Novel Approach for Computational Modeling of a Non-Premixed Rotating Detonation Engine
read more
Citations
Recent Progress, Development Trends, and Consideration of Continuous Detonation Engines
Modeling thermodynamic trends of rotating detonation engines
Investigation of counter-rotating shock wave and wave direction control of hollow rotating detonation engine with Laval nozzle
Modeling Thermodynamic Trends of Rotating Detonation Engines
Formation of multiple detonation waves in rotating detonation engines with inhomogeneous methane/oxygen mixtures under different equivalence ratios
References
Two-equation eddy-viscosity turbulence models for engineering applications
Towards the ultimate conservative difference scheme V. A second-order sequel to Godunov's method
An Interior Trust Region Approach for Nonlinear Minimization Subject to Bounds
Procedure for Estimation and Reporting of Uncertainty Due to Discretization in CFD Applications
On the convergence of interior-reflective Newton methods for nonlinear minimization subject to bounds
Related Papers (5)
Steady-State Analysis of Rotating Detonation Engine Flowfields with the Method of Characteristics
Thermodynamic analysis of a gas turbine engine with a rotating detonation combustor
Numerical Investigation of Rotating Detonation Engine Propulsive Performance
Frequently Asked Questions (17)
Q2. What are the future works in "Novel approach for computational modeling of a non- premixed rotating detonation engine" ?
The effect of product diluents on the wave structure, detonation cell size, and heat release using high-fidelity simulations is a part of the future work of the research group.
Q3. What is the simplest method for calculating the energy of the fluxes?
A coupled flow, coupled energy solver with a third-order implicit, Monotonic Upstream-Centered Scheme for Conservation Laws (MUSCL) [38] is used for spatial discretization of the fluxes.
Q4. How can The authorsolve the kinetics and viscous effects at these length scales?
Resolving the kinetics and viscous effects at these length scales are computationally expensive and require high-fidelity simulation methods such as Direct Numerical Simulation with AMR, which are currently beyond the scope of this work; however, the method presented in the present study can be applied to various levels of modeling inhomogeneous fuel-oxidizer injection.
Q5. What is the effect of the inhomogeneity of the reactant mixture?
The peak detonation pressure and detonability of the mixture are also affected by the inhomogeneity of the reactant mixture [13].
Q6. What is the effect of the fuel-product stratification on the detonation velocity?
The fuel-product stratification has a significant impact on the detonation velocity compared to heat loss from the RDE, as the detonation velocity drops in both these cases.
Q7. What is the reason for the interest in using hydrogen as fuel in RDEs?
The detonation cell size of hydrogen is small compared to most hydrocarbon fuels [56], which is the primary reason for the interest in using H2 as fuel in most RDEs [57].
Q8. How many microns are required to resolve the chemical kinetics and viscous effects?
Powers et al [51] state that the finest length scale required to fully resolve the chemical kinetics and viscous effects is 0.1 microns.
Q9. Who provided the computational resources to run the CFD simulations?
I thank the Advanced Research Computing (ARC) department of Virginia Tech for providing computational resources in their cluster to run the CFD simulations.
Q10. What is the probability density function of the fuel mass fraction from a converged 3-D?
A Probability Density Function (PDF) of the fuel mass fraction from a converged 3-D, non-reacting simulation is extracted and is used as a spatially and temporally varying inlet boundary condition in the 2-D simulation.
Q11. What is the method used in this work?
The method used in this work can be used for any injector design and is a powerful/efficient way to numerically analyze a Rotating Detonation Engine.
Q12. What are the advantages of numerical simulations of RDE?
Numerical simulations of RDE provide additional flexibility over experiments in understanding the flow field, analyzing physical/chemical processes, and detonation wave structures which propagate at or near sonic speeds.
Q13. How do the OH and H2O mass fractions differ with the ZND profile?
The OH and H2O mass fractions resemble the ZND profile, such that they vary linearly with local equivalence ratio up to the value of 1, beyond which the variation is gradual.
Q14. How large is the mesh size used for further analysis?
As the simulation results obtained using a grid size of 100 microns reasonably predicts the physics such as wave structures, with values of peak pressures, and detonation wave speeds close to the theoretical conditions and satisfies the global mass balance in the domain, in addition to having a low discretization error value (Table 1), this mesh size (100 microns) is used for further analysis in this study.
Q15. What is the effect of heat loss on the detonation velocity?
Tomeasure the effect of heat loss on the detonation velocity, a modified version of the system of equations Eqs. (14-16) is solved in which a heat loss term (Qloss) is added to Eq. (15) which then becomes Eq. (20)𝑒2 − 𝑒1 = 0.5 (𝑝22 − 𝑝1 2)𝛾2𝑝2𝜌2 − 𝑄𝑙𝑜𝑠𝑠 (20)Heat loss from the RDE also deters the detonation velocity (Fig. 23), although not as significant as fuel-product stratification.
Q16. What was the method used to account for the mixing length?
Paxson et al [33] utilized a method in which the first few grid cells of the computational domain were made non-reacting to account for the mixing length, although the inlet mixture was perfectly premixed.
Q17. What is the mean cell size for the non-premixed case?
The mean values measured using Shepherd’s code [58] are 3.895 mm and 3.825 mm respectively for the non-premixed and premixed cases.