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Chemical source term equilibrium-chemistry limit

In Section 5.1, we have seen (Fig. 5.2) that the molar concentration vector c can be transformed using the SVD of the reaction coefficient matrix T into a vector c that has Nr reacting components cr and N conserved components cc.35 In the limit of equilibrium chemistry, the behavior of the Nr reacting scalars will be dominated by the transformed chemical source term S. 36 On the other hand, the behavior of the N conserved scalars will depend on the turbulent flow field and the inlet and initial conditions for the flow domain. However, they will be independent of the chemical reactions, which greatly simplifies the mathematical description. [Pg.176]

Thus, for a turbulent reacting flow in the equilibrium-chemistry limit, the difficulty of closing the chemical source term is shifted to the problem of predicting / ( x, t). [Pg.198]

In summary, in the equilibrium-chemistry limit, the computational problem associated with turbulent reacting flows is greatly simplified by employing the presumed mixture-fraction PDF method. Indeed, because the chemical source term usually leads to a stiff system of ODEs (see (5.151)) that are solved off-line, the equilibrium-chemistry limit significantly reduces the computational load needed to solve a turbulent-reacting-flow problem. In a CFD code, a second-order transport model for inert scalars such as those discussed in Chapter 3 is utilized to find ( ) and and the equifibrium com-... [Pg.199]


See other pages where Chemical source term equilibrium-chemistry limit is mentioned: [Pg.257]    [Pg.16]    [Pg.175]    [Pg.201]    [Pg.226]    [Pg.156]    [Pg.182]    [Pg.207]    [Pg.436]   
See also in sourсe #XX -- [ Pg.177 ]

See also in sourсe #XX -- [ Pg.177 ]




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