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Modern Engineering Thermodynamics

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19.3 Linear Phenomenological Equations 765<br />

Table 19.3 Entropy Production Rate Density One-Dimensional and Three-Dimensional<br />

Formulae<br />

Entropy Production Rate Density Due To<br />

Heat transport of energy<br />

Viscous dissipation<br />

Electrical energy dissipation<br />

Diffusion of n dissimilar chemical species<br />

EPRD Formula<br />

<br />

σ Q = − _q <br />

dT<br />

= ! q .∇ ! 1 <br />

T 2 dx T<br />

ðσ W Þ vis<br />

= μ <br />

dV 2<br />

= τ: ! ∇ ! V<br />

T dx e<br />

ðσ W Þ elect<br />

= ρ e J 2 E /T = − E! . ! J E /T<br />

ðσ m Þ diff<br />

= ∑ n<br />

i =1<br />

J_<br />

ix<br />

. d dx<br />

^μi<br />

<br />

= ∑ n<br />

T<br />

i =1<br />

!<br />

Ji .∇ ! μ <br />

i<br />

T<br />

Table 19.4 Generalized EPRD One-Dimensional Flux and Force Formulae<br />

Entropy Production<br />

Rate Density (σ)<br />

Generalized Energy<br />

Transport Flux (J)<br />

Generalized Energy<br />

Transport Force (X)<br />

σ Q _q = ! q /A = heat flux vector − 1 <br />

dT <br />

T 2 dx<br />

<br />

ðσ W Þ vis μ dV <br />

<br />

1<br />

dx<br />

T dV <br />

dx<br />

ðσ W Þ J E = I/A = electron flux ρ e J e<br />

elect = −<br />

T T<br />

1 <br />

dϕ<br />

dx<br />

<br />

ðσ m Þ _<br />

diff<br />

J ix = mass flux of chemical<br />

d ^μi<br />

species i in the x direction<br />

dx T<br />

In Table 19.3 J E = I/A = the current (electron) flux. Note that each σ listed in Table 19.3 has the form<br />

σ = JX = J ! . X ! =<br />

e<br />

J :<br />

e<br />

X (19.1)<br />

where J, ! J , J = generalized (scalar, vector, or tensor) energy transport flux, and X, ! X , X = generalized (scalar, vector,<br />

or tensor) e energy transport driving force producing the flux.<br />

e<br />

Table 19.4 identifies the various flux and force terms associated with the entropy production rate density formulae<br />

given in Table 19.3.<br />

For any system containing a number of entropy production rate densities resulting from the simultaneous operation<br />

of a number of irreversible processes, the total EPRD is simply the sum of all the individual EPRDs present<br />

within the system. Also, the second law of thermodynamics requires that the total EPRD be positive, so<br />

σ total = σ Q + ðσ W Þ vis + ðσ W Þ elect + ðσ m Þ diff + … > 0 (19.2)<br />

Using the generalized flux-force formulation, this can be written for m such densities as<br />

σ total = J Q X Q + ðJ W X W Þ vis + … = ∑ m<br />

J i X i > 0 (19.3)<br />

19.3 LINEAR PHENOMENOLOGICAL EQUATIONS<br />

We begin by postulating that all simultaneously occurring physical phenomena that can be coupled are coupled<br />

to each other in some way. This is succinctly stated in the “coupling postulate.”<br />

For example, consider a system that has two energy transport fluxes, J 1 and J 2 , which result from two generalized<br />

forces, X 1 and X 2 . The coupling postulate states that<br />

and<br />

J 1 = J 1 ðX 1 , X 2 Þ<br />

J 2 = J 2 ðX 1 , X 2 Þ<br />

Expanding J 1 about the “equilibrium” state X 1 = X 2 = 0 using a Taylor’s series gives<br />

J 1 ðX 1 , X 2 Þ≃J 1 ð0, 0Þ + ∂J 1<br />

∂X 1<br />

dX 1 + ∂J 2<br />

∂X 2<br />

dX 2 + higher order terms<br />

i=1

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