Open main menu
Home
Random
Recent changes
Special pages
Community portal
Preferences
About Wikipedia
Disclaimers
Incubator escapee wiki
Search
User menu
Talk
Dark mode
Contributions
Create account
Log in
Editing
Euler equations (fluid dynamics)
(section)
Warning:
You are not logged in. Your IP address will be publicly visible if you make any edits. If you
log in
or
create an account
, your edits will be attributed to your username, along with other benefits.
Anti-spam check. Do
not
fill this in!
===Thermodynamics of ideal fluids=== In [[thermodynamics]] the independent variables are the [[specific volume]], and the [[specific entropy]], while the [[specific energy]] is a [[function of state]] of these two variables. {{hidden |Deduction of the form valid for thermodynamic systems |Considering the first equation, variable must be changed from density to specific volume. By definition: <math display="block"> v \equiv \frac 1 \rho </math> Thus the following identities hold: <math display="block"> \nabla \rho = \nabla \left(\frac{1}{v}\right) = -\frac{1}{v^2} \nabla v</math> <math display="block"> \frac{\partial\rho}{\partial t} = \frac{\partial}{\partial t} \left(\frac{1}{v}\right) = -\frac{1}{v^2} \frac{\partial v}{\partial t} </math> Then by substituting these expressions in the mass conservation equation: <math display="block"> - \frac{\mathbf{u}}{v^2} \cdot \nabla v - \frac 1 {v^2} \frac {\partial v}{\partial t} = - \frac 1 v \nabla \cdot \mathbf{u} </math> And by multiplication: <math display="block"> {\partial v \over\partial t}+\mathbf u \cdot \nabla v = v \nabla \cdot \mathbf u </math> This equation is the only belonging to general continuum equations, so only this equation have the same form for example also in Navier-Stokes equations. On the other hand, the pressure in thermodynamics is the opposite of the partial derivative of the specific internal energy with respect to the specific volume: <math display="block">p(v, s) = - {\partial e(v, s) \over \partial v}</math> since the internal energy in thermodynamics is a function of the two variables aforementioned, the pressure gradient contained into the momentum equation should be explicited as: <math display="block">- \nabla p (v,s) = - \frac {\partial p}{\partial v} \nabla v - \frac {\partial p}{\partial s} \nabla s = \frac {\partial^2 e}{\partial v^2} \nabla v + \frac {\partial^2 e}{\partial v \partial s}\nabla s </math> It is convenient for brevity to switch the notation for the second order derivatives: <math display="block"> - \nabla p (v,s) = e_{vv} \nabla v + e_{vs} \nabla s </math> Finally, the energy equation: <math display="block">{D e \over Dt} = - p v \nabla \cdot \mathbf u </math> can be further simplified in convective form by changing variable from specific energy to the specific entropy: in fact the [[first law of thermodynamics]] in local form can be written: <math display="block">{D e \over Dt} = T {D s \over Dt} - p {D v \over Dt}</math> by substituting the material derivative of the internal energy, the energy equation becomes: <math display="block">T {D s \over Dt} + \frac p {\rho^2} \left( {D \rho \over Dt} + \rho \nabla \cdot \mathbf u \right) = 0</math> now the term between parenthesis is identically zero according to the conservation of mass, then the Euler energy equation becomes simply: <math display="block">{D s \over Dt} = 0</math> |style = border: 1px solid lightgray; width: 90%; |headerstyle = text-align:left; }} For a thermodynamic fluid, the compressible Euler equations are consequently best written as: {{Equation box 1 |indent=: |title='''Euler equations'''<br/>(''convective form, for a thermodynamic system'') |equation=<math>\begin{align} {Dv \over Dt} &= v \nabla \cdot \mathbf u\\[1.2ex] \frac{D\mathbf{u}}{Dt} &= ve_{vv}\nabla v + ve_{vs}\nabla s + \mathbf{g} \\[1.2ex] {Ds \over Dt} &= 0 \end{align}</math> |cellpadding |border |border colour = #FFFF00 |background colour = #ECFCF4 }} where: * <math>v</math> is the specific volume * <math>\mathbf u</math> is the flow velocity vector * <math>s</math> is the specific entropy In the general case and not only in the incompressible case, the energy equation means that '''for an inviscid thermodynamic fluid the specific entropy is constant along the [[flow lines]]''', also in a time-dependent flow. Basing on the mass conservation equation, one can put this equation in the conservation form:{{sfn|Landau|Lifshitz|2013|p=4|loc= Eqs 2.6 and 2.7}} <math display="block">{\partial \rho s \over \partial t} + \nabla \cdot (\rho s \mathbf u) = 0,</math> meaning that for an inviscid nonconductive flow a continuity equation holds for the entropy. On the other hand, the two second-order partial derivatives of the specific internal energy in the momentum equation require the specification of the [[fundamental equation of state]] of the material considered, i.e. of the specific internal energy as function of the two variables specific volume and specific entropy: <math display="block">e = e(v, s).</math> The ''fundamental'' equation of state contains all the thermodynamic information about the system (Callen, 1985),{{sfn|Henderson|2000|p=152|loc=2.6 Thermodynamic properties of materials}} exactly like the couple of a ''thermal'' equation of state together with a ''caloric'' equation of state.
Edit summary
(Briefly describe your changes)
By publishing changes, you agree to the
Terms of Use
, and you irrevocably agree to release your contribution under the
CC BY-SA 4.0 License
and the
GFDL
. You agree that a hyperlink or URL is sufficient attribution under the Creative Commons license.
Cancel
Editing help
(opens in new window)