1988
DOI: 10.2514/3.10013
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Finite-volume method for the calculation of compressible chemically reacting flows

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Cited by 148 publications
(39 citation statements)
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“…= pr,b ( + p) (9) where Le"1' and Pr are the Lewis number and the Prandtl number of vibrational mode 1, respectively. q1 is the heat flux vector which is represented as q1= (10) where C is the specific heat at constant pressure by molecular translational and rotational motions, ic is the molecular heat conductivity coefficient, Pr is the turbulent Prandtl number. The equation of state for perfect gas is available in the translational mode gas of = 1.4 using the method of Ruse " , which is almost minimum length, and (3) a S.(Straight) nozzle, which is conical behind the throat.…”
Section: Methodsmentioning
confidence: 99%
“…= pr,b ( + p) (9) where Le"1' and Pr are the Lewis number and the Prandtl number of vibrational mode 1, respectively. q1 is the heat flux vector which is represented as q1= (10) where C is the specific heat at constant pressure by molecular translational and rotational motions, ic is the molecular heat conductivity coefficient, Pr is the turbulent Prandtl number. The equation of state for perfect gas is available in the translational mode gas of = 1.4 using the method of Ruse " , which is almost minimum length, and (3) a S.(Straight) nozzle, which is conical behind the throat.…”
Section: Methodsmentioning
confidence: 99%
“…However, the application of multigrid methods to reactive flow calculations has been limited. Bussing and Murman (1988) The approach taken in this paper is to use a previously validated multigrid solver (Martinelli, 1987;Martinelli and Jameson, 1988;Tatsumi et al, 1994) and include chemical source terms on all levels (Sheffer, 1997;Sheffer et al, 1997b). The coarse grid corrections to the species densities are limited to ensure that no mass fraction becomes negative.…”
Section: Multigrid Convergence Accelerationmentioning
confidence: 99%
“…The chemical source vector w was treated in a point implicit manner (Bussing and Murman, 1988). An explicit treatment of the source terms leads, in general, to a time step restriction due to the stability limitation of the explicit scheme.…”
Section: Chemical Source Termsmentioning
confidence: 99%
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“…Reacting flows in the hypersonic regime [5][6][7], reactive mixing layers [8], flames [9], detonations [10][11][12] and nonequilibrium nozzle flows [13] are modeled by systems of partial differential equations (PDEs) and are frequently solved by a local implicit treatment of the stiff source terms according to the method of lines and the time-step or operator splitting approach. Preconditioning techniques are also used to solve steady state problems efficiently [11,14,52].…”
Section: Introductionmentioning
confidence: 99%