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Aim Perform a combustion simulation on the combustor model and plot the variation of the mass fraction of the different species’ in the simulation using line probes at different locations of the combustor as shown in Fig. You need to plot for CO2, H2O, CH4, N2, O2, NOx emissions & Soot formation. As a second…
Syed Saquib
updated on 14 Jun 2023
Aim
Introduction
Natural gas combustion is an exothermic chemical reaction in which natural gas and oxygen react, producing heat and several chemical byproducts. This reaction can be controlled and harnessed to generate heat for cooking and heating. It can also be used to power an electrical generator used to create electricity which can be used for lighting and other purposes. Natural gas is comprised primarily of methane. Sources for natural gas include fossil fuel deposits which can be processed to yield natural gas and biofuel generators which can be used to make methane from biological material. The gas is treated to make it as pure as possible, removing compounds which could impair the combustion process or generate pollution which would make combustion harmful to the environment.
In the past years strategies for the reduction in soot emissions relied mainly on correlations, experience and trial-and-error attempts. The increasingly diffusion of CFD is allowing to analyze and optimize combustion devices with sufficient confidence. However, the uncertainty increases significantly when soot is concerned: the complexity of the gas-phase chemistry and the numerous mechanisms involved in soot formation process, which are strongly coupled with mixing and radiative heat transfer and depend on soot volume fraction itself, make the prediction of soot emissions still a challenging task, leading to large errors in exhaust concentration even with small mispredictions in the formation rates
Different mechanisms are in fact involved in the determination of the final concentration at the exit of the combustion device, such as inception, coagulation, surface growth and oxidation. Even though reasonable predictions can be achieved on laminar diffusion flames , the scenario is further complicated when turbulent flames burning common fuels such as diesel or kerosene are concerned, as the applicability of models developed for simple aliphatic hydrocarbon fuels (such as methane) is questioned. Soot production in methane-air flames usually takes place from small species (e.g. acetylene) that grow to form polyaromatic hydrocarbons (PAH) and eventually soot.
Geometry
Mesh
Setup
So Since air contains mostly (79% nitrogen and 21% Oxigen )we have the equation for the reactants as CH4+ar(O2+3.76N2)��4+��(�2+3.76�2) where ar is the stoichiometric coefficient. And we have the product side as aCO2+bH2O+cN2���2+��2�+��2 ,
we have to balance the product side and reactant side using the coefficients a,b,c
Balancing carbon atoms , a =1.
Balancing Hydrogen atoms , 4=2b ⇒⇒b = 2.
For balancing 'ar' Take the coefficients of oxigen and nitrogen from products side and equate them
hence 2ar = 2a+b
ar =a + b/2
= 1+1 =2
Now we can fine the inlet Mass fractions for Fuel and air
Air contains 2 moles of Oxigen (O2) and 7.52 moles of Nitrogen , The Oxigen Mole fraction would be 2/(2+7.52) = 2/9.52 = 0.21 , when converted to mass fraction it would be 0.23
Since CH4 is only of 1 mole we can Input the fuel inlet with mass fraction of 1 for CH4 in Fuel inlet
Outputs
Part 1 - Baseline Simulation (No water injection with fuel)
Part 2-
Temperature Contours of Each cases
case-1 (5% of water injection)
Case 2 - Water Injection 10%
Case 3 - Water Injection 15%
Case 4 - Water Injection 20%
Case 5 - Water Injection 25%
Case 6 - Water Injection 30%
Plots
Comparison of Temperature plots of each cases
Observations
Comparison of soot plots of each cases
Observations
Comparison of NO plots of each cases
Comparison of Oxigen plots of each cases
Observations
Comparison of Carbon dioxide plots of each cases
Observations
Comparison of Carbon Monoxide plots of each cases
Observations
Water plots of each cases
Methane mass fractions of each cases
Nitrogen mass fractions of each cases
Parametric table
Conclusion
References
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