALA to PPIX </h1>
 +
 
 +
<h4> Basic Principle </h4>
 
<p>
 
<p>
 
One of the aims of this project was to re-engineer <i> E.coli </i> to produce chlorophyll a which <i> E.coli </i> does not naturally produce. It produces heme which shares the same precursor as a chlorophyll a, Protoporphyrin IX (PPIX) (figure 1) (Willows, 2004). The PPIX pathway begins from aminolevulinic acid (ALA), which is produced naturally in <i> E.coli </i> but can be also be added to increase the production of PPIX (Willows, 2004). </p> </br>
 
One of the aims of this project was to re-engineer <i> E.coli </i> to produce chlorophyll a which <i> E.coli </i> does not naturally produce. It produces heme which shares the same precursor as a chlorophyll a, Protoporphyrin IX (PPIX) (figure 1) (Willows, 2004). The PPIX pathway begins from aminolevulinic acid (ALA), which is produced naturally in <i> E.coli </i> but can be also be added to increase the production of PPIX (Willows, 2004). </p> </br>
Line 27: Line 29:
 
<p> Fig 1: Biosynthetic pathway from ALA to the first coloured intermediate protoporphyrin IX. a. ALA dehydratase; b. porphobilinogen deaminase; c. uroporphyrinogen III synthase; d. uroporphyrinogen decarboxylase; e. coproporphyrinogen oxidase; f. protoporphyrinogen oxidase (Willows, 2004)
 
<p> Fig 1: Biosynthetic pathway from ALA to the first coloured intermediate protoporphyrin IX. a. ALA dehydratase; b. porphobilinogen deaminase; c. uroporphyrinogen III synthase; d. uroporphyrinogen decarboxylase; e. coproporphyrinogen oxidase; f. protoporphyrinogen oxidase (Willows, 2004)
 
.</p> </br>
 
.</p> </br>
<p> Our initial aim was to model the pathway from ALA to PPIX in native E. coli cells to determine what concentration of ALA would give us the optimal yield of PPIX. Ultimately, we plan to model the entire Chlorophyll a biosynthesis pathway, and the production of H2 gas (link to PSII model). </p> </br>
+
<p> Our initial aim was to model the pathway from ALA to PPIX in native E. coli cells to determine what concentration of ALA would give us the optimal yield of PPIX. Ultimately, we plan to model the entire Chlorophyll a biosynthesis pathway, and the production of H2 gas. </p> </br>
<h5> Mathematical Model Overview- </h5>
+
<h4> Mathematical Model Overview- </h4>
 
<p> Michaelis-­Menten type enzyme kinetics were studied first prior to establishing appropriate parameters from reported literature to propose our models. The adopted kinetic equation was then used to determine enzyme concentration through first-hand experiments and then fedback on our model which contains an arbitrary amount of enzyme concentrations.</p>
 
<p> Michaelis-­Menten type enzyme kinetics were studied first prior to establishing appropriate parameters from reported literature to propose our models. The adopted kinetic equation was then used to determine enzyme concentration through first-hand experiments and then fedback on our model which contains an arbitrary amount of enzyme concentrations.</p>
 
</br> <div class="centreStuffInline">
 
</br> <div class="centreStuffInline">
Line 35: Line 37:
 
<p>The initial velocity of the reaction (V<sub>i</sub>) directly depends on the rate of the conversion of ES to P. It is also dependent on the total enzyme concentration (Keleti & Kramer, 1986). By using the following formula, the total enzyme concentration can be determined from the experimental values of V<sub>i</sub> and S, which also corresponds to initial ALA concentration. (Keleti & Kramer, 1986) </p>   
 
<p>The initial velocity of the reaction (V<sub>i</sub>) directly depends on the rate of the conversion of ES to P. It is also dependent on the total enzyme concentration (Keleti & Kramer, 1986). By using the following formula, the total enzyme concentration can be determined from the experimental values of V<sub>i</sub> and S, which also corresponds to initial ALA concentration. (Keleti & Kramer, 1986) </p>   
 
                                                        
 
                                                        
<h5> Our Model </h5>
+
<h4> Our Model </h4>
 
<p> Abbreviations used   
 
<p> Abbreviations used   
 
<ul>
 
<ul>
Line 53: Line 55:
  
  
<p> In our modelling experiment, the initial concentration of ALA, [ALA]<sub>0</sub>, was used as a known independent variable while initial enzyme concentration, [E]<sub>0</sub>,  was used as a dependent variable . We assumed that all the substrates and products had a concentration of 0 at time 0 sec (t=0). [ALA]<sub>0</sub> was varied from 1mM to 5mM to 10 mM to 20mM. [E]<sub>0</sub> was arbitrarily chosen in a realistic interval of 0.1 µM to 1 µM. This is the natural concentration of enzyme seen in <i> E.coli </i>. For this first model, we assume that there would be no inhibition of any enzymatic activity and that ALA would only be converted to PPIX only follows this biosynthesis pathway.</p> </br>
+
<p> In our modelling experiment, the initial concentration of ALA, [ALA]<sub>0</sub>, was used as a known independent variable while initial enzyme concentration, [E]<sub>0</sub>,  was used as a dependent variable . We assumed that all the substrates and products had a concentration of 0 at time 0 sec (t=0). [ALA]<sub>0</sub> was varied from 1mM to 5mM to 10 mM to 20mM. [E]<sub>0</sub> was arbitrarily chosen in a realistic interval of 0.1 µM to 1 µM. This is the natural concentration of enzyme seen in <i> E.coli </i>. For this first model, we assume that there would be no inhibition of any enzymatic activity and that ALA would only be converted to PPIX only and it only follows this biosynthesis pathway shown below.</p> </br>
<h5> First model </h5>
+
<h4> First model </h4>
 
<p> In this model we considered the following reaction for ALA to PPIX transformation: </br> </p>
 
<p> In this model we considered the following reaction for ALA to PPIX transformation: </br> </p>
 
<img src= "https://static.igem.org/mediawiki/2015/1/1f/MQAUST_P3.png">
 
<img src= "https://static.igem.org/mediawiki/2015/1/1f/MQAUST_P3.png">
  
 
 
 
<div class="centreStuffInline">  
 
<div class="centreStuffInline">  
<img src= "https://static.igem.org/mediawiki/2015/8/8a/MQAUST_25.png">
+
<img src= "https://static.igem.org/mediawiki/2015/b/b4/MQAUST_P250.png">
 
</div>
 
</div>
  
Line 77: Line 77:
 
</div>
 
</div>
 
<p> Graph 2: This consists of graph 1 zoomed in to view the change in concentration of the intermediates involved  at the initial stage of the reaction. PPB was the first intermediate produced, thus it appeared first and began to decrease as HMB was produced. As Uroporphyrinogen III synthase has a very high Kcat (500/s) , URO production from HMB was almost instant, hence, HMB was rapidly consumed. </p> </br>
 
<p> Graph 2: This consists of graph 1 zoomed in to view the change in concentration of the intermediates involved  at the initial stage of the reaction. PPB was the first intermediate produced, thus it appeared first and began to decrease as HMB was produced. As Uroporphyrinogen III synthase has a very high Kcat (500/s) , URO production from HMB was almost instant, hence, HMB was rapidly consumed. </p> </br>
<p> From this, we performed a preliminary experiment with measurements at time intervals of 5, 10, 20, 30, 60 and 120 minutes. However, no brown coloured solution was observed to indicate PPIX formation, which was further verified by nanodrop absorbance readings. </p> </br>
+
<p> Based on this, we performed a preliminary experiment with measurements at time intervals of 5, 10, 20, 30, 60 and 120 minutes. However, no brown coloured solution was observed to indicate PPIX formation, which was further verified by nanodrop absorbance readings. </p> </br>
 
<p>Based on this, we constructed a second model taking into account the intermediates consisting of enzyme complexes. </p> </br>
 
<p>Based on this, we constructed a second model taking into account the intermediates consisting of enzyme complexes. </p> </br>
<p> In order to quantify the number of enzymes involved in the ALA to PPIX pathway, we measured the concentrations for each of the pathway’s intermediates. </p> </br>
+
<p> In order to estimate the quantities of the enzymes involved in the ALA to PPIX pathway, we measured the concentrations for each of the pathway’s intermediates. </p> </br>
  
 
<p>The E. coli cultures were grown overnight with shaking at 300 rpm at 37°C. The cells were harvested by centrifugation, supernatant discarded. The cells were resuspended in 5 mL of 0.1 mM glucose in 1 mM ALA, then incubated in the dark for up to 14 days. Approximately 250 uL of cells were extracted each time over 24 hour intervals, and lysed with lysis buffer and neutralized with neutralization buffer (Sigma plasmid prep kit). The precipitates were separated by centrifugation for 10 mins, and the absorbance of the supernatant measured with the nanodrop (Thermoscientific Nanodrop 2000 spectrophotometer). The absorbance maxima of PPIX is 404 nm. </p> </br>
 
<p>The E. coli cultures were grown overnight with shaking at 300 rpm at 37°C. The cells were harvested by centrifugation, supernatant discarded. The cells were resuspended in 5 mL of 0.1 mM glucose in 1 mM ALA, then incubated in the dark for up to 14 days. Approximately 250 uL of cells were extracted each time over 24 hour intervals, and lysed with lysis buffer and neutralized with neutralization buffer (Sigma plasmid prep kit). The precipitates were separated by centrifugation for 10 mins, and the absorbance of the supernatant measured with the nanodrop (Thermoscientific Nanodrop 2000 spectrophotometer). The absorbance maxima of PPIX is 404 nm. </p> </br>
  
<h5> Second Model- </h5>
+
<h4> Second Model- </h4>
 
<p> When the intermediates (enzyme complexes) were added, the following reactions were obtained: </p> </br>
 
<p> When the intermediates (enzyme complexes) were added, the following reactions were obtained: </p> </br>
 
<div class="centreStuffInline">
 
<div class="centreStuffInline">
Line 109: Line 109:
 
<p> Graph 3: This graph was obtained using 1mM [ALA]<sub>0</sub> and 0.1 µM as initial enzyme concentrations. [PPIX] reached its peak after approximately 7 days. From our first experiment, a significant concentration of PPIX was observed after 1 week, and peaked after another 7 days (shown in experimental part). </p> </br> </br>  
 
<p> Graph 3: This graph was obtained using 1mM [ALA]<sub>0</sub> and 0.1 µM as initial enzyme concentrations. [PPIX] reached its peak after approximately 7 days. From our first experiment, a significant concentration of PPIX was observed after 1 week, and peaked after another 7 days (shown in experimental part). </p> </br> </br>  
  
<h5> The second experiment </h5>
+
<h4> The second experiment </h4>
<p> The second experiment enabled us to examine the effect of cell concentration on PPIX production.  It was initially speculated that the intracellular and extracellular concentration of ALA was consistent, and our model assumed that the cells occupied the entire space. That is, we assumed that the added ALA solution enters directly into the cells, which is not the case. Thus, we took this into consideration and remodeled our code to take into account the fact that cells only occupy a certain percentage of the total volume. Here are the explanations: </p> </br>
+
<p> The second experiment aimed to examine the effect of cell concentration on PPIX production.  It was initially speculated that intracellular and extracellular concentration of ALA was homogeneous, and our model assumed that the cells occupied the entire space. That is, we assumed that the added ALA solution enters directly into the cells, which is not the case. Thus, we took this into consideration and remodeled our code to take into account the fact that cells only occupy a certain percentage of the total volume. Here are the explanations: </p> </br>
 
<div class="centreStuffInline">
 
<div class="centreStuffInline">
  
Line 126: Line 126:
 
                     <li>dc=molar quantity which is consumed between t and t+dt </li>
 
                     <li>dc=molar quantity which is consumed between t and t+dt </li>
 
                     <li>We know dc and we want to find de knowing that C<sub>1</sub>(t) = C<sub>2</sub>(t) at any time: </li>
 
                     <li>We know dc and we want to find de knowing that C<sub>1</sub>(t) = C<sub>2</sub>(t) at any time: </li>
 +
<br>
  
 
<img src= "https://static.igem.org/mediawiki/2015/0/07/MQAUST_20.png">
 
<img src= "https://static.igem.org/mediawiki/2015/0/07/MQAUST_20.png">
Line 135: Line 136:
 
</div>
 
</div>
 
<p> Graph 4-  Concentrations of product and intermediates produced over time using enzyme concentration of 0.3 µM, 1mM initial ALA concentration and considering effects of cell concentration. </p>  </br>
 
<p> Graph 4-  Concentrations of product and intermediates produced over time using enzyme concentration of 0.3 µM, 1mM initial ALA concentration and considering effects of cell concentration. </p>  </br>
<h5> Experiments </h5>
+
<h4> Experiments </h4>
<p>It was observed from preliminary experiments that certain key factors such as ALA concentration, co-factor metal ion concentrations, cell number could significantly increase the production of PPIX. With this in mind, several experiments were performed with the aim of optimising the production of PPIX. The initial experiment involved the resuspension of our <i> E.coli </i> cells in a solution of 1mM ALA. The formation of PPIX is indicated by a colour change from clear to brown which took approximately one week before the first traces of PPIX were observed. Several assumptions were made and then new experiments were carried out with slight changes to the original experiments including a decrease in cell concentration, varying the ALA concentration and the addition of zinc and magnesium to the cell culture.</p> </br>
+
<p>It was observed from preliminary experiments that certain key factors such as ALA concentration, co-factor metal ion concentrations, cell number could significantly increase the production of PPIX. With this in mind, several experiments were performed with the aim of optimising the production of PPIX. The preliminary experiment involved the resuspension of the <i> E.coli </i> cells in a solution of 1mM ALA. The formation of PPIX is indicated by a colour change of the media from colourless to brown, taking approximately one week to be detectable by eye. Several assumptions were made and then new experiments were carried out with slight changes to the original experiments including a decrease in cell concentration, varying the ALA concentration and the addition of zinc and magnesium to the cell culture.</p> </br>
  
<h5>FIRST EXPERIMENTS (16/07-29/07) </h5>
+
<h4>FIRST EXPERIMENT(16/07-29/07) </h4>
  
<h6>Protocol </h6>
+
<h4>Protocol </h4>
  
<h6>Tools: </h6>  
+
<h4>Tools: </h4>  
 
<ul><li> LB Media (250 mL) </li>   
 
<ul><li> LB Media (250 mL) </li>   
<li><i>E.coli cells </i> </li>
+
<li><i>E.coli </i> cells  </li>
 
<li>lysis solution (200 µL doses) </li>
 
<li>lysis solution (200 µL doses) </li>
 
<li>Binding buffer (350 µL doses) </li>
 
<li>Binding buffer (350 µL doses) </li>
Line 150: Line 151:
  
 
<h5>Methods:</h5>
 
<h5>Methods:</h5>
<p>In order to quantify the number of enzymes involved in the ALA to PPIX pathway, we measured the concentrations for each of the pathway’s intermediates. </p> </br>
+
<p>In order to quantify the activity of the enzymes involved in the ALA to PPIX pathway, we measured the concentrations of the intermediates within in the pathway. </p> </br>
  
 
<p>The E. coli cultures were grown overnight with shaking at 300 rpm at 37°C. The cells were harvested by centrifugation, supernatant discarded. The cells were resuspended in 5 mL of 0.1 mM glucose in 1 mM ALA, then incubated in the dark for up to 14 days. 250 uL of cells were extracted each time over 24 hour intervals and lysed with lysis buffer (Sigma plasmid prep kit) and neutralized (buffer). The precipitates were separated by centrifugation for 10 mins, and the absorbance of the supernatant measured with the nanodrop (Thermoscientific Nanodrop 2000 spectrophotometer). The absorbance maxima of PPIX is 404 nm. </p> </br>
 
<p>The E. coli cultures were grown overnight with shaking at 300 rpm at 37°C. The cells were harvested by centrifugation, supernatant discarded. The cells were resuspended in 5 mL of 0.1 mM glucose in 1 mM ALA, then incubated in the dark for up to 14 days. 250 uL of cells were extracted each time over 24 hour intervals and lysed with lysis buffer (Sigma plasmid prep kit) and neutralized (buffer). The precipitates were separated by centrifugation for 10 mins, and the absorbance of the supernatant measured with the nanodrop (Thermoscientific Nanodrop 2000 spectrophotometer). The absorbance maxima of PPIX is 404 nm. </p> </br>
  
  
<h5>Results</h5>
+
<h4>Results</h4>
 
<div class="centreStuffInline">
 
<div class="centreStuffInline">
 
<img src= "https://static.igem.org/mediawiki/2015/b/bb/MQAUST_P15.png">
 
<img src= "https://static.igem.org/mediawiki/2015/b/bb/MQAUST_P15.png">
Line 163: Line 164:
  
  
<p>As a result of conducting these experiments, an approximation for the time needed to produce a significant quantity of PPIX was established which is 14 days. Optimal concentration of PPIX was produced in 14 days. Considering the first traces of PPIX were detected 1 week after the beginning of the experiment, several possible optimisation strategies were examined:</p> </br>
+
<p>As a result of conducting these experiments, it was established that 14 days was required to produce a significant quantity of PPIX. Optimal PPIX concentration was produced in 14 days. Considering the first traces of PPIX were detected 1 week after the beginning of the experiment, several possible optimisation strategies were examined:</p> </br>
 
<ul><li>Cell concentration - oxygen is a key requirement for this pathway. If the current oxygen levels were maintained while reducing the quantity of the cells that are present, more oxygen is available for each cell and could increase the rate of the reaction. </li>
 
<ul><li>Cell concentration - oxygen is a key requirement for this pathway. If the current oxygen levels were maintained while reducing the quantity of the cells that are present, more oxygen is available for each cell and could increase the rate of the reaction. </li>
 
<li>ALA concentration - the substrate concentration greatly influences the final concentration of the product. By varying the concentration of ALA, an optimum value can be determined for the production of PPIX.</li>
 
<li>ALA concentration - the substrate concentration greatly influences the final concentration of the product. By varying the concentration of ALA, an optimum value can be determined for the production of PPIX.</li>
 
<li>Addition of Zinc, Magnesium and PBS - ALA dehydratase catalyzes the first step of the PPIX biosynthesis from ALA. It exists mainly as a high activity octamer or a low activity hexamer (Lawrence, Ramirez, Selwood, Stith, & Jaffe, 2009). Magnesium acts as an allosteric regulator of ALA dehydratase and contains a binding site only in the octamer. As well as this, it has been demonstrated that the absence of magnesium promotes the formation of these low activity hexamers (Breinig et al., 2003) However,  ALA dehydratase purifies with eight Zn2+ ions per octamer(Jaffe, Martins, Li, Kervinen, & Dunbrack, 2001). </li>
 
<li>Addition of Zinc, Magnesium and PBS - ALA dehydratase catalyzes the first step of the PPIX biosynthesis from ALA. It exists mainly as a high activity octamer or a low activity hexamer (Lawrence, Ramirez, Selwood, Stith, & Jaffe, 2009). Magnesium acts as an allosteric regulator of ALA dehydratase and contains a binding site only in the octamer. As well as this, it has been demonstrated that the absence of magnesium promotes the formation of these low activity hexamers (Breinig et al., 2003) However,  ALA dehydratase purifies with eight Zn2+ ions per octamer(Jaffe, Martins, Li, Kervinen, & Dunbrack, 2001). </li>
 
<li>This suggests that the addition of both zinc and magnesium would promote the formation of the more active octamers and hence increase the rate of the first step of the PPIX biosynthesis</li>
 
<li>This suggests that the addition of both zinc and magnesium would promote the formation of the more active octamers and hence increase the rate of the first step of the PPIX biosynthesis</li>
<li>Perform an in vitro experiment: this allows us to check the assumption [ALA]int = [ALA]ext </p> </br> </li> </ul>
+
<li>Performed an in vitro experiment: this allows us to check the assumption [ALA]int = [ALA]ext </p> </br> </li> </ul>
  
  
  
<h5>SECOND EXPERIMENTS (from 03/08)</h5>
+
<h4>SECOND EXPERIMENT (from 03/08)</h4>
  
<h6>Protocol2 </h6>
+
<h4>Protocol2 </h4>
  
<h6>Tools: </h6>
+
<h4>Tools: </h4>
 
<ul> <li>LB Media (250 mL) </li>
 
<ul> <li>LB Media (250 mL) </li>
 
<li><i>E.coli </i> cells</li>
 
<li><i>E.coli </i> cells</li>
Line 187: Line 188:
  
 
<h6>Methods: </h6>
 
<h6>Methods: </h6>
<p> As described previously, we measured the concentrations for each of the pathway’s intermediates to quantify the number of enzymes involved in the ALA to PPIX pathway. </p> ></br>
+
<p> As described previously, we measured the concentrations for each of the pathway’s intermediates to quantify the activity of the enzymes involved in the ALA to PPIX pathway. </p> </br>
  
 
<p> The E. coli cultures were grown overnight with shaking at 300 rpm at 37°C. The cells were harvested by centrifugation, supernatant discarded. The cells were resuspended in a solution of phosphate buffered saline, Zinc(10µM) and Mg(2mM), then incubated in the dark for up to 19 days. The cultures were adjusted to an OD of 0.2 and 0.02 to observe the effect of cell concentration on PPIX output. Four concentrations of ALA were tested against these conditions as follows:  </p> </br>
 
<p> The E. coli cultures were grown overnight with shaking at 300 rpm at 37°C. The cells were harvested by centrifugation, supernatant discarded. The cells were resuspended in a solution of phosphate buffered saline, Zinc(10µM) and Mg(2mM), then incubated in the dark for up to 19 days. The cultures were adjusted to an OD of 0.2 and 0.02 to observe the effect of cell concentration on PPIX output. Four concentrations of ALA were tested against these conditions as follows:  </p> </br>
  
 
<div class="centreStuffInline">
 
<div class="centreStuffInline">
<img src= "https://static.igem.org/mediawiki/2015/e/e2/MQAUST_P26.png">
+
<img src= "https://static.igem.org/mediawiki/2015/6/6e/MQAUST_53.png">
 
</div>
 
</div>
 +
<p> Table 2- Showing different initial concentrations of ALA added to different concentrations of <i> E.coli </i> cell culture.  </p>
  
 
<p>Approximately 25 uL of cells were extracted each time over 24 hour intervals, and lysed with lysis buffer (20 uL) (Sigma plasmid prep kit) and neutralized (neutralisation buffer). The precipitates were separated by centrifugation for 10 mins and the absorbance of the supernatant measured with the nanodrop (Thermoscientific Nanodrop 2000 spectrophotometer). </p> </br>
 
<p>Approximately 25 uL of cells were extracted each time over 24 hour intervals, and lysed with lysis buffer (20 uL) (Sigma plasmid prep kit) and neutralized (neutralisation buffer). The precipitates were separated by centrifugation for 10 mins and the absorbance of the supernatant measured with the nanodrop (Thermoscientific Nanodrop 2000 spectrophotometer). </p> </br>
Line 203: Line 205:
 
   
 
   
  
<p>Graph 6 - Shows concentration of PPIX produced from various initial concentration of ALA for  <i> E.coli</i> cell culture of 0.2mM concentration. For 5 mM of initial ALA concentration most PPIX was produced which is due to substrate inhibition (shown in figure 2 below).  </p> </br>
+
<p>Graph 6 - Shows concentration of PPIX produced from various initial concentrations of ALA for  <i> E.coli</i> cell culture concentration of 0.2mM. The most PPIX was produced from an initial ALA concentration of 5 mM as greater concentrations resulted in substrate inhibition (shown in figure 2 below).  </p> </br>
  
 
<div class="centreStuffInline">
 
<div class="centreStuffInline">
 
<img src= "https://static.igem.org/mediawiki/2015/9/9b/MQAUST_19.png">
 
<img src= "https://static.igem.org/mediawiki/2015/9/9b/MQAUST_19.png">
 
</div>
 
</div>
<p>Graph 7 - Shows concentration of PPIX produced from various initial concentration of ALA for <i> E.coli</i> cell culture of 0.02mM concentration. For 5 mM of initial ALA concentration most PPIX was produced which is due to substrate inhibition (shown in figure 2 below).  </p> </br>
+
<p>Graph 7 - Shows concentration of PPIX produced from various initial concentrations of ALA for <i> E.coli</i> cell culture concentration of 0.02mM. The most PPIX was produced from an initial ALA concentration of 5 mM as greater concentrations resulted in substrate inhibition (shown in figure 2 below).  </p> </br>
 
+
 
+
 
+
 
+
  
  
 
<h5>Discussion </h5>
 
<h5>Discussion </h5>
<p> 5mM of initial concentration of ALA produced optimum concentration of PPIX. This is due to substrate inhibition where Protoporphyrinogen IX inhibits conversion of ALA to porphobilinogen via porphobilinogen synthase (Stamford, Capretta, & Battersby, 1995). </p> </br>
+
<p> An initial ALA concentration of 5mM produced the optimum concentration of PPIX. This is likely to be due to substrate inhibition at greater concentrations where Protoporphyrinogen IX inhibits the conversion of ALA to porphobilinogen via porphobilinogen synthase (Stamford, Capretta, & Battersby, 1995). </p> </br>
<p> Moreover, change in concentration of cells did not change the production of PPIX ensuring oxygen  
+
<p> Moreover, the change in cell concentration did not change the production of PPIX, indicating that oxygen  
availability did not affect the PPIX production that much. Adding of glucose resulted a little increase in PPIX production which ensured. Hence, we can say that it doesn’t affect PPIX production that much.A little difference was seen  between experimental PPIX formation and predicted PPIX formation.  
+
availability did not greatly influence the production of PPIX. The addition of glucose resulted in a subtle increase in PPIX production. As such, it cannot be deduced that glucose significantly impacts the production of PPIX. A slight difference was observed between the experimental PPIX formation and the predicted PPIX formation.  
We predicted formation of 0.12 mM PPIX (shown in Graph 1) form 1 mM ALA but only 0.065 mM PPIX was produced experimentally (shown in Graph 7 ).
+
We predicted the formation of 0.12 mM PPIX (Graph 1) from 1 mM ALA but only 0.065 mM of PPIX was produced (Graph 7 ).
 
  </p>
 
  </p>
 
<div class="centreStuffInline">
 
<div class="centreStuffInline">
Line 228: Line 226:
 
</div>
 
</div>
  
<p> Fig 3- Protoporphyrinogen IX inhibiting conversion of ALA to porphobilinogen via porphobilinogen synthase (Stamford, Capretta, & Battersby, 1995). This is a process of substrate inhibition which  allows a certain concentration of ALA  to produce optimum amount of PPIX which in our case was 5mM (Stamford, Capretta, & Battersby, 1995). </p> </br>
+
<p> Fig 3- Protoporphyrinogen IX inhibiting the conversion of ALA to porphobilinogen via porphobilinogen synthase (Stamford, Capretta, & Battersby, 1995). This is a process of substrate inhibition which  allows a certain concentration of ALA  to produce an optimum amount of PPIX which in our case was 5mM (Stamford, Capretta, & Battersby, 1995). </p> </br>
 
+
  
 
<h5> Conclusion </h5>
 
<h5> Conclusion </h5>
<p> Our experiments enabled us to get a  better understanding of how the pathway from ALA to PPIX worked. Substantial amount of PPIX was produced from ALA and the ratio of ALA:PPIX concentration produced was 1:8 as expected (Wachowska et al., 2011).  ALA seemed to pass through the membrane passively. As no excess energy was needed to introduce ALA to <i>E.coli</i>. Oxygen availability did not have a massive impact on the PPIX production as change in concentration of cells did not affect the concentration of PPIX produced. Moreover, due to substrate inhibition, 5mM initial ALA concentration produced higher concentration of PPIX compared to other concentrations. We didn’t find the enzyme concentration as we expected as the experiments were too long and we didn’t have time to measure other concentration such as those of the intermediates</p> </br> </br>
+
<p> Our experiments enabled us to improve our understanding of how the ALA to PPIX pathway operates. A substantial amount of PPIX was produced from ALA and the ratio of ALA:PPIX concentration was 1:8 as expected (Wachowska et al., 2011).  It was speculated that ALA enters cells via passive transport, as no excess energy was needed to introduce ALA to <i>E.coli</i>. Oxygen availability did not have a significant impact on PPIX production as the change in concentration of cells little effect. Furthermore, due to substrate inhibition, an initial ALA concentration of 5mM resulted in the greatest yield of PPIX compared to the other concentrations used. Enzyme concentrations were not determined due to the excessive length of the experiments. This was also the case with other concentrations such as those of the intermediates.</p> </br> </br>
  
  
<h6> References  </h6>
+
<h5> References  </h5>
 
<ul> <li> Alwan, A. F., Mgbeje, B., & Jordan, P. M. (1989). Purification and properties of uroporphyrinogen III synthase (co-synthase) from an overproducing recombinant strain of Escherichia coli K-12. <i>Biochem. J</i>, 264, 397-402. </li>
 
<ul> <li> Alwan, A. F., Mgbeje, B., & Jordan, P. M. (1989). Purification and properties of uroporphyrinogen III synthase (co-synthase) from an overproducing recombinant strain of Escherichia coli K-12. <i>Biochem. J</i>, 264, 397-402. </li>
 
<li>Boynton, T. O., Daugherty, L. E., Dailey, T. A., & Dailey, H. A. (2009). Identification of Escherichia coli HemG as a novel, menadione-dependent flavodoxin with protoporphyrinogen oxidase activity.<i> Biochemistry</i>, 48(29), 6705-6711.  </li>
 
<li>Boynton, T. O., Daugherty, L. E., Dailey, T. A., & Dailey, H. A. (2009). Identification of Escherichia coli HemG as a novel, menadione-dependent flavodoxin with protoporphyrinogen oxidase activity.<i> Biochemistry</i>, 48(29), 6705-6711.  </li>
Line 255: Line 252:
 
  <li> Wachowska, M., Muchowicz, A., Firczuk, M., Gabrysiak, M., Winiarska, M., Wańczyk, M., . . . Golab, J. (2011). Aminolevulinic acid (ALA) as a prodrug in photodynamic therapy of cancer.<i> Molecules</i>, 16(5), 4140-4164. </li>  
 
  <li> Wachowska, M., Muchowicz, A., Firczuk, M., Gabrysiak, M., Winiarska, M., Wańczyk, M., . . . Golab, J. (2011). Aminolevulinic acid (ALA) as a prodrug in photodynamic therapy of cancer.<i> Molecules</i>, 16(5), 4140-4164. </li>  
 
</ul>
 
</ul>
 
<h1> PHOTOSYSTEM II </h1>
 
</div>
 
 
<h5> Basic Principle </h5>
 
<p>
 
The mechanism by which the photosystem II (PSII) reaction centre absorbs and utilises sunlight is critical to the functioning of our photosynthetic <i> E. coli</i>. Visible light (~400-70 nm) is the major impetus provoking release by PSII of the electrons necessary for subsequent hydrogen generation via hydrogenase enzymes. </p> </br>
 
<div class="centreStuffInline">
 
<img src= "https://static.igem.org/mediawiki/2015/1/12/MQAUST_PS1.png">
 
</div>
 
 
<p> Figure 1:  Light-induced water splitting by photosystem II in photosynthesis and hydrogen production by an [FeFe] hydrogenase (Lubitz <i>et al</i>., 2008). </p> </br>
 
 
 
<p> We therefore designed this three-stage model to explore efficiency of PSII action towards hydrogen production within bounds established by an initial conception of our implementation prototype. </p> </br>
 
<div class="centreStuffInline">
 
<img src= "https://static.igem.org/mediawiki/2015/1/12/MQAUST_PS1.png">
 
</div>
 
 
 
 
<p> The initial stage of our model examines the sunlight absorbance process. It calculates the capacity of chlorophyll-a, and thereby PSII, to absorb sunlight; and calculates the light intensity received by the <i>E. coli</i> cells as situated in our prototype. The second stage establishes the electron production rate per PSII. The model’s final stage integrates the preceding findings to predict H<sub>2</sub> production per mL of <i>E. coli</i> cells per hour.  </p> </br>
 
<div class="centreStuffInline">
 
<img src= "https://static.igem.org/mediawiki/2015/1/12/MQAUST_PS1.png">
 
 
</div>
 
 
 
 
<h5> Stage 1 </h5>
 
<p>The production of H<sub>2</sub> is ultimately driven by sunlight. The optimal functioning of our prototype in generating hydrogen thus relies upon the sunlight absorption process. The scheme shown (Figure 2) outlines the physical model we have devised, and upon which our calculations are based, to take best advantage of available light. </br> </br>
 
<div class="centreStuffInline">
 
<img src="https://static.igem.org/mediawiki/2015/c/c3/MQAUST_PS5.png">
 
</div>
 
 
 
 
 
<p> Figure 2: The basic implementation prototype initially designed. Our photosynthetic <i>E. coli</i> cells are housed between two layers of media, each backed by a one-way mirrored surface to reflect and magnify light. </p> </br>
 
 
<p> Absorption of the sunlight is governed by: </p> </br>
 
 
<ul> <li> a: absorption by <i>E. coli</i> </li>
 
<li> k: absorption by the solution = 0.722 (Paolin, 2012) </li>
 
<li> r: reflexion coefficients of the mirrors = 0.95 </li> </ul> </br>
 
 
<p> Calculation of <i>a</i> first requires the concentration of PSII ([PSII]). In deriving this concentration, we have assumed firstly that PSII will be located only at the surface of <i>E. coli</i> cells; and secondly that they will occupy 10% of this area. This percentage is a minimum value, not taking into account the possibility of an increased occupancy by placing PSIIs within vesicles inside the <i>E. coli</i> cells. </p>
 
 
<p>These initial assumptions fed into the development of specific physical parameters for the surface areas of our initial prototype, as follows: </p>
 
<ul>
 
<li>S<sub>e</sub>: surface area of <i>E. coli</i> cells = 18.8 µm<sup>2</sup>    </li>
 
<li>S<sub>u</sub>: ‘useful’ surface area of <i>E. coli</i> cells = 6 µm<sup>2</sup></li>
 
<li>S<sub>PSII</sub>: surface area of PSII = 0.202 µm<sup>2</sup> (Morris <i>et al</i>., 1997)</li>
 
<li>N<sub>e</sub>: number of <i>E. coli</i> cells (per mL) = 10<sup>9</sup> cells/mL</li> </ul> </br> </br>
 
<div class="centreStuffInline">
 
<img src="https://static.igem.org/mediawiki/2015/b/b4/MQAUST_PS6.png">
 
</div>
 
 
<p> Figure 3: Scheme representing physical parameters of <i>E. coli</i> total (S<sub>e</sub>) and ‘useful’ (S<sub>u</sub>) cell surfaces as determined in accordance with our initial prototype. </p> <br>
 
 
<p> These parameters provide the number of PSIIs per <i>E. coli</i> cell (N<sub>PSII</sub>), and consequently [PSII]: </p> </br>
 
<img src="https://static.igem.org/mediawiki/2015/6/6e/MQAUST_PS7.png">
 
 
 
<p> Concentration of the antenna pigment chlorophyll-a ([chla]) is known to be eight times the [PSII] (Liu <i>et al</i>., 2004). Therefore: </p> </br> <img src="https://static.igem.org/mediawiki/2015/c/cd/MQAUST_PS8.png">
 
 
 
 
 
 
<p> Using ε of [chla], we can derive its absorbance A. This allowed consequent determination of <i>a</i>, the percentage of light absorbed by <i>E. coli</i>:</p> </br>
 
<img src="https://static.igem.org/mediawiki/2015/b/b4/MQAUST_PS9.png">
 
 
<ul> <li>ε: extinction coefficient of chla = 73300 L/mol/cm (Inskeep and Bloom, 1985) </li>
 
<li> l: pathlength = 1 cm </li> </ul>
 
 
 
<p> Having established the cells’ capacity to absorb light relative to its intensity, we proceeded to calculate the light available for that absorbance process in the environment of our theorised implementation prototype (Figure 4). </p> </br>
 
 
<div class="centreStuffInline">
 
<img src="https://static.igem.org/mediawiki/2015/8/81/MQAUST_PS10.png">
 
</div>
 
 
<p> Figure 4: A more detailed scheme of our prototype. </p> </br>
 
 
 
<p>We have assumed for this physical model that the light is absorbed first by the media, then by the <i>E. coli</i> cells, and finally follows the reflection on the mirrors. From this scheme, we were able to create a discrete model deducing the absorption of sunlight:</p> </br>
 
 
<p> Absorption of the media at depth <i>z</i>: </p> </br>
 
<img src="https://static.igem.org/mediawiki/2015/a/ae/MQAUST_PS11.png">
 
 
 
 
 
<p> As the light crosses two layers of media of <i>l</i> length = 0.01, light intensity: </p> </br>
 
<img src="https://static.igem.org/mediawiki/2015/e/e1/MQAUST_PS12.png">
 
 
 
 
 
 
<p> Absorption of <i>E. coli</i>: </p> </br>
 
<img src="https://static.igem.org/mediawiki/2015/a/a5/MQAUST_PS13.png">
 
 
 
 
 
<p> Loss of intensity due to reflection:</p> </br>
 
<img src="https://static.igem.org/mediawiki/2015/1/10/MQAUST_PS14.png">
 
 
 
 
<p> The relationship between <i>I<sub>n+1</sub></i> and <i>I<sub>n</sub></i> therefore becomes:</p> </br>
 
<img src="https://static.igem.org/mediawiki/2015/c/cd/MQAUST_PS15.png">
 
 
 
 
 
<p> This gives us: </p> </br>
 
 
<img src="https://static.igem.org/mediawiki/2015/3/3d/MQAUST_PS21.png">
 
 
 
 
 
<p>The above equation, solved for <i>N</i> iterations = 100, was used to derive cumulative intensity. Available reflected light passing through the prototype to be absorbed by our cells declined with each iteration; this decrease (<i>e<sup>-k.2l</sup>.r.a</i>) was relative to light intensity, and itself showed decline over time. The sum total of light intensity available per each iteration proved to be magnified from the initial light input, <i>I<sub>0</sub></i>. </p> </br>
 
 
<p>We have thereby concluded that the light intensity received by the <i>E. coli</i> cells is about 13.4 times that of the light entering the prototype.
 
(cf “absorption” excel file) </p> </br>
 
 
 
<h5> Stage 2 </h5>
 
<p>The absorbance of visible light by Photosystem II causes the release of electrons, which travel via the electron transport chain to Photosystem I. Our aim is to divert these electrons, preventing them from reaching the electron transport chain, and instead utilise them in hydrogen production. </p> </br>
 
<div class="centreStuffInline">
 
<img src="https://static.igem.org/mediawiki/2015/1/12/MQAUST_PS17.png">
 
</div>
 
 
 
 
<p> Figure 5: Electron produced by Photosystem II diverted to H<sub>2</sub> production instead of entering the electron transport chain. </p> </br>
 
 
<p> Conversion of introduced light energy to primary product is affected by limiting factors including the low electron transfer rate between Photosystems II and I. Under full sunlight, up to 90% of captured photons may decay as heat or fluorescence (Hallenbeck and Benemann, 2002). When the electrons generated are diverted to hydrogen production, this lag between photosystems is irrelevant. The electron production rate per PSII (ETR<sub>PSII</sub>) becomes directly proportional to the amount of light introduced to Photosystem II. </p> </br>
 
<div class="centreStuffInline">
 
 
<img src="https://static.igem.org/mediawiki/2015/3/35/MQAUST_PS18.png">
 
</div>
 
 
 
 
 
<p> Figure 6: The green curve represents electron production rate for electrons introduced into the electron transport chain; the blue line represents electron production rate for electrons used in hydrogen production. </p> </br>
 
 
<p> We have taken the photosynthetic photon flux, <i>Isun</i>, to be 2000 umol/m²/s as previously reported (Posada <i>et al</i>., 2009).* Our modelling of its direct relationship with release of electrons by PSII, 2*<i>Isun</i>, is illustrated in Figure 6.  </p> </br>
 
 
<p>ETR<sub>PSII</sub> was therefore found to be 4000 é/s/PSII (Zorz <i>et al</i>., 2015).</p> </br>
 
 
<p>[*The intensity of sunlight assumed here is the maximum value, not that which cells will receive throughout the day; daily irradiance can show significant variation.] </p> </br>
 
 
 
<h5> Stage 3 </h5>
 
<P> Hydrogen is generated through the action of the hydrogenase enzyme. This process utilises two diverted electrons released by PSII per H<sub>2</sub> molecule:</p> </br>
 
 
<p> 2<sup>H+</sup> + 2<sup>e-</sup> ⇄ H<sub>2</sub>. </p> </br>
 
 
<p> Hydrogenase reaction rates are known to range between 10<sup>3</sup>-10<sup>4</sup> turnovers per second at 30<sup>o</sup>C, sufficiently high to circumvent any potential limiting factors (Pershad <i>et al</i>., 1999; Lubitz <i>et al</i>., 2008). Our modelling has consequently used the following known parameters: </p> </br>
 
 
<ul> <li>ETR<sub>PSII</sub>: production of electrons per PSII = 4000 é/s/PSII </li>
 
<li>N<sub>PSII</sub>: number of PSII per cells = 9300 </li>
 
<li>S<sub>u</sub>: “useful” surface of <i>E. coli</i> cells = 6.0 µm<sup>2</sup> </li>
 
<li>S<sub>e</sub>: surface of <i>E. coli</i> cells = 18.8 µm<sup>2</sup></li>
 
<li>N<sub>e</sub>: number of <i>E. coli</i> in one mL = 10<sup>9</sup> cells/mL</li>
 
<li>v(H<sub>2</sub>): molar volume of H<sub>2</sub> = 22.43 mol/L</li> </ul>
 
 
<p>We have thereby calculated the H<sub>2</sub> production in mL/hour per mL of our solution: </p>
 
<img src="https://static.igem.org/mediawiki/2015/2/22/MQAUST_PS19.png">
 
 
 
 
 
 
 
<p> By this model, 1 mL of our <i>E. coli</i> cells will give 0.8 mL of H<sub>2</sub> per hour. </p> </br>
 
 
<p> Given that the electron production rate per PSII (ETR<sub>PSII</sub>) is proportional to the sunlight absorbed, the coefficient linking the magnified amount of sunlight absorbed by our prototype (x13.4) can be directly introduced: </p> </br>
 
<img src="https://static.igem.org/mediawiki/2015/9/9c/MQAUST_PS20.png">
 
 
 
 
 
<p>
 
Our 1 mL of cells can therefore be predicted to produce 10.7 mL of H<sub>2</sub> per hour! </p> </br>
 
 
<h5>CONCLUSION </h5>
 
 
<p> The models created for PSII production of (é) and of H<sub>2</sub> through hydrogenase have provided us with highly encouraging results. The H<sub>2</sub> production of 10.7 mL per mL of <i>E. coli</i> per hour predicted by this modelling indicates higher quantities than comparable procedures currently under investigation. </p> </br>
 
 
<p> For reference, green algae had previously been calculated to yield hydrogen at about 10 moles of H<sub>2</sub> per m<sup>2</sup> of cell culture area per day (Melis and Happe, 2001; Melis, 2007). An engineered cyanobacterial strain has recently been shown to generate H<sub>2</sub> at a maximal volumetric production rate of 6.2 mL per litre per hour (Nyberg <i>et al</i>., 2015). Both of these fall below our own estimation, which thus represents a significant improvement in photobiological hydrogen production efficacy. </p> </br>
 
 
<p>The improved understanding of the light absorption and hydrogen production processes that was provided by this modelling informed further development of our business implementation prototype. </p> </br>
 
 
 
<h6>References: </h6>
 
<p>
 
<ul> <li> Hallenbeck, P.C. and Benemann, J.R. (2002). Biological hydrogen production; fundamentals and limiting processes. <i>International Journal of Hydrogen Energy</i>, 27, 1185-1193. </li>
 
 
<li>Inskeep, W.P. and Bloom, P.R. (1985). Extinction Coefficients of Chlorophyll a and b in N,N-Dimethylformamide and 80% Acetone. <i>Plant Physiology</i>, 77, 483-485. </li>
 
 
<li>Liu, Z., Yan, H., Wang, K., Kuang, T., Zhang, J., Gui, L., An, X., Chang, W. (2004). Crystal structure of spinach major light-harvesting complex at 2.72Å resolution. <i>Nature</i>, 428, 287-292. </li>
 
 
<li>Lubitz, W., Reijerse, E.J., Messinger, J. (2008). Solar water-splitting into H2 and O2: design principles of photosystem II and hydrogenases. <i>Energy and Environmental Science</i>, 1, 15-31. </li>
 
 
<li>Melis, A., Happe, T. (2001). Hydrogen Production. Green Algae as a Source of Energy. <i>Plant Physiology</i>, 127, 740-748.
 
</li>
 
 
<li> Melis, A. (2007). Photosynthetic H2 metabolism in <i>Chlamydomonas reinhardtii</i> (unicellular green algae). <i>Planta</i>, 226, 1075-1086.</li>
 
<li>
 
Morris, E.P., Hankamer, B., Zheleva, D., Friso, G., Barber, J. (1997). The three-dimensional structure of a photosystem II core complex determined by electron crystallography. <i>Structure</i>, 5, 837-849.</li>
 
<li>
 
Nyberg, M., Heidorn, T., Lindblad, P. (2015). Hydrogen production by the engineered cyanobacterial strain <i>Nostoc</i> PCC 7120 Δ<i>hupW</i> examined in a flat panel photobioreactor system. <i>Journal of Biotechnology</i>, doi:10.1016/j.jbiotec.2015.08.028.
 
</li>
 
<li>
 
Paolin, M. (2012). Étude des facteurs contrôlant l’atténuation lumineuse dans une lagune semi-fermée. Calibration d’un modèle bio-optique pour le Bassin d’Arcachon. (available online http://archimer.ifremer.fr/doc/00101/21209/18824.pdf).
 
</li>
 
<li>
 
Pershad, H.R., Duff, J.L.C., Heering, H.A., Duin, E.C., Albracht, S.P.J., Armstrong, F.A. (1999). Catalytic Electron Transport in <i>Chromatium vinosum</i> [NiFe]-Hydrogenase: Application of Voltammetry in Detecting Redox-Active Centres and Establishing That Hydrogen Oxidation Is Very Fast Even at Potentials Close to the Reversible H+/H2 Value. <i>Biochemistry</i>, 38, 8992-8999.</li>
 
<li>
 
Posada, J.M., Lechowicz, M.J., Kitajima, K. (2009). Optimal photosynthetic use of light by tropical tree crowns achieved by adjustment of individual leaf angles and nitrogen content. <i>Annals of Botany</i>, 103, 795-805.</li>
 
<li>Zorz, J.K., Allanach, J.R., Murphy, C.D., Roodvoets, M.S., Campbell, D.A., and Cockshutt, A.M. (2015). The RUBISCO to Photosystem II Ratio Limits the Maximum Photosynthetic Rate in Picocyanobacteria. <i>Life</i>, 5, 403-417.
 
</li> </ul>
 
  
  

Latest revision as of 12:19, 19 November 2015

Modelling
Link to Experiments & Protocols page
Link to photoSysII page

ALA to PPIX

Basic Principle

One of the aims of this project was to re-engineer E.coli to produce chlorophyll a which E.coli does not naturally produce. It produces heme which shares the same precursor as a chlorophyll a, Protoporphyrin IX (PPIX) (figure 1) (Willows, 2004). The PPIX pathway begins from aminolevulinic acid (ALA), which is produced naturally in E.coli but can be also be added to increase the production of PPIX (Willows, 2004).


Fig 1: Biosynthetic pathway from ALA to the first coloured intermediate protoporphyrin IX. a. ALA dehydratase; b. porphobilinogen deaminase; c. uroporphyrinogen III synthase; d. uroporphyrinogen decarboxylase; e. coproporphyrinogen oxidase; f. protoporphyrinogen oxidase (Willows, 2004) .


Our initial aim was to model the pathway from ALA to PPIX in native E. coli cells to determine what concentration of ALA would give us the optimal yield of PPIX. Ultimately, we plan to model the entire Chlorophyll a biosynthesis pathway, and the production of H2 gas.


Mathematical Model Overview-

Michaelis-­Menten type enzyme kinetics were studied first prior to establishing appropriate parameters from reported literature to propose our models. The adopted kinetic equation was then used to determine enzyme concentration through first-hand experiments and then fedback on our model which contains an arbitrary amount of enzyme concentrations.


The initial velocity of the reaction (Vi) directly depends on the rate of the conversion of ES to P. It is also dependent on the total enzyme concentration (Keleti & Kramer, 1986). By using the following formula, the total enzyme concentration can be determined from the experimental values of Vi and S, which also corresponds to initial ALA concentration. (Keleti & Kramer, 1986)

Our Model

Abbreviations used

  • ALA -δ-aminolevulinic acid
  • PPBS -porphobilinogen synthase
  • PPB -porphobilinogen
  • PPBD -porphobilinogen deaminase
  • HMB -hydrymethylbilane
  • UROS -uroporphyrinogen III synthase
  • URO -uroporphyrinogen III
  • UROD -uroporphyrinogen decarboxylase
  • CPO -coproporphyrinogen
  • CPOO -coproporphyrinogen oxidase
  • POIX -protoporphyrinogen IX
  • POO -protoporphyrinogen oxidase
  • PPIX -protoporphyrin IX

In our modelling experiment, the initial concentration of ALA, [ALA]0, was used as a known independent variable while initial enzyme concentration, [E]0, was used as a dependent variable . We assumed that all the substrates and products had a concentration of 0 at time 0 sec (t=0). [ALA]0 was varied from 1mM to 5mM to 10 mM to 20mM. [E]0 was arbitrarily chosen in a realistic interval of 0.1 µM to 1 µM. This is the natural concentration of enzyme seen in E.coli . For this first model, we assume that there would be no inhibition of any enzymatic activity and that ALA would only be converted to PPIX only and it only follows this biosynthesis pathway shown below.


First model

In this model we considered the following reaction for ALA to PPIX transformation:

Table 1- Table displaying enzyme properties involved.

The above equations were used to obtain the following graphs via Matlab, and was adopted for all the intermediates. In this equation, S1 denotes the substrate and S2 denotes the intermediate produced from that substrate. For example, for the first step of reaction, ALA to porphobilinogen, S1 denotes ALA and S2 denotes porphobilinogen;for the following step of the reaction, porphobilinogen to hydroxymethylbilane, S1 denotes porphobilinogen and S2 denotes hydroxymethylbilane.


Graph 1: The above graph was plotted using initial ALA concentration of 1mM and 0mM of the remaining intermediates, enzyme and products involved. From the graph, it was observed that [ALA] became 0 at an accelerated rate and [PPIX] reached its peak value in approximately 0.7h . Combined values of Kcat for all the intermediates contribute to the time for formation of PPIX. This peak [PPIX] value was 1/8th of [ALA]0, which was expected as the conjugation of eight ALA molecules yields one protoporphyrin IX (PPIX) molecule(Wachowska et al., 2011).


Graph 2: This consists of graph 1 zoomed in to view the change in concentration of the intermediates involved at the initial stage of the reaction. PPB was the first intermediate produced, thus it appeared first and began to decrease as HMB was produced. As Uroporphyrinogen III synthase has a very high Kcat (500/s) , URO production from HMB was almost instant, hence, HMB was rapidly consumed.


Based on this, we performed a preliminary experiment with measurements at time intervals of 5, 10, 20, 30, 60 and 120 minutes. However, no brown coloured solution was observed to indicate PPIX formation, which was further verified by nanodrop absorbance readings.


Based on this, we constructed a second model taking into account the intermediates consisting of enzyme complexes.


In order to estimate the quantities of the enzymes involved in the ALA to PPIX pathway, we measured the concentrations for each of the pathway’s intermediates.


The E. coli cultures were grown overnight with shaking at 300 rpm at 37°C. The cells were harvested by centrifugation, supernatant discarded. The cells were resuspended in 5 mL of 0.1 mM glucose in 1 mM ALA, then incubated in the dark for up to 14 days. Approximately 250 uL of cells were extracted each time over 24 hour intervals, and lysed with lysis buffer and neutralized with neutralization buffer (Sigma plasmid prep kit). The precipitates were separated by centrifugation for 10 mins, and the absorbance of the supernatant measured with the nanodrop (Thermoscientific Nanodrop 2000 spectrophotometer). The absorbance maxima of PPIX is 404 nm.


Second Model-

When the intermediates (enzyme complexes) were added, the following reactions were obtained:


The first reaction was translated into a mathematical equation to give:-


The second mathematical model was then based on these equations.









Fig 2 : 2 ALA molecules combine to produce 1 PPB molecule. 4 PGB molecules form 1 HMB molecule (Ryter & Tyrrell, 2000).



The stoichiometric relationships displayed in figure 2 were introduced into matlab and used to obtain the following graph:


Graph 3: This graph was obtained using 1mM [ALA]0 and 0.1 µM as initial enzyme concentrations. [PPIX] reached its peak after approximately 7 days. From our first experiment, a significant concentration of PPIX was observed after 1 week, and peaked after another 7 days (shown in experimental part).



The second experiment

The second experiment aimed to examine the effect of cell concentration on PPIX production. It was initially speculated that intracellular and extracellular concentration of ALA was homogeneous, and our model assumed that the cells occupied the entire space. That is, we assumed that the added ALA solution enters directly into the cells, which is not the case. Thus, we took this into consideration and remodeled our code to take into account the fact that cells only occupy a certain percentage of the total volume. Here are the explanations:


Notations:

  • 1 =solution with which we resuspended cells (ALA)
  • 2=cells
  • Vi=volume of the media i
  • V=volume total = V1 + V2
  • xvol=proportion of cells in the media
  • C1(t)= concentration at t
  • ni(t)=molar quantity of the media i at t
  • de=molar quantity which enter in cells between t and t+dt
  • dc=molar quantity which is consumed between t and t+dt
  • We know dc and we want to find de knowing that C1(t) = C2(t) at any time:

  • Thereby, we obtained the following graph with an enzyme concentration of 0.3 µM by taking into account of the above cell percentage:


    Graph 4- Concentrations of product and intermediates produced over time using enzyme concentration of 0.3 µM, 1mM initial ALA concentration and considering effects of cell concentration.


    Experiments

    It was observed from preliminary experiments that certain key factors such as ALA concentration, co-factor metal ion concentrations, cell number could significantly increase the production of PPIX. With this in mind, several experiments were performed with the aim of optimising the production of PPIX. The preliminary experiment involved the resuspension of the E.coli cells in a solution of 1mM ALA. The formation of PPIX is indicated by a colour change of the media from colourless to brown, taking approximately one week to be detectable by eye. Several assumptions were made and then new experiments were carried out with slight changes to the original experiments including a decrease in cell concentration, varying the ALA concentration and the addition of zinc and magnesium to the cell culture.


    FIRST EXPERIMENT(16/07-29/07)

    Protocol

    Tools:

    • LB Media (250 mL)
    • E.coli cells
    • lysis solution (200 µL doses)
    • Binding buffer (350 µL doses)
    • 0.1 mM glucose in 1 mM ALA (5 mL)
    Methods:

    In order to quantify the activity of the enzymes involved in the ALA to PPIX pathway, we measured the concentrations of the intermediates within in the pathway.


    The E. coli cultures were grown overnight with shaking at 300 rpm at 37°C. The cells were harvested by centrifugation, supernatant discarded. The cells were resuspended in 5 mL of 0.1 mM glucose in 1 mM ALA, then incubated in the dark for up to 14 days. 250 uL of cells were extracted each time over 24 hour intervals and lysed with lysis buffer (Sigma plasmid prep kit) and neutralized (buffer). The precipitates were separated by centrifugation for 10 mins, and the absorbance of the supernatant measured with the nanodrop (Thermoscientific Nanodrop 2000 spectrophotometer). The absorbance maxima of PPIX is 404 nm.


    Results

    Graph 5- PPIX was observable after approximately one week of incubation and continued to increase for a further 6 days. The theoretical absorbance value for a complete conversion of ALA to PPIX was calculated to be 2.0625. At 14th day, 2.0625 mM concentration of PPIX was produced.


    As a result of conducting these experiments, it was established that 14 days was required to produce a significant quantity of PPIX. Optimal PPIX concentration was produced in 14 days. Considering the first traces of PPIX were detected 1 week after the beginning of the experiment, several possible optimisation strategies were examined:


    • Cell concentration - oxygen is a key requirement for this pathway. If the current oxygen levels were maintained while reducing the quantity of the cells that are present, more oxygen is available for each cell and could increase the rate of the reaction.
    • ALA concentration - the substrate concentration greatly influences the final concentration of the product. By varying the concentration of ALA, an optimum value can be determined for the production of PPIX.
    • Addition of Zinc, Magnesium and PBS - ALA dehydratase catalyzes the first step of the PPIX biosynthesis from ALA. It exists mainly as a high activity octamer or a low activity hexamer (Lawrence, Ramirez, Selwood, Stith, & Jaffe, 2009). Magnesium acts as an allosteric regulator of ALA dehydratase and contains a binding site only in the octamer. As well as this, it has been demonstrated that the absence of magnesium promotes the formation of these low activity hexamers (Breinig et al., 2003) However, ALA dehydratase purifies with eight Zn2+ ions per octamer(Jaffe, Martins, Li, Kervinen, & Dunbrack, 2001).
    • This suggests that the addition of both zinc and magnesium would promote the formation of the more active octamers and hence increase the rate of the first step of the PPIX biosynthesis
    • Performed an in vitro experiment: this allows us to check the assumption [ALA]int = [ALA]ext


    SECOND EXPERIMENT (from 03/08)

    Protocol2

    Tools:

    • LB Media (250 mL)
    • E.coli cells
    • Lysis solution (20 µL)
    • ALA (20 mM)
    • glucose (20 mM)
    • PBS solution
    • ZnCl2 (10 µM)
    • MgCl or MgSO4 (2 mM)
    Methods:

    As described previously, we measured the concentrations for each of the pathway’s intermediates to quantify the activity of the enzymes involved in the ALA to PPIX pathway.


    The E. coli cultures were grown overnight with shaking at 300 rpm at 37°C. The cells were harvested by centrifugation, supernatant discarded. The cells were resuspended in a solution of phosphate buffered saline, Zinc(10µM) and Mg(2mM), then incubated in the dark for up to 19 days. The cultures were adjusted to an OD of 0.2 and 0.02 to observe the effect of cell concentration on PPIX output. Four concentrations of ALA were tested against these conditions as follows:


    Table 2- Showing different initial concentrations of ALA added to different concentrations of E.coli cell culture.

    Approximately 25 uL of cells were extracted each time over 24 hour intervals, and lysed with lysis buffer (20 uL) (Sigma plasmid prep kit) and neutralized (neutralisation buffer). The precipitates were separated by centrifugation for 10 mins and the absorbance of the supernatant measured with the nanodrop (Thermoscientific Nanodrop 2000 spectrophotometer).


    Results

    Graph 6 - Shows concentration of PPIX produced from various initial concentrations of ALA for E.coli cell culture concentration of 0.2mM. The most PPIX was produced from an initial ALA concentration of 5 mM as greater concentrations resulted in substrate inhibition (shown in figure 2 below).


    Graph 7 - Shows concentration of PPIX produced from various initial concentrations of ALA for E.coli cell culture concentration of 0.02mM. The most PPIX was produced from an initial ALA concentration of 5 mM as greater concentrations resulted in substrate inhibition (shown in figure 2 below).


    Discussion

    An initial ALA concentration of 5mM produced the optimum concentration of PPIX. This is likely to be due to substrate inhibition at greater concentrations where Protoporphyrinogen IX inhibits the conversion of ALA to porphobilinogen via porphobilinogen synthase (Stamford, Capretta, & Battersby, 1995).


    Moreover, the change in cell concentration did not change the production of PPIX, indicating that oxygen availability did not greatly influence the production of PPIX. The addition of glucose resulted in a subtle increase in PPIX production. As such, it cannot be deduced that glucose significantly impacts the production of PPIX. A slight difference was observed between the experimental PPIX formation and the predicted PPIX formation. We predicted the formation of 0.12 mM PPIX (Graph 1) from 1 mM ALA but only 0.065 mM of PPIX was produced (Graph 7 ).

    Fig 3- Protoporphyrinogen IX inhibiting the conversion of ALA to porphobilinogen via porphobilinogen synthase (Stamford, Capretta, & Battersby, 1995). This is a process of substrate inhibition which allows a certain concentration of ALA to produce an optimum amount of PPIX which in our case was 5mM (Stamford, Capretta, & Battersby, 1995).


    Conclusion

    Our experiments enabled us to improve our understanding of how the ALA to PPIX pathway operates. A substantial amount of PPIX was produced from ALA and the ratio of ALA:PPIX concentration was 1:8 as expected (Wachowska et al., 2011). It was speculated that ALA enters cells via passive transport, as no excess energy was needed to introduce ALA to E.coli. Oxygen availability did not have a significant impact on PPIX production as the change in concentration of cells little effect. Furthermore, due to substrate inhibition, an initial ALA concentration of 5mM resulted in the greatest yield of PPIX compared to the other concentrations used. Enzyme concentrations were not determined due to the excessive length of the experiments. This was also the case with other concentrations such as those of the intermediates.



    References
    • Alwan, A. F., Mgbeje, B., & Jordan, P. M. (1989). Purification and properties of uroporphyrinogen III synthase (co-synthase) from an overproducing recombinant strain of Escherichia coli K-12. Biochem. J, 264, 397-402.
    • Boynton, T. O., Daugherty, L. E., Dailey, T. A., & Dailey, H. A. (2009). Identification of Escherichia coli HemG as a novel, menadione-dependent flavodoxin with protoporphyrinogen oxidase activity. Biochemistry, 48(29), 6705-6711.
    • Breckau, D., Mahlitz, E., Sauerwald, A., Layer, G., & Jahn, D. (2003). Oxygen-dependent coproporphyrinogen III oxidase (HemF) from Escherichia coli is stimulated by manganese. Journal of Biological Chemistry , 278(47), 46625-46631.
    • Breinig, S., Kervinen, J., Stith, L., Wasson, A. S., Fairman, R., Wlodawer, A., . . . Jaffe, E. K. (2003). Control of tetrapyrrole biosynthesis by alternate quaternary forms of porphobilinogen synthase. Nature Structural & Molecular Biology, 10(9), 757-763.
    • Camadro, J.-M., Matringe, M., Scalla, R., & Labbe, P. (1991). Kinetic studies on protoporphyrinogen oxidase inhibition by diphenyl ether herbicides. Biochem. J, 277, 17-21.
    • Dixon, J. M., Taniguchi, M., & Lindsey, J. S. (2005). PhotochemCAD 2: A Refined Program with Accompanying Spectral Databases for Photochemical Calculations¶. Photochemistry and photobiology, 81(1), 212-213.
    • Jaffe, E. K., Martins, J., Li, J., Kervinen, J., & Dunbrack, R. L. (2001). The molecular mechanism of lead inhibition of human porphobilinogen synthase. Journal of Biological Chemistry, 276(2), 1531-1537.
    • Keleti, T., & Kramer, M. (1986). Basic enzyme kinetics: Akademiai Kiado Budapest.
    • Lawrence, S. H., Ramirez, U. D., Selwood, T., Stith, L., & Jaffe, E. K. (2009). Allosteric inhibition of human porphobilinogen synthase. Journal of Biological Chemistry, 284(51), 35807-35817.
    • Maneli, M. H., Corrigall, A. V., Klump, H. H., Davids, L. M., Kirsch, R. E., & Meissner, P. N. (2003). Kinetic and physical characterisation of recombinant wild-type and mutant human protoporphyrinogen oxidases. Biochimica et Biophysica Acta (BBA)-Proteins and Proteomics, 1650(1), 10-21.
    • Ryter, S. W., & Tyrrell, R. M. (2000). The heme synthesis and degradation pathways: role in oxidant sensitivity: heme oxygenase has both pro-and antioxidant properties. Free Radical Biology and Medicine , 28(2), 289-309.
    • Stamford, N. P. J., Capretta, A., & Battersby, A. R. (1995). Expression, purification and characterisation of the product from the Bacillus subtilis hemD gene, uroporphyrinogen III synthase. European Journal of Biochemistry , 231(1), 236-241.
    • Willows, R. (2004). Chlorophylls.
    • Wachowska, M., Muchowicz, A., Firczuk, M., Gabrysiak, M., Winiarska, M., Wańczyk, M., . . . Golab, J. (2011). Aminolevulinic acid (ALA) as a prodrug in photodynamic therapy of cancer. Molecules, 16(5), 4140-4164.