3.5 Alternative Forms of the Energy Equation
Chalmers University of Technology
Department of Mechanical Engineering
Division of Fluid Dynamics
Total internal energy is defined as
eo=e+21v⋅v Inserted in Eqn. (3.57), this gives
ρDtDe+ρv⋅DtDv+∇⋅(pv)=ρf⋅v+q˙ρ Now, let’s replace the substantial derivative Dv/Dt using the momentum equation on non-conservation form (Eqn. (3.51)).
ρDtDe−v⋅∇p+ρf⋅v+∇⋅(pv)=ρf⋅v+q˙ρ Now, expand the term ∇⋅(pv) gives
ρDtDe−v⋅∇p+v⋅∇p+p(∇⋅v)=q˙ρ⇒ρDtDe+p(∇⋅v)=q˙ρ Divide by ρ
DtDe+ρp(∇⋅v)=q˙ Conservation of mass gives
DtDρ+ρ(∇⋅v)=0⇒∇⋅v=−ρ1DtDρ Insert in Eqn. (3.62)
DtDe−ρ2pDtDρ=q˙⇒DtDe+pDtD(ρ1)=q˙ DtDe+pDtDν=q˙ Compare with the first law of thermodynamics: de=δq−δw
h=e+ρp⇒DtDh=DtDe+ρ1DtDp+pDtD(ρ1) with De/Dt from Eqn. (3.62)
DtDh=q˙−pDtD(ρ1)+ρ1DtDp+pDtD(ρ1) DtDh=q˙+ρ1DtDp ho=h+21vv⇒DtDho=DtDh+v⋅DtDv From the momentum equation (Eqn. (3.51))
DtDv=f−ρ1∇p which gives
DtDho=DtDh+v⋅f−ρ1v⋅∇p Inserting Dh/Dt from Eqn. (3.68) gives
DtDho=q˙+ρ1DtDp+v⋅f−ρ1v⋅∇p=ρ1[DtDp−v⋅∇p]+q˙+v⋅f The substantial derivative operator applied to pressure
DtDp=∂t∂p+v⋅∇p and thus
DtDp−v⋅∇p=∂t∂p which gives
DtDho=ρ1∂t∂p+q˙+v⋅f If we assume adiabatic flow without body forces
DtDho=ρ1∂t∂p If we further assume the flow to be steady state we get
DtDho=0 This means that in a steady-state adiabatic flow without body forces, total enthalpy is constant along a streamline.