Team:Braunschweig/Modeling-content
From 2014.igem.org
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- | Degradation of methane took 3.5 times longer if E. cowli was immobilized (see FIG 4 ). Based on Michaelis-Menten kinetics and our mathematical model an initial concentration of 2.3 µM was estimated corresponding to the amount of active enzyme. In comparison, the amount of initial, active enzyme in non immobilized E. cowli has been 2.4 times higher. However this was not unexpected. The beads were manually produced via polymerization of the alginate. Residual alginate as well as natural product loss led to reduction of used cells and ultimately to a loss of enzyme. This was quantified by subsequent weighing of residual alginate. The loss amounted approximately 32 % due to an unoptimized method and a high viscosity of the alginate solution. Moreover a possible explanation for the loss of activity lies in the variation of pH between the media. The activity of sMMO has been reported to be highly dependent on the milieu [11]. | + | Degradation of methane took 3.5 times longer if <i>E. cowli</i> was immobilized (see FIG 4 ). Based on Michaelis-Menten kinetics and our mathematical model an initial concentration of 2.3 µM was estimated corresponding to the amount of active enzyme. In comparison, the amount of initial, active enzyme in non immobilized <i>E. cowli</i> has been 2.4 times higher. However this was not unexpected. The beads were manually produced via polymerization of the alginate. Residual alginate as well as natural product loss led to reduction of used cells and ultimately to a loss of enzyme. This was quantified by subsequent weighing of residual alginate. The loss amounted approximately 32 % due to an unoptimized method and a high viscosity of the alginate solution. Moreover a possible explanation for the loss of activity lies in the variation of pH between the media. The activity of sMMO has been reported to be highly dependent on the milieu [11]. |
- | Fortunately the pH of ruminal fluid fluctuates between 6.7 and 7.2 [7]. The measured pH values of the ruminal fluid and the NMS-media were 6.7 corresponding to a 36% loss in activity. Thus approximately only 43.52 % of the initial enzyme is active, representing the worst case scenario. An industrial production of alginate beads for entrapment is much more effective.<br><br> | + | Fortunately the pH of ruminal fluid fluctuates between 6.7 and 7.2 [7]. The measured pH values of the ruminal fluid and the NMS-media were 6.7 corresponding to a 36 % loss in activity. Thus approximately only 43.52 % of the initial enzyme is active, representing the worst case scenario. An industrial production of alginate beads for entrapment is much more effective.<br><br> |
- | Furthermore a discrepancy between cultivation of immobilized E. cowli in NMS-media and ruminal fluid was observed. The cultivation in NMS-media resulted in a slightly lower rate of methane degradation if compared to cultivation in rumen fluid, which is discussed in the <a href="https://2014.igem.org/Team:Braunschweig/Results-content#resultspart3"</a>results.<br> | + | Furthermore a discrepancy between cultivation of immobilized <i>E. cowli</i> in NMS-media and ruminal fluid was observed. The cultivation in NMS-media resulted in a slightly lower rate of methane degradation if compared to cultivation in rumen fluid, which is discussed in the <a href="https://2014.igem.org/Team:Braunschweig/Results-content#resultspart3"</a>results.<br> |
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- | The immobilization of E. cowli in a calcium alginate matrix allows growth and enzymatic activity while cultivated in ruminal fluid. The costs for production of alginate beads shall be evaluated subsequently. As previously determined a total active enzyme amount of 244 g is necessary for complete degradation of methane produced through enteric fermentation. | + | The immobilization of <i>E. cowli</i> in a calcium alginate matrix allows growth and enzymatic activity while cultivated in ruminal fluid. The costs for production of alginate beads shall be evaluated subsequently. As previously determined a total active enzyme amount of 244 g is necessary for complete degradation of methane produced through enteric fermentation. |
In this project beads were manually produced using transfer pipettes, thus the diameter was 7 mm in average with 4×10<sup>9</sup> cells. Consequently a total of 750 beads is needed to reduce the methane emission to a minimum, which have a retention time of 4 days in the cows rumen. For reduction of the costs the bead composition can be optimized. It has been reported that small amounts of paraffin increase the solubility of methane in the liquid phase vastly [12]. However the health effects of paraffin has to be evaluated.<br><br> | In this project beads were manually produced using transfer pipettes, thus the diameter was 7 mm in average with 4×10<sup>9</sup> cells. Consequently a total of 750 beads is needed to reduce the methane emission to a minimum, which have a retention time of 4 days in the cows rumen. For reduction of the costs the bead composition can be optimized. It has been reported that small amounts of paraffin increase the solubility of methane in the liquid phase vastly [12]. However the health effects of paraffin has to be evaluated.<br><br> | ||
Our costs for the production were 50 cent per ratio, which consists of 750 beads. Hence a total of 50 $ per year is needed to reduce the annual methane emission by 110 kg per cow. Ideally the worldwide methane emission is reduced by 164 milion tons, based on a total number of 1.5 billion cows [13]. This is the ideal case. Nevertheless in case only 1% percent of the sMMO is active if immobilized and introduced into the rumen, the methane emission is reduced by 164 ×10<sup>4</sup> tons.<br><br> | Our costs for the production were 50 cent per ratio, which consists of 750 beads. Hence a total of 50 $ per year is needed to reduce the annual methane emission by 110 kg per cow. Ideally the worldwide methane emission is reduced by 164 milion tons, based on a total number of 1.5 billion cows [13]. This is the ideal case. Nevertheless in case only 1% percent of the sMMO is active if immobilized and introduced into the rumen, the methane emission is reduced by 164 ×10<sup>4</sup> tons.<br><br> |
Revision as of 13:28, 17 October 2014
Modeling Approach
Due to the increasing consume of Beef and dairy products cattle are nowadays a major contributor to the emission of greenhouse gases, thus vastly affecting global warming. In this year’s project the iGEM Team Braunschweig is aiming at reducing the cows’ share of the cake by designing a methane degrading bacterium – E. cowli.
However, due to safety and ethical concerns it is not easily manageable to test our system in vivo. Nonetheless, the effects of E. cowli on methane emissions by cattle need to be evaluated. Therefore we created a mathematical model simulation based on data experimentally obtained in this project and previously published literature. The model was used to evaluate eventual costs and a theoretical scale-up of the system.
Mathematical Model
In this year’s iGEM project our objective is to decrease the amount of methane produced through enteric fermentation inside the cows’ rumen without affecting the internal microbiota. Produced methane is subsequently released from the digestive tract through the mouth by eructation or burping. To inhibit the emission, thus reducing the atmospheric methane levels, we established a methane degrading bacterium – E. cowli
Our mathematical model, based on laboratory and literature data, provides an overview of the efficiency and impact of our system.
E. cowli is capable of utilizing methane for the production of methanol. Methanol is subsequently excreted and metabolized by other organisms of the cows’ microbiota [1]. To degrade methane E. cowli uses the well-characterized enzyme complex soluble methane monooxygenase (sMMO) from M. capsulatus catalyzing the conversion of methane to methanol with simultaneous consumption of oxygen and the cofactor NADH+H+ (see eq. 1 and eq. 2).
According to literature data the reaction kinetics can be described using Michaelis-Menten kinetics [2]. Kinetic parameters varied from 3 to 23 µM for the Michaelis-Menten constant (KM), thus the most confident values shown in table 1 were selected for modeling.