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Reaction-progress variables initial/inlet conditions

The dimensionless vector of reaction-progress variables Y is then defined to be null in the initial and inlet conditions, and obeys... [Pg.200]

Using the same inlet/initial conditions as were employed for the one-step reaction, this reaction system can be written in terms of two reaction-progress variables (Fi, Y2) and the mixture fraction f. A linear relationship between c and (co, Y, f) can be derived starting from (5.162) with y = Y2 = A0B0/(A0 + B0) ... [Pg.204]

Unlike for the mixture fraction, the initial and inlet conditions for the mean and variance of Y will be zero. Thus, the chemical source term will be responsible for the generation of non-zero values of the mean and variance of the reaction-progress variable inside the reactor. Appealing again to the assumption of independence, the mean reaction-progress variable is given by... [Pg.237]

Note that the reaction-progress vector in the first column is non-zero. Thus, as we suspected, the mixture-fraction basis is not a linear-mixture basis. The same conclusion will be drawn for all other mixture-fraction bases found starting from (5.118). For these initial and inlet conditions, a two-component mixture-fraction vector can be found however, it is of no practical interest since the number of conserved-variable scalars is equal to Nq,m = 1 (k e 0, 1, 2). In conclusion, although the mixture fraction can be defined for the... [Pg.190]


See other pages where Reaction-progress variables initial/inlet conditions is mentioned: [Pg.190]    [Pg.171]   
See also in sourсe #XX -- [ Pg.183 , Pg.204 ]

See also in sourсe #XX -- [ Pg.183 , Pg.204 ]




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Initial conditions

Initiation conditions

Initiation reaction

Inlet

Inlet conditions

Progress variable

Reaction condition

Reaction initiated

Reaction progress

Reaction progress variable

Reaction variable

Reaction-progress variables conditional

Variable conditions

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