Numerical simulations of variable density starting jets

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1 Advances in Fluid Mechanics VII 409 Numerical simulations of variable density starting jets S. Benteboula 1,2 & G. Lauriat 3 1 UPMC Univ Paris 06, UMR 7598, Laboratoire Jacques-Louis Lions F-75005, Paris, France 2 CEA Saclay, DM2S/SFME/LTMF, Gif sur Yvette Cedex, France 3 Université Paris-Est, Laboratoire de Modélisation et Simulation Multiéchelle FRE 3160 CNRS, Marne-la-Vallee, France Abstract This work aims at developing computing tools for the numerical simulation of impulsively started jets with variable physical properties due to large thermal gradients. The fluid is injected at temperature T j and density ρ j in a quiescent surroundings at different temperature and density T a, ρ a. The 3D-time dependent Navier Stokes equations, formulated in the low Mach number approximation, were numerically integrated by using a non divergence-free projection method. The computations were performed for 3D and axisymmetric jets, and for a wide range of the jet-to-ambient density ratio, α = ρ j /ρ a, providing the expected flow features. Exceptthe formation of a leading vortex in the head of the flow followed by a jet stem, the results show that the behaviour and the dynamics are quite different for hot and cold jets. The hot jet is indeed characterised by a leading vortex in which the hotter fluid is concentrated, while the vortex ring is a region of intermediate temperature and density for a cold jet. Particular attention is given to the influence of α on the integral characteristics of vortex rings such as circulation and impulse. Keywords: numerical simulation, anisothermal vortex ring, low mach number flow, variable density. 1 Introduction The fluid injection through an orifice or a nozzle in a stagnant atmosphere leads to the generation of a vortex ring followed by a tail. Vortex rings are encountered doi: /afm080401

2 410 Advances in Fluid Mechanics VII in nature, cyclones, human heart, and in several industrial applications such as internal combustion engines. Experimentally, the vortex ring is obtained with a piston-cylinder mechanism by pushing a column of fluid. The boundary layers at the orifice edge separate and roll up into a vortex ring which detaches from the rear flow and travels downstream induced by its own momentum. During its evolution, the vortex grows by viscous diffusion and entrainment of the surrounding fluid. For long-time injections, Kelvin Helmholtz instabilities may develop in the trailing layer with more vortex interactions. Vortex rings were the subject of numerous studies based on the constant density assumption. For a general review on the generation, formation, evolution and interaction of vortex rings, the reader could refer to Shariff and Leonard [1]. Theoretically, there are two models that predict evolution laws of the vortex characteristics. The first one (Saffman [2]) relies on the similarity theory while the slug-flow model estimates the circulation, impulse and energy, using the injection program only. In the present work, started jets with large density and temperature differences are investigated to get an insight into more complicated flows such as combustion which involves vortex ring dynamics. The flow is assumed to be laminar and the injection velocity small enough to consider applicable the formulation of the 3D Navier Stokes equations derived in the low Mach number approximation. This model, proposed by Majda and Sethian [3] for combustion problems with premixed flames, is intermediate between the compressible and incompressible Navier Stokes equations. Few results are available in the open literature about the variable density vortex rings, in particular the influences of the jet-to-ambient density ratio on the vortex characteristics. To our best knowledge, there is only a brief recent communication of Iglesias et al. [4] in which the authors suggest an extension of the slug-flow model to estimate circulation of variable density vortex rings. Computations of variable density flows at low Mach number by using fully compressible Navier Stokes equations solvers are not well adapted for industrial flows. This is due to the large differences between the acoustic and the advective scales. Thus, very small time steps are required for stability conditions. In this study, an incompressible algorithm [5] was extended to handle non divergence-free velocity flows ( v 0). This approach is used in different ways by several authors (see Nicoud [6], Cook and Riley [7], Najm et al. [8]). By applying the low Mach number approximation to the Navier Stokes equations, acoustic waves are removed while the convective modes are described. In these conditions, large density variations due to thermal effects are allowed irrespective of pressure fluctuations, for instance, in combustion. In what follows, the mathematical model of the Navier Stokes equations is first introduced within the framework of the low Mach number approximation. We describe then the numerical procedure used to integrate the governing equations. Results for variable density vortex rings simulations with different ratios α are discussed for both cases of hot and cold jets. The simulations are compared to the reference case of an incompressible vortex ring (α = 1).

3 Advances in Fluid Mechanics VII Governing equations The fully compressible Navier Stokes equations are nondimensionalized by using the reference quantities associated to the injected fluid. Let Dj,V j, ρ j, T j be the orifice diameter, velocity, density and temperature, respectively. The buoyancy forces are neglected. We define the Mach, Reynolds and Prandtl numbers as: Ma = Vj / γrtj, Re = ρ j V j D j /µ j, Pr = µ j C p /λ j. All the primitive variables of the flow are then expanded in power series law of the small parameter ɛ (ɛ = γ Ma 2 1). Under the hypothesis that the flow is fully described by the advective space and time scales, the single scale asymptotic analysis (Müller [9]) leads to the following Navier Stokes equations of zero order. continuity equation ρ 0 + (ρ 0 v 0 ) = 0 (1) momentum equations (ρ 0 v 0 ) + (ρ 0 v 0 v 0 ) = p Re τ 0 (2) The shear stress tensor τ 0 for a Newtonian fluid is given by τ 0 = 2 3 µ( v 0) I + µ( v 0 + t v 0 ) The viscosity variation is approximated by the following power law µ = T σ 0 with σ 0.5 (3) energy equation in term of density ρ 0 + v 0 ρ 0 = 1 [ ] 1 T 0 RePr (µ T 0) (4) Eq. (4) is obtained by combining the energy, the continuity equations and the equation of state (see Cook and Riley [7]). Another form of the energy equation can be derived in term of temperature (see Najm et al. [8]). At the order 1, the momentum equations reduce to p 0 = 0. (5) The most important outcome of the low Mach number approximation is the splitting of the pressure into two components: a thermodynamic pressure p 0 constant in space and allowed to vary in time according to Eq. (5), and a dynamic pressure p 1 decoupled from density and temperature fluctuations. Since we are considering an open computational domain, the thermodynamic pressure p 0 is also

4 412 Advances in Fluid Mechanics VII Figure 1: (a) Radial profile at the orifice exit, (b) velocity injection program. constant in time and is given by the equation of state for an ideal gas p 0 = ρ 0 T 0 = 1 (6) The equations are formulated in cylindrical coordinates (r,θ,z) for the set of conservative variables (ρ, ρq r,ρv θ,ρv z,p),whereq r = rv r. Initial and boundary conditions At t = 0, the density and temperature fields are assumed uniform within the computational domain, ρ = ρ a = 1/α, T = T a = α. Moreover, the dynamic pressure and all the velocities are set equal to zero. At z = 0, injection conditions are applied: ρv z (r, t) = f(r)g(t),ρq r = ρv θ = 0, where f(r) is the top hat jet profile proposed by Michalke [10] (Fig. 1(a)). The impulsive and longtime injection program g(t) in Fig. 1(b) controls the inflow velocity (see James and Madnia [11]). The density at the orifice z = 0and0 r< 0.5 is parameterised by the ratio α, ρ(r,t) = ρ a [1 + (α 1)f (r)g(t)]. At the exit z = L z, the dependent variables ρq r,ρv θ and ρv z in the momentum equations satisfy the convection equation X/ + C X/ z = 0. Note that the value of the phase speed C = 0.5 does not affect the solution because the velocities at the outlet are corrected at each time step to insure mass conservation. For the density, Neumann condition ρ/ z = 0 is used. At the axis r = 0, symmetry conditions are applied, except for the radial component ρq r which is set equal zero ( ρ/ r = ρv θ / r = ρv z / r = ρq r = 0). At the lateral boundary r = L r, Neumann conditions for the density and fluxes are applied ( ρ/ r = ρv θ / r = ρq r / r = ρv z / r = 0). These conditions allow the entrainment of fluid through the lateral boundary. In the θ direction, periodicity is imposed on all variables. 3 Numerical procedure The cylindrical computational domain was covered with a staggered grid, the fluxes and velocities being located at the centers of the faces and the scalar variables ρ,t,p at the center of the cells. A centered finite-differencescheme with a second-order accuracy was used for the spatial discretization. A total variation diminishing scheme (TVD) was employed for the conservative part (ρv)

5 Advances in Fluid Mechanics VII 413 of the convective terms in the energy equation Eq. (4), as in Vreugenhil and Koren [12] in order to damp spurious oscillations for high density ratios. The time integration method employed is an extension of the fractional-step method to the low Mach number regime with v 0. Different schemes (Benteboula [13]) were implemented and tested. The most efficient version in terms of CPU time is described here. The energy equation was firstly integrated with a first-order Euler scheme ρ n+1 ρ n t = ( A ρ + D ρ ) n where A ρ and D ρ are the convective and diffusive terms, respectively. A ρ = (ρv) ρ v, D ρ = 1 [ ] 1 T RePr (µ T) Next, the conservative momentum equations are advanced in time with a fractional-step method by using a second-order explicit Adams-Bashforth scheme. The resolution consists in two main steps: 1 Prediction: in this step, an intermediate solution ρv c is computed as ρv c ρ n v n c t = p n ( A c + C c + D c ) n 1 2 ( A c + C c + D c ) n 1 where v c = (rv r,v θ,v z ) and A c,c c,d c are the advective terms, coupled viscous terms and second-order derivatives viscous terms, respectively. 2 Projection: in order to satisfy the mass conservation, the following Poisson equation for the variable related to the pressure was solved n+1 = 1 t [ ρv c + ( ) ρ n+1 ], where ( ) ρ n+1 = 3ρn+1 4ρ n + ρ n 1 2 t A second-order backward scheme seemed to be well adapted to approximate ρ/ which is generally a source of instability, as reported in Nicoud [6]. The corrected velocity fields are then obtained from the following equation (ρv c ) n+1 ρv c = t n+1 The pressure gradient is next updated with p n+1 = p n + n+1. Finally, the temperature distribution is deduced from the equation of state, T n+1 = 1/ρ n+1, and the viscosity field from the power law µ n+1 = (T n+1 ) σ. 4 Results and discussion The computational domain is a cylinder of radius L r = 3 and length L z = 7, in which the fluid is injected through an orifice of radius r j = 0.5 located at the center of the cylinder. The cylinder was discretized with a grid of N θ N r

6 414 Advances in Fluid Mechanics VII Figure 2: Surfaces of constant vorticity (a) axisymmetric cold jet α = 2, ω θ = 0.5, 2, 5, (b) disturbed hot jet α = 1/2, ω θ = 3, 1.8, 3.5. N z = cells. For axisymmetric simulations N θ = 1. We consider Re = 1000, 2000 and Pr = 0.71 is kept constant. The effect of the jet-to-ambient density ratio is analysed for cold jets 1 <α 8, isothermal jet α = 1 and for hot jets 1/8 <α 1. 3D simulations of a vortex ring produced by impulsively started jets are shown in Figure 2(a) for axisymmetric cold jet and in Figure 2(b) for disturbed hot jet. It can be seen a roll up of the sheet of vorticity that leads to the formation of a toroidal vortex ring at the head of the flow, followed by a symmetric annular layer. The vortex ring moves downstream by inertial effects and grows by diffusion and entrainment of the surrounding fluid. 3D effects are highlighted in Figure 2(b) by applying a random azimutal perturbation to the spatial profile f(r). The surfaces of constant vorticity demonstrate how the resulting vortex ring is distorted by this perturbation which is shed in the trailing jet. In the following, the analysis is restricted to axisymmetric flow. The plots in Fig. 3 show the azimuthal vorticity ω θ = v r / z v z / r in the plane (r, z) at the same time t = 10. For hot jets, the roll-up of vorticity sheets is more intense and the core diameter of the leading vortex becomes smaller as the injected fluid is hotter. Furthermore, we observe the development of a negative vorticity layer at the head of the vortex as well as in the jet stem. This counter-rotation is due to the baroclinic torque that acts in regions of non-uniform density. On the other hand, Figure 3: Instantaneous vorticity contours, t = 10, Re = 1000, for different density ratios, negative vorticity.

7 Advances in Fluid Mechanics VII 415 Figure 4: Instantaneous temperature fields: hot jet α = 1/8, Re = 2000 (up), cold jet α = 8, Re = 1000 (down). the cold jet has a more voluminous and more inertial leading vortex which makes its penetration easier. Therefore, the vortex ring grows considerably by thermal diffusion when its vorticity decreases, as can be seen for α = 8. It should be noted that the negative vorticity near the inlet section is due to the formation of the stopping vortex. The temperature fields are shown in Fig. 4, during and after the injection, for both hot and cold jets with strong density contrasts. It is worth noting that the Reynolds number being based on the jet properties, the kinematic viscosity of the surrounding flow is smaller than the hot jet one by a factor α 1+σ.The high temperature fluid, initially distributed at the orifice section, is progressively conveyed toward the vortex ring. At time t = 12, the hot fluid is trapped into the vortex core while the ambient fluid is led into the axis region for t>12. Moreover, a sort of wake appears in the trailing flow with vortex pairing near the orifice exit. The maps in Fig. 4 (down) show that the colder fluid remains concentrated around the axis while the outer layer in contact with the surroundings is heated. Unlike the hot jet, the temperature values in the vortex core are now intermediate between those of the injected fluid and ambience. This outcome is due to the increase in thermal diffusivity with the temperature for constant Pr. The jet front, z f, is defined as the position on the axis where the scaled density (ρ ρ a )/(ρ j ρ a ) is equal to 0.5. Except during the initial time development, the curves in Fig. 5(a) display a linear evolution with an increase in the slope with α. As expected, the cold jet having more inertia and evolving into a surroundings of lower density, travels much faster andspreads all the morequicklyas α increases. While, the more viscous heated jets penetrate into the ambience more slowly. The corresponding front velocity, U v = dz f /dt, is shown in Fig. 5(b). Irrespective to the ratio α, the velocities considerably drop at the beginning of the vortex generation (t <2). They reach then an almost constant value, mainly for cold jets. The hot jets velocities exhibit a drop at the end of the injection program (t = 8).

8 416 Advances in Fluid Mechanics VII Figure 5: Time evolution (a) jet front, (b) front velocity for different α. Figure6:Timeevolution:(a) -totalcirculation,---slug-flowcirculation, (b) impulse. The time evolution of the total circulation, Ɣ = L z 0 0 ω θ drdz, is compared to the circulation, Ɣ = t [1 + U v 2 (1 α)], predicted by the slug-flow model (Iglesias et al. [4]) for different ratios α in Fig. 6. This model assumes a constant velocity at the orifice equal to the piston one and requires a prior knowledge of the vortex velocity U v which is computed in a post-processing (Fig. 5(b)). The circulation presents an almost linear evolution, in particular, for cold jets. The growth rate of the circulation is larger when increasing values of α. The comparison with the slug-flow model shows a rather good agreement although this model overestimates the circulation for hot and isothermal jets. The discrepancies are partly due to non-constant hot jets velocities and to the contribution of the radial component of the velocity which is neglected in the slug-flow model. The hydrodynamic impulse I = π L z Lr 0 0 ω θ r 2 drdz delivered in the streamwise direction by the vortex is more important for cold jets compared to hot jets. Significant growth during the fluid discharge is noticed for α = 8. The large differences between the impulse curves are mainly due to the influence of the vortex sizes in the crosswise direction r. To account for the smaller values of circulation and impulse for hot jets, we can examine the plots of the vorticity in Fig. 3. Indeed, the vorticity is considerably higher compared to that of the cold jet but at the same time it is in part balanced by the negative one in the integration. Furthermore, the vortices are confined in a narrow region in the vicinity of the orifice rim. On the other hand, even if the vorticity of the cold jet is small, the vortex is shed on much broader region. Lr

9 Advances in Fluid Mechanics VII Conclusion A computational code for simulating variable density jets and appropriate for dealing with strong density and temperature contrasts was developed. Simulations performed for different injection cases of hot or cold fluid allow to describe the jet flow dynamics and thermals. The influences of the jet-to-ambient density ratio on the vorticity and temperature distributions as well as on the characteristics of the leading vortex ring (circulation, jet front and impulse) are discussed. These effects are found to amplify when increasing the density ratio α. Our results are in a good agreement with the theoretical slug-flow model. References [1] Shariff, K. & Leonard, A., Vortex rings. Ann Rev Fluid Mech, 24, pp , [2] Saffman, P.G., The number of waves on unstable vortex rings. J Fluid Mech, 84, p. 625, [3] Majda, A. & Sethian, J., The derivation and numerical solution of the equation for zero mach number combustion. Combust Sci Technol, 42, p. 185, [4] Iglesias, I., Vera, M. & Antonio, L.S., Simulations of starting gas jets at low mach numbers. Phys Fluids, 17, p , [5] Danaila, I. & Benteboula, S., Etude numérique et théorique des structures tourbillonnaires dans une injection gaz-gaz. simulations numériques directes avec les codes jetles et avbp. Technical report, Paris 6 et Institut Français du Pétrole, [6] Nicoud, F., Conservative high-order finite-difference scheme for low-mach number flows. J Comput Physics, 158, pp , [7] Cook, A.W. & Riley, J.J., Direct numerical simulation of a turbulent reactive plume on a parallel computer. J Comput Physics, 129, pp , [8] Najm, H.N., Wyckoff, P. & Knio, O.M., A semi-implicite numerical scheme for reacting flow. J Comput Physics, 143, p. 381, [9] Müller, B., Low mach number asymptotics of the navier-stokes equations. Journal of Ingineering Mathematics, 34, pp , [10] Michalke, A., Survey on jet instability theory. Prog Aerospace Sci, 21, p. 159, [11] James, S. & Madnia, C.K., Direct numerical simulation of a laminar vortex ring. Phys Fluids, 8, p. 2400, [12] Vreugenhil, C.B. & Koren, B., Numerical methods for advection-diffusion problems, volume 45. Vieweg, Braunschweig, [13] Benteboula, S., Résolution des équations de Navier Stokes à faible nombre Mach-Application à l anneau de vorticité à masse volumique variable. Ph.D. thesis, Université Paris-Est de Marne-la-Vallée, 2006.

DNS of Reacting H 2 /Air Laminar Vortex Rings

46th AIAA Aerospace Sciences Meeting and Exhibit 7-10 January 2008, Reno, Nevada AIAA 2008-508 DNS of Reacting H 2 /Air Laminar Vortex Rings Jeff Doom and Krishnan Mahesh University of Minnesota, Minneapolis,