A more accurate projection in the rate-controlled constrained-equilibrium method for dimension reduction of combustion chemistry

The rate-controlled constrained-equilibrium (RCCE) method for dimension reduction of combustion chemistry is revisited from a geometric viewpoint. A constrained equilibrium manifold (CEM) is defined as all compositions that satisfy the maximum-entropy or minimum-free energy conditions of the gas mixture, subject to specified constraints. The RCCE method is based solely on thermodynamics, and it is shown that this method contains a hidden assumption of an orthogonal projection that projects the rate equation of the chemical system onto the CEM. An extension of the RCCE method is constructed by making an alternative projection based on the conjecture that, near the CEM, there is a close parallel inertial manifold (CPIM). The CPIM assumption introduces the chemical kinetics directly through the local Jacobian and hence leads to greater accuracy than RCCE. The comparison between the RCCE method and its extension is made in the test calculations of hydrogen–air and methane–air autoignition.

[1]  Stephen B. Pope,et al.  Implementation of combustion chemistry by in situ adaptive tabulation of rate-controlled constrained equilibrium manifolds , 2002 .

[2]  Sanford Gordon,et al.  Computer program for calculation of complex chemical equilibrium compositions , 1972 .

[3]  Mitchell D. Smooke,et al.  Reduced Kinetic Mechanisms and Asymptotic Approximations for Methane-Air Flames: A Topical Volume , 1991 .

[4]  Robert W. Dibble,et al.  Pdf Modeling of Turbulent Nonpremixed Methane Jet Flames , 1989 .

[5]  J.-Y. Chen,et al.  A self-organizing-map approach to chemistry representation in combustion applications , 2000 .

[6]  Chung King Law,et al.  An augmented reduced mechanism for methane oxidation with comprehensive global parametric validation , 1998 .

[7]  W. C. Reynolds,et al.  The Element Potential Method for Chemical Equilibrium Analysis : Implementation in the Interactive Program STANJAN, Version 3 , 1986 .

[8]  U. Maas,et al.  A general algorithm for improving ILDMs , 2002 .

[9]  J. Warnatz,et al.  Ignition processes in carbon-monoxide-hydrogen-oxygen mixtures , 1989 .

[10]  Tamás Turányi,et al.  Parameterization of Reaction Mechanisms Using Orthonormal Polynomials , 1994, Comput. Chem..

[11]  James C. Keck,et al.  Constrained-equilibrium calculations for chemical systems subject to generalized linear constraints using the NASA and STANJAN equilibrium programs , 1997 .

[12]  V. Yousefian,et al.  A Rate-Controlled Constrained-Equilibrium Thermochemistry Algorithm for Complex Reacting Systems , 1998 .

[13]  H. Rabitz,et al.  High Dimensional Model Representations , 2001 .

[14]  James C. Keck,et al.  Rate-controlled constrained-equilibrium method using constraint potentials , 1998 .

[15]  J. Keck Rate-controlled constrained-equilibrium theory of chemical reactions in complex systems☆ , 1990 .

[16]  James C. Keck,et al.  Rate-controlled partial-equilibrium method for treating reacting gas mixtures , 1971 .

[17]  Stephen B. Pope,et al.  Computationally efficient implementation of combustion chemistry using in situ adaptive tabulation , 1997 .

[18]  Michael Frenklach,et al.  PRISM: piecewise reusable implementation of solution mapping. An economical strategy for chemical kinetics , 1998 .

[19]  Ulrich Maas,et al.  Simplifying chemical kinetics: Intrinsic low-dimensional manifolds in composition space , 1992 .

[20]  Stephen B. Pope,et al.  Probability density function calculations of local extinction and no production in piloted-jet turbulent methane/air flames , 2000 .

[21]  Forman A. Williams,et al.  The asymptotic structure of stoichiometric methaneair flames , 1987 .

[22]  W. E. Stewart,et al.  Sensitivity analysis of initial value problems with mixed odes and algebraic equations , 1985 .