summaryrefslogtreecommitdiff
path: root/source/know/concept/euler-equations/index.md
blob: 3730ea3053c77455b2adfc7a7bf2352a61d932ca (plain)
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
70
71
72
73
74
75
76
77
78
79
80
81
82
83
84
85
86
87
88
89
90
91
92
93
94
95
96
97
98
99
100
101
102
103
104
105
106
107
108
109
110
111
112
113
114
115
116
117
118
119
120
121
122
123
124
125
126
127
128
129
130
131
132
133
134
135
136
137
138
139
140
141
142
143
144
145
146
147
148
149
150
151
152
153
154
155
156
157
158
159
160
161
162
163
164
165
166
167
168
169
170
171
172
173
174
175
176
177
178
179
180
181
182
183
---
title: "Euler equations"
sort_title: "Euler equations"
date: 2021-03-31
categories:
- Physics
- Fluid mechanics
- Fluid dynamics
layout: "concept"
---

The **Euler equations** are a system of partial differential equations
that govern the movement of **ideal fluids**,
i.e. fluids without viscosity.
There exist several forms, depending on
the surrounding assumptions about the fluid.


## Incompressible fluid

In a fluid moving according to the velocity vield $$\va{v}(\va{r}, t)$$,
the acceleration felt by a particle is given by
the **material acceleration field** $$\va{w}(\va{r}, t)$$,
which is the [material derivative](/know/concept/material-derivative/) of $$\va{v}$$:

$$\begin{aligned}
    \va{w}
    \equiv \frac{\mathrm{D} \va{v}}{\mathrm{D} t}
    = \pdv{\va{v}}{t} + (\va{v} \cdot \nabla) \va{v}
\end{aligned}$$

This infinitesimal particle obeys Newton's second law,
which can be written as follows:

$$\begin{aligned}
    \va{w} \dd{m}
    = \va{w} \rho \dd{V}
    = \va{f^*} \dd{V}
\end{aligned}$$

Where $$\dd{m}$$ and $$\dd{V}$$ are the particle's mass volume,
and $$\rho$$ is the fluid density, which we assume, in this case, to be constant in space and time.
Then the **effective force density** $$\va{f^*}$$ represents the net force-per-particle.
By dividing the law by $$\dd{V}$$, we find:

$$\begin{aligned}
    \rho \va{w}
    = \va{f^*}
\end{aligned}$$

Next, we want to find another expression for $$\va{f^*}$$.
We know that the overall force $$\va{F}$$ on an arbitrary volume $$V$$ of the fluid
is the sum of the gravity body force $$\va{F}_g$$,
and the pressure contact force $$\va{F}_p$$ on the enclosing surface $$S$$.
Using the divergence theorem, we then find:

$$\begin{aligned}
    \va{F}
    = \va{F}_g + \va{F}_p
    = \int_V \rho \va{g} \dd{V} - \oint_S p \dd{\va{S}}
    = \int_V (\rho \va{g} - \nabla p) \dd{V}
    = \int_V \va{f^*} \dd{V}
\end{aligned}$$

Where $$p(\va{r}, t)$$ is the pressure field,
and $$\va{g}(\va{r}, t)$$ is the gravitational acceleration field.
Combining this with Newton's law, we find the following equation for the force density:

$$\begin{aligned}
    \va{f^*}
    = \rho \va{w}
    = \rho \va{g} - \nabla p
\end{aligned}$$

Dividing this by $$\rho$$,
we get the first of the system of Euler equations:

$$\begin{aligned}
    \boxed{
        \va{w}
        = \frac{\mathrm{D} \va{v}}{\mathrm{D} t}
        = \va{g} - \frac{\nabla p}{\rho}
    }
\end{aligned}$$

The last ingredient is **incompressibility**:
the same volume must simultaneously
be flowing in and out of an arbitrary enclosure $$S$$.
Then, by the divergence theorem:

$$\begin{aligned}
    0
    = \oint_S \va{v} \cdot \dd{\va{S}}
    = \int_V \nabla \cdot \va{v} \dd{V}
\end{aligned}$$

Since $$S$$ and $$V$$ are arbitrary,
the integrand must vanish by itself everywhere:

$$\begin{aligned}
    \boxed{
        \nabla \cdot \va{v} = 0
    }
\end{aligned}$$

Combining this with the equation for $$\va{w}$$,
we get a system of two coupled differential equations:
these are the Euler equations for an incompressible fluid
with spatially uniform density $$\rho$$:

$$\begin{aligned}
    \boxed{
        \frac{\mathrm{D} \va{v}}{\mathrm{D} t}
        = \va{g} - \frac{\nabla p}{\rho}
        \qquad \quad
        \nabla \cdot \va{v}
        = 0
    }
\end{aligned}$$

The above form is straightforward to generalize to incompressible fluids
with non-uniform spatial densities $$\rho(\va{r}, t)$$.
In other words, these fluids are "lumpy" (variable density),
but the size of their lumps does not change (incompressibility).

To update the equations, we demand conservation of mass:
the mass evolution of a volume $$V$$
is equal to the mass flow through its boundary $$S$$.
Applying the divergence theorem again:

$$\begin{aligned}
    0
    = \dv{}{t}\int_V \rho \dd{V} + \oint_S \rho \va{v} \cdot \dd{\va{S}}
    = \int_V \dv{\rho}{t} + \nabla \cdot (\rho \va{v}) \dd{V}
\end{aligned}$$

Since $$V$$ is arbitrary, the integrand must be zero.
This leads to the following **continuity equation**,
to which we apply a vector identity:

$$\begin{aligned}
    0
    = \dv{\rho}{t} + \nabla \cdot (\rho \va{v})
    = \dv{\rho}{t} + (\va{v} \cdot \nabla) \rho + \rho (\nabla \cdot \va{v})
\end{aligned}$$

Thanks to incompressibility, the last term disappears,
leaving us with a material derivative:

$$\begin{aligned}
    \boxed{
        0
        = \frac{\mathrm{D} \rho}{\mathrm{D} t}
        = \dv{\rho}{t} + (\va{v} \cdot \nabla) \rho
    }
\end{aligned}$$

Putting everything together, Euler's system of equations
now takes the following form:

$$\begin{aligned}
    \boxed{
        \frac{\mathrm{D} \va{v}}{\mathrm{D} t}
        = \va{g} - \frac{\nabla p}{\rho}
        \qquad
        \nabla \cdot \va{v}
        = 0
        \qquad
        \frac{\mathrm{D} \rho}{\mathrm{D} t}
        = 0
    }
\end{aligned}$$

Usually, however, when discussing incompressible fluids,
$$\rho$$ is assumed to be spatially uniform,
in which case the latter equation is trivially satisfied.



## References
1.  B. Lautrup,
    *Physics of continuous matter: exotic and everyday phenomena in the macroscopic world*, 2nd edition,
    CRC Press.