Euler equations (fluid dynamics)
In fluid dynamics, the Euler equations are a set of quasilinear hyperbolic equations governing adiabatic and inviscid flow. They are named after Leonhard Euler. The equations represent Cauchy equations of conservation of mass (continuity), and balance of momentum and energy, and can be seen as particular Navier–Stokes equations with zero viscosity and zero thermal conductivity. In fact, Euler equations can be obtained by linearization of some more precise continuity equations like Navier-Stokes equations in around a local equilibrium state given by a Maxwellian[disambiguation needed]. The Euler equations can be applied to incompressible and to compressible flow – assuming the flow velocity is a solenoidal field, or using another appropriate energy equation respectively (the simplest form for Euler equations being the conservation of the specific entropy). Historically, only the incompressible equations have been derived by Euler. However, fluid dynamics literature often refers to the full set – including the energy equation – of the more general compressible equations together as "the Euler equations".
From the mathematical point of view, Euler equations are notably hyperbolic conservation equations in the case without external field (i.e. in the limit of high Froude number). In fact, like any Cauchy equation, the Euler equations originally formulated in convective form (also called usually "Lagrangian form", but this name is not self-explanatory and historically wrong, so it will be avoided) can also be put in the "conservation form" (also called usually "Eulerian form", but also this name is not self-explanatory and is historically wrong, so it will be avoided here). The conservation form emphasizes the mathematical interpretation of the equations as conservation equations through a control volume fixed in space, and is the most important for these equations also from a numerical point of view. The convective form emphasizes changes to the state in a frame of reference moving with the fluid.
- 1 History
- 2 Incompressible Euler equations with constant and uniform density
- 3 Incompressible Euler equations
- 4 Euler equations
- 5 Quasilinear form and characteristic equations
- 6 Bernoulli's theorems for steady inviscid flow
- 7 Discontinuities
- 8 Constraints
- 9 See also
- 10 Notes
- 11 Further reading
The Euler equations first appeared in published form in Euler's article "Principes généraux du mouvement des fluides", published in Mémoires de l'Academie des Sciences de Berlin in 1757 (in this article Euler actually published only the general form of the continuity equation and the momentum equation; the energy balance equation would be obtained a century later). They were among the first partial differential equations to be written down. At the time Euler published his work, the system of equations consisted of the momentum and continuity equations, and thus was underdetermined except in the case of an incompressible fluid. An additional equation, which was later to be called the adiabatic condition, was supplied by Pierre-Simon Laplace in 1816.
During the second half of the 19th century, it was found that the equation related to the balance of energy must at all times be kept, while the adiabatic condition is a consequence of the fundamental laws in the case of smooth solutions. With the discovery of the special theory of relativity, the concepts of energy density, momentum density, and stress were unified into the concept of the stress–energy tensor, and energy and momentum were likewise unified into a single concept, the energy–momentum vector.
Incompressible Euler equations with constant and uniform density
In convective form (i.e. the form with the convective operator made explicit in the momentum equation), the incompressible Euler equations in case of density constant in time and uniform in space are:
Incompressible Euler equations with constant and uniform density (convective or Lagrangian form)
- is the flow velocity vector, with components in a N-dimensional space ,
- denotes the material operator in time,
- denotes the scalar product,
- is the nabla operator, here used in the flow velocity divergence (first equation), and in flow velocity and specific pressure gradients (second equation), and
- is the convective operator,
- is the specific (with the sense of per unit mass) thermodynamic work, the internal source term.
- represents body accelerations (per unit mass) acting on the continuum, for example gravity, inertial accelerations, electric field acceleration, and so on.
In fact for a flow with uniform density the following identity holds:
where is the mechanic pressure. The second equation is the incompressible constraint, stating the flow velocity is a solenoidal field (the order of the equations is not casual, but underlines the fact that the incompressible constraint is not a degenerate form of the continuity equation, but rather of the energy equation, as it will become clear in the following). Notably, the continuity equation would be required also in this incompressible case as an additional third equation in case of density varying in time or varying in space. For example, with density uniform but varying in time, the continuity equation to be added to the above set would correspond to:
So the case of constant and uniform density is the only one not requiring the continuity equation as additional equation regardless of the presence or absence of the incompressible constraint. In fact, the case of incompressible Euler equations with constant and uniform density being analyzed is a toy model featuring only two simplified equations, so it is ideal for didactical purposes even if with limited physical relevancy.
The equations above thus represent respectively conservation of mass (1 scalar equation) and momentum (1 vector equation containing scalar components, where is the physical dimension of the space of interest). In 3D for example and the and vectors are explicitly and . Flow velocity and pressure are the so-called physical variables.
These equations may be expressed in subscript notation:
where the and subscripts label the N-dimensional space components. These equations may be more succinctly expressed using Einstein notation:
where the and subscripts label the N-dimensional space components, and ; is the Kroenecker delta. In 3D and the and vectors are explicitly and , and matched indices imply a sum over those indices and and .
Although Euler first presented these equations in 1755, many fundamental questions about them remain unanswered.
In three space dimensions it is not even known whether solutions of the equations are defined for all time or if they form singularities.
Smooth solutions of the free (in the sense of without source term: g=0) equations satisfy the conservation of specific kinetic energy:
In the one dimensional case without the source term (both pressure gradient and external force), the momentum equation becomes the inviscid Burgers equation:
This is a model equation giving many insights on Euler equations.
In order to make the equations dimensionless, a characteristic length , and a characteristic velocity , need to be defined. These should be chosen such that the dimensionless variables are all of order one. The following dimensionless variables are thus obtained:
and of the field unit vector:
Substitution of these inversed relations in Euler equations, defining the Froude number, yields (omitting the * at apix):
Incompressible Euler equations with constant and uniform density (nondimensional form)
Euler equations in the Froude limit (no external field) are named free equations and are conservative. The limit of high Froude numbers (low external field) is thus notable and can be studied with perturbation theory.
The conservation form emphasizes the mathematical properties of Euler equations, and especially the contracted form is often the most convenient one for computational fluid dynamics simulations. Computationally, there are some advantages in using the conserved variables. This gives rise to a large class of numerical methods called conservative methods.
The free Euler equations are conservative, in the sense they are equivalent to a conservation equation:
or simply in Einstein notation:
where the conservation quantity in this case is a vector, and is a flux matrix. This can be simply proved.
At last Euler equations can be recast into the particular equation:
Incompressible Euler equation(s) with constant and uniform density (conservation or Eulerian form)
For certain problems, especially when used to analyze compressible flow in a duct or in case the flow is cylindrically or spherically symmetric, the one-dimensional Euler equations are a useful first approximation. Generally, the Euler equations are solved by Riemann's method of characteristics. This involves finding curves in plane of independent variables (i.e., and ) along which partial differential equations (PDE's) degenerate into ordinary differential equations (ODE's). Numerical solutions of the Euler equations rely heavily on the method of characteristics.
Incompressible Euler equations
In convective form the incompressible Euler equations in case of density variable in space are:
Incompressible Euler equations (convective or Lagrangian form)
where the additional variables are:
The first equation, which is the new one, is the incompressible continuity equation. In fact the general continuity equation would be:
but here the last term is identically zero for the incompressibility constraint.
The incompressible Euler equations in the Froude limit are equivalent to a single conservation equation with conserved quantity and associated flux respectively:
Here has length N+2 and has size N(N+2). In general (not only in the Froude limit) Euler equations are expressible as:
The variables for the equations in conservation form are not yet optimised. In fact we could define:
- is the momentum density, a conservation variable.
Incompressible Euler equation(s) (conservation or Eulerian form)
- is the force density, a conservation variable.
In differential convective form, the compressible (and most general) Euler equations can be written shorty with the material derivative notation:
Euler equations (convective form)
where the additional variables here is:
- is the specific internal energy (internal energy per unit mass).
The equations above thus represent conservation of mass, momentum, and energy: the energy equation expressed in the variable internal energy allows to understand the link with the incompressible case, but it is not in the simplest form. Mass density, flow velocity and pressure are the so-called convective variables (or physical variables, or lagrangian variables), while mass density, momentum density and total energy density are the so-called conserved variables (also called eulerian, or mathematical variables). If one explicitates the material derivative the equations above are:
Coming back to the incompressible case, it now becomes apparent that the incompressible constraint typical of the former cases actually is a particular form valid for incompressible flows of the energy equation, and not of the mass equation. In particular, the incompressible constraint corresponds to the following very simple energy equation:
Thus for an incompressible inviscid fluid the specific internal energy is constant along the flow lines, also in a time-dependent flow. The pressure in an incompressible flow acts like a Lagrange multiplier, being the multiplier of the incompressible constraint in the energy equation, and consequently in incompressible flows it has no thermodynamic meaning. In fact, thermodynamics is typical of compressible flows and degenerates in incompressible flows.
Basing on the mass conservation equation, one can put this equation in the conservation form:
meaning that for an incompressible inviscid nonconductive flow a continuity equation holds for the internal energy.
Since by definition the specific enthalpy is:
The material derivative of the specific internal energy can be expressed as:
Then by substituting the momentum equation in this expression, one obtains:
And by substituting the latter in the energy equation, one obtains that the enthalpy expression for the Euler energy equation:
In a reference frame moving with an inviscid and nonconductive flow, the variation of enthalpy directly corresponds to a variation of pressure.
For a thermodynamic fluid, the compressible Euler equations are consequently best written as:
Euler equations (convective form, for a thermodynamic system)
- is the specific volume
- is the flow velocity vector
- is the specific entropy
Note that, 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:
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:
Note that the fundamental equation of state contains all the thermodynamic information about the system (Callen, 1985), exactly like the couple of a thermal equation of state together with a caloric equation of state.
The Euler equations in the Froude limit are equivalent to a single conservation equation with conserved quantity and associated flux respectively:
- is the momentum density, a conservation variable.
- is the total energy density (total energy per unit volume).
Here has length N+2 and has size N(N+2). In general (not only in the Froude limit) Euler equations are expressible as:
Euler equation(s) (original conservation or Eulerian form)
- is the force density, a conservation variable.
However, we already mentioned that for a thermodynamic fluid the equation for the total energy density is equivalent to the conservation equation:
Then the conservation equations in the case of a thermodynamic fluid are more simply expressed as:
Euler equation(s) (conservation form, for thermodynamic fluids)
- is the entropy density, a thermodynamic conservation variable.
Another possible form for the energy equation, being particularly useful for isobarics, is:
- is the total enthalpy density.
Quasilinear form and characteristic equations
Expanding the fluxes can be an important part of constructing numerical solvers, for example by exploiting (approximate) solutions to the Riemann problem. In regions where the state vector y varies smoothly, the equations in conservative form can be put in quasilinear form :
Obviously this jacobian does not exist in disconinuity regions (e.g. contact disconitnuities, shock waves in inviscid nonconductive flows). Note that if the flux Jacobians are not functions of the state vector , the equations reveals linear.
The compressible Euler equations can be decoupled into a set of N+2 wave equations that describes sound in Eulerian continuum if they are expressed in characteristic variables instead of conserved variables.
In fact the tensor A is always diagonalizable. If the eigenvalues (the case of Euler equations) are all real the system is defined hyperbolic, and physically eignevalues represent the speeds of propagation of information. If they are all distinguished, the system is defined strictly hyperbolic (it will be proved to be the case of one-dimensional Euler equations). Furthermore, note that diagonalisation of compressible Euler equation is easier when the energy equation is expressed in the variable entropy (i.e. with equations for thermodynamic fluids) than in other energy variables. This will become clear by considering the 1D case.
One can finally find the characteristic variables as:
Since A is constant, multiplying the original 1-D equation in flux-Jacobian form with P−1 yields the characteristic equations:
The original equations have been decoupled into N+2 characteristic equations each describing a simple wave, with the eigenvalues being the wave speeds. The variables wi are called the characteristic variablesand are a subset of the conservative variables. The solution of the initial value problem in terms of characteristic variables is finally very simple. In one spatial dimension it is:
Then the solution in terms of the original conservative variables is obtained by transforming back:
this computation can be explicited as the linear combination of the eigenvectors:
Now it becomes apparent that the characteristic variables act as weights in the linear combination of the jacobian eigenvectors. The solution can be seen as superposition of waves, each of which is advected independently without change in shape. Each i-th wave has shape wipi and speed of propagation λi. In the following we show a very simple example of this solution procedure.
Waves in 1D inviscid, nonconductive thermodynamic fluid
If one considers Euler equations for a thermodynamic fluid with the two further assumptions of one spatial dimension and free (no external field: g=0) :
If one defines the vector of variables:
recalling that is the specific volume, the flow speed, the specific entropy, the corresponding jacobian matrix is:
At first one must find the eigenvalues of this matrix by solving the characteristic equation:
that is explicitly:
This determinant is very simple: the fastest computation starts on the last row, since it has the highest number of zero elements.
Now by computing the determinant 2x2:
by defining the parameter:
or equivalently in mechanical variables, as:
This parameter is always real according to the second law of thermodynamics. In fact the second law of thermodynamics can be expressed by several postulates. The most elementary of them in mathematical terms is the statement of convexity of the fundamental equation of state, i.e. the hessian matrix of the specific energy expresseed as function of specific volume and specific entropy:
is defined positive. This statement corresponds to the two conditions:
The first condition is the one ensuring the parameter a is defined real.
The characteristic equation finally results:
That has three real solutions:
Then the matrix has three real eigenvalues all distinguished: the 1D Euler equations are a strictly hyperbolic system.
At this point one should determine the three eigenvectors: each one is obtained by substituting one eigenvalue in the eigenvalue equation and then solving it. By substituting the first eigenvalue λ1 one obtains:
Basing on the third equation that simply has solution s1=0, the system reduces to:
The two equations are redundant as usual, then the eigenvector is defined with a multiplying constant. We choose as right eigenvector:
The other two eigenvectors can be found with analogous procedure as:
Then the projection matrix can be built:
Finally it becomes apparent that the real parameter a previously defined is the speed of propagation of the information characteristic of the hyperbolic system made of Euler equations, i.e. it is the wave speed. It remains to be shown that the sound speed corresponds to the particular case of an isoentropic transformation:
Compressibility and sound speed
Sound speed is defined as the wavespeed of an isentropic transformation:
by the definition of the isoentropic compressibility:
the soundspeed results always the square root of ratio between the isoentropic compressibility and the density:
The sound speed in an ideal gas depends only on its temperature:
Since the specific enthalpy in an ideal gas is proportional to its temperature:
the sound speed in an ideal gas can also be made dependent only on its specific enthalpy:
Bernoulli's theorems for steady inviscid flow
Incompressible case and Lamb's form
where the Feynman subscript notation is used, which means the subscripted gradient operates only on the factor .
the Euler momentum equation in Lamb's form becomes:
Now, basing on the other identity:
the Euler momentum equation assumes a form that is optimal to demonstrate Bernoulli's theorem for steady flows:
In fact, in case of an external conservative field, by defining its potential φ:
In case of a steady flow the time derivative of the flow velocity disappears, so the momentum equation becomes:
In the steady incompressible case the mass equation is simply:
, that is the mass conservation for a steady incompressible flow states that the density along a streamline is constant. Then the Euler momentum equation in the steady incompressible case becomes:
The convenience of defining the total head for an inviscid liquid flow is now apparent:
, in fact the above equation can be simply written as:
That is, the momentum balance for a steady inviscid and incompressible flow in an external conservative field states that the total head along a streamline is constant.
In the most general steady (compressibile) case the mass equation in conservation form is:
and the steady energy equation in conservation form is:
Thanks to the mass conservation equation and to the definition of the momentum density, the first member becomes simply:
and for an external conservative field, the second member becomes:
Then by dividing for the density, the energy equation becomes:
Since the external field potential is usually small compared to the other terms, it is convenient to group the latters in the total enthalpy:
and the Bernoulli invariant for an inviscid gas flow is:
, in fact the above equation can be always written as:
That is, the energy balance for a steady inviscid flow in an external conservative field states that the sum of the total enthalpy and the external potential is constant along a streamline.
In the usual case of small potential field, simply:
Friedman form and Crocco form
By substituting the pressure gradient with the entropy and enthapy gradient, according to the first law of thermodynamics in the enthalpy form:
in the convective form of Euler momentum equation, one arrives to:
Friedmann deduced this equation for the particular case of a perfect gas and published it in 1922. However, this equation is general for an inviscid nonconductive fluid and no equation of state is implicit in it.
On the other hand, by substituting the enthalpy form of the first law of thermodynamics in the rotational form of Euler momentum equation, one obtains:
and by defining the specific total enthalpy:
In the steady case the two variables entropy and total enthalpy are particularly useful since Euler equations can be recast into the Crocco's form:
Finally if the flow is also isothermal:
by defining the specific total Gibbs free energy:
the Crocco's form can be reduced to:
From these relationships one deduces that the specific total free energy is uniform in a steady, irrotational, isothermal, isoentropic, inviscid flow.
The Euler equations are quasilinear[disambiguation needed] hyperbolic equations and their general solutions are waves. Under certain assumptions they can be simplified leading to Burgers equation. Much like the familiar oceanic waves, waves described by the Euler Equations 'break' and so-called shock waves are formed; this is a nonlinear effect and represents the solution becoming multi-valued. Physically this represents a breakdown of the assumptions that led to the formulation of the differential equations, and to extract further information from the equations we must go back to the more fundamental integral form. Then, weak solutions are formulated by working in 'jumps' (discontinuities) into the flow quantities – density, velocity, pressure, entropy – using the Rankine–Hugoniot equations. Physical quantities are rarely discontinuous; in real flows, these discontinuities are smoothed out by viscosity and by heat transfer. (See Navier–Stokes equations)
To properly compute the continuum quantities in discontinuous zones (for example shock waves or boundary layers) from the local forms (all the above forms are local forms, since the variables being described are typical of one point in the space caonsidered, i.e. they are local variables) of Euler equations through finite difference methods generally too many space points and time steps would be necessary for the memory of computers now and in the near future. In these cases it is mandatory to avoid the local forms of the conservation equations, passing some weak forms, like the finite volume one.
Starting from the simplest case, one consider a steady free conservation equation in conservation form in the space domain:
where in general F is the flux matrix. By integrating this local equation over a fixed volume Vm, it becomes:
then, basing on the divergence theorem, we can transform this integral in a boundary integral of the flux:
this global form simply states that there is no net flux of a conserved quantity passing through a region in the case steady and without source. In 1D the volume reduces to an interval, its boundary being its extrema, then the divergence theorem reduces to the fundamental theorem of calculus:
that is the simple finite difference equation, known as the jump relation:
That can be made explicit as:
where the notation employed is:
Or, if one performs an indefinite integral:
On the other hand, a transient conservation equation:
brings to a jump relation:
For one-dimensional Euler equations the conservation variables and the flux are the vectors:
- is the specific volume
- is the mass flux
In the steady one dimensional case the become simply:
thanks to the mass difference equation, the energy difference equation can be simplyfied without any restriction:
where is the specific total enthalpy.
these are the usually expressed in the convective variables:
- is the flow speed
- is the specific internal energy.
Note that the energy equation is an integral form of the Bernoulli equation in the compressible case. The former mass and momentum equations by substitution lead to the Rayleigh equation:
Since the second member is a constant, the Rayleigh equation always describes a simple line in the pressure volume plane not depending of any equation of state, i.e. the Rayleigh line. By substituition in the Rankine-Hugoniot equations, that can be also made explicit as:
one can also obtain the kinetic equation and to the Hugoniot equation. The analytical passages are not shown here for brevity.
These are respectively:
The Hugoniot equation, coupled with the fundamental equation of state of the material:
describes in general in the pressure volume plane a curve passing by the conditions (v0,p0), i.e. the Hugoniot curve, whose shape strongly depends on the type of material considered.
It is also customary to define a Hugoniot function:
allowing to quantify deviations from the Hugoniot equation, similarly to the previous definition of the hydraulic head, useful for the deviations from the Bernoulli equation.
Finite volume form
On the other hand, by integrating a generic conservation equation:
on a fixed volume Vm, and then basing on the divergence theorem, it becomes:
and by integrating this equation also over a time interval:
Now by defining the node conserved quantity:
we deduce the finite volume form:
In particular, for Euler equations, once the conserved quantities have been determined, the convective variables are deduced by back substitution:
Then the explicit finite volume expressions of the original convective variables are:
Euler equations (Finite volume form)
It has been shown that Euler equations are not a complete set of equations, but they require some additional constraints to admit a unique solution: these are the equation of state of the material considered. To be constistent with thermodynamics these equations of state should satisfy the two laws of thermodynamics. On the other hand, by definition non-equilibrium system are described by laws lying outside these laws. In the following we list some very simple equations of state and the corresponding influence on Euler equations.
Ideal polytropic gas
where is the specific energy, is the specific volume, is the specific entropy, is the molecular mass, here is considered a constant (polytropic process), and can be shown to correspond to the heat capacity ratio. This equation can be shown to be consistent with the usual equations of state employed by thermodynamics.
From this equation one can derive the equation for pressure by its thermodynamic definition:
By inverting it one arrives to the mechanical equation of state:
Then for an ideal gas the compressible Euler equations can be simply expressed in the mechanical or primitive variables specific volume, flow velocity and pressure, by taking the set of the equations for a thermodynamic system and modifying the energy equation into a pressure equation through this mechanical equation of state. At last, in convective form they result:
Euler equations for an ideal polytropic gas (convective form)
and in one-dimensional quasilinear form they results:
where the conservative vector variable is:
Steady flow in material coordinates 
Let be a Frenet–Serret orthonormal basis which consists of a tangential unit vector, a normal unit vector, and a binormal unit vector to the streamline, respectively. Since a streamline is a curve that is tangent to the velocity vector of the flow, the left-handed side of the above equation, the convective derivative of velocity, can be described as follows:
where is the radius of curvature of the streamline.
Therefore, the momentum part of the Euler equations for a steady flow is found to have a simple form:
The second equation expresses that, in the case the streamline is curved, there should exist a pressure gradient normal to the streamline because the centripetal acceleration of the fluid parcel is only generated by the normal pressure gradient.
The third equation expresses that pressure is constant along the binormal axis.
Streamline curvature theorem
Let be the distance from the center of curvature of the streamline, then the second equation is written as follows:
This equation states:
Although this relationship between the pressure field and flow curvature is very useful, it doesn't have a name in the English-language scientific literature. Japanese fluid-dynamicists call the relationship the "Streamline curvature theorem". 
This "theorem" explains clearly why there are such low pressures in the centre of vortices, which consist of concentric circles of streamlines. This also is a way to intuitively explain why airfoils generate lift forces.
- Bernoulli's theorem
- Kelvin's circulation theorem
- Cauchy equations
- Madelung equations
- Froude number
- Navier-Stokes equations
- Burgers equation
- see Toro, p. 24
- Anderson, John D. (1995), Computational Fluid Dynamics, The Basics With Applications. ISBN 0-07-113210-4
- E226 -- Principes generaux du mouvement des fluides
- Christodoulou, Demetrios (October 2007). "The Euler Equations of Compressible Fluid Flow" (PDF). Bulletin of the American Mathematical Society 44 (4): 581–602. doi:10.1090/S0273-0979-07-01181-0. Retrieved June 13, 2009.
- Hunter, J.K. An Introduction to the Incompressible Euler Equations
- Hunter, An introduction to incompressible Euler equations, p.2
- In 3D for example has length 5, has size 3x3 and has size 3x5, so the explicit forms are:
- (Italian) Quartapelle, Autieri, Fluidodinamica comprimibile, Chap. 9, p.13
- Landau, Lifshits, Fluid Mechanics, par. 1.1, eq. 2.6 and 2.7
- L.F. Henderson, par. 2.6 Thermodynamic properties of materials, in Handbook of Shock Waves, p. 152
- In 3D for example y has length 5, I has size 3x3 and F has size 3x5, so the explicit forms are:
- Chorin, Marsden, A mathematical introduction to fluid mechanics, par. 3.2 Shocks, p.118
- Toro, Rienmann solvers and numerical methods for fluid dynamics, par 2.1 Quasi-linear Equations: Basic concept, p.44
- Toro, op. cit., par 2.3 Linear Hyperbolic System, p.52
- (Italian)Valorani, Nasuti, Metodi di analisi delle turbomacchine, p.11-12
- Friedmann A. An essay on hydrodynamics of compressible fluid (Опыт гидромеханики сжимаемой жидкости), Petrograd, 1922, 516 p., reprinted in 1934 under the editorship of Nikolai Kochin (see the first formula on page 198 of the reprint).
- Handbook of Shock Waves, Vol I, par. 2.12 Crocco's theorem, p.177
- Sometimes the local and the global forms are also called respectively differential and non-differential, but this is not appropriate in all cases. For example, this is appropriate for Euler equations, while it is not for Navier-Stokes equations since in their global form there are some residual spatial first-order derivative operators in all the caractheristic transport terms that in the local form contains second-order spatial derivatives.
- Chorin, Marsden, A mathematical introduction to fluid mechanics, par. 3.2 Shocks, p. 122
- L.F. Henderson, par. 2.96 The Bethe-Weyl theorem, in Handbook of Shock Waves, p. 167
- (Italian) Quartapelle, Autieri, Fluidodinamica comprimibile, par. 11.10: Forma differenziale: metodo dei volumi finiti, p.161
- (Italian) Quartapelle, Autieri, Fluidodinamica comprimibile, Appendix E, p.A-61
- Toro, par 3.1.2 Nonconservative formulations, p.91
- M. Zingale, Notes on the Euler equations
- Toro, p.92
- James A. Fay (June 1994). Introduction to Fluid Mechanics. MIT Press. ISBN 0-262-06165-1. see "4.5 Euler's Equation in Streamline Coordinates" pp.150-pp.152 <http://books.google.com/books?id=XGVpue4954wC&pg=150>
- Babinsky, Holger (November 2003), "How do wings work?" (PDF), Physics Education
- 今井 功 (IMAI, Isao) (November 1973). 『流体力学(前編)』(Fluid Dynamics 1) (in Japanese). 裳華房 (Shoukabou). ISBN 4-7853-2314-0.
- Batchelor, G. K. (1967). An Introduction to Fluid Dynamics. Cambridge University Press. ISBN 0-521-66396-2.
- Thompson, Philip A. (1972). Compressible Fluid Flow. New York: McGraw-Hill. ISBN 0-07-064405-5.
- Toro, E.F. (1999). Riemann Solvers and Numerical Methods for Fluid Dynamics. Springer-Verlag. ISBN 3-540-65966-8.