Continuum Mechanics

Table of Contents

1. Mechanical Properties

1.1. Stress

1.1.1. Cauchy Stress Tensor

The force per area on a surface is called the traction \( \mathbf{t} \). The Cauchy stress tensor \( \boldsymbol{\sigma} \) is defined to satisfy \[ \mathbf{t} = \boldsymbol{\sigma}\hat{\mathbf{n}} \] where \( \hat{\textbf{n}} \) is the unit normal vector of the surface.

The stress is being applied to a control volume which is a infinitesimal inertial volume. In particular, for a cube of side length \( \ell \), the torque is \( \ell^3(\sigma_{ij} - \sigma_{ji}) \) and the moment of inertia is proportional to \( \ell^5 \). That means the angular acceleration is infinite, if \( \sigma_{ij} \neq \sigma_{ji} \). Similarly the force is proportional to \( \ell^2 \) while the mass is proportional to \( \ell^3 \). This also suggest that the acceleration would be infinite. Therefore, the control volume is at a quasi-equalibrium, that is, the changes in tensile and shear stresses across the volume are infinitesimal and the forces and torques should sum to zero. This justifies the Cauchy stress tensor being symmetric.

In a coordinate system, \( \sigma_{ij} \) is the force in \( i \)th direction, when the surface is facing \( j \)th direction.

1.1.2. Volumetric Stress Tensor

  • Mean Normal Stress Tensor

The isotropic stress can change the volumn of the stressed body. \[ \pi \mathbf{I} := \frac{1}{3}\operatorname{tr} (\boldsymbol{\sigma}) \mathbf{I}. \] The three accounts for the three direction that the stress is applied.

1.1.3. Pressure

In its full generality, \[ p := \zeta \nabla\cdot \mathbf{u} - \pi \] where \( \zeta \) is teh volume viscosity, \( \mathbf{u} \) is the flow velocity.

The isotropic stress from volume strain is already included in the total isotropic stress: \[ \pi = -p + \zeta \nabla\cdot \mathbf{u}. \]

1.1.4. Deviatoric Stress Tensor

  • \( \boldsymbol{\tau} \), \( s_{ij} \)
  • Shear Stress Tensor, Stress Deviator Tensor

Deviation of the Cauchy stress tensor from the isotropy. \[ \boldsymbol{\tau} := \boldsymbol{\sigma} - \pi \mathbf{I}. \]

1.1.5. Mohr's Circle

Given three principal stresses \(\sigma_1, \sigma_2, \sigma_3\), the shear stress and normal stress inbetween the \(i\)th and \(j\)th principal axis are:

\begin{align*} \sigma_{\rm normal} &= \vu{n}\vdot (\vb*{\sigma} \vu{n}) \\ &= \vu{n} \vdot (\sigma_i \cos \theta \vb{e}_i + \sigma_j \sin\theta \vb{e}_j)\\ &= \sigma_i\cos^2\theta + \sigma_j\sin^2\theta \\ &= \frac{\sigma_i + \sigma_j}{2} + \frac{\sigma_i - \sigma_j}{2} \cos 2\theta \end{align*} \begin{align*} \tau &= \vu{T} \vdot (\vb*{\sigma}\vu{n}) \\ &= (-\sin\theta \vb{e}_i + \cos\theta \vb{e}_j) \vdot (\sigma_i \cos \theta \vb{e}_i + \sigma_j \sin\theta \vb{e}_j)\\ &= -\sigma_i\sin\theta\cos\theta + \sigma_j\cos\theta \sin\theta \\ &= - \frac{\sigma_i - \sigma_j}{2}\sin 2\theta \end{align*}

They together forms a circle centered at the average and radius \(|\sigma_i - \sigma_j|/2\).

The three circles are drawn on top of one another in normal stress-shear stress plane, which give us the Mohr's circle.

For principal stresses \(\sigma_3 < \sigma_2 < \sigma_1\), the shaded crescent is the set of admissible (normal, shear) stress states on any plane through the point; the two small circles are tangent at \(\sigma_2\).

Mohr-circle-export.svg

1.2. Strain

1.2.1. Strain Tensor

  • Rate of Deformation Tensor (when \(\mathbf{u}\) is strain-rate), Infinitesimal Strain

Given a displacement field (or strain-rate) \( \mathbf{u} \), \( \nabla \vb{u} \) can be divided into four parts:

  • Volumetric part: Uniformly stretched in all direction.
  • Axial Deviatoric: Streched along each axis, with no overall volume change.
  • Symmetric Shear: Non-rotational shear.
  • Antisymmetric Shear: rotation.

The second and third collectively make up the deviatoric part.

In a non-compressible material: \[ \boldsymbol{\varepsilon} := \frac{1}{2}(\nabla \mathbf{u} + (\nabla \mathbf{u})^{\rm T}), \qquad \varepsilon_{ij} = \frac{1}{2}(\partial_iu_j + \partial_ju_i). \] This is the symmetric part of the gradient that contains the first three parts: volumetric and deviatoric part.

\( \mathbf{u} \) can be the flow velocity, in which case this is strain-rate tensor. The strain rate tensor generate stress the same way the strain would.

1.2.2. Volumetric and Deviatoric Strain

\[ \varepsilon_v := \varepsilon_{xx} + \varepsilon_{yy} + \varepsilon_{zz}. \] It tells the (infinitesimal) total volume change.

The volumetric part of strain tensor is given by: \[ \vb{\varepsilon}_{\rm vol} = \frac{1}{3} (\nabla \cdot \mathbf{u}) \mathbf{I}. \]

The volumetric strain and deviatoric strain can be separated:

\begin{align*} \varepsilon &= \varepsilon_{\rm vol} + \varepsilon_{\rm dev} \\ &= \frac{1}{3}(\div{\vb{u}}) \vb{I} + \left( \frac{1}{2}(\grad{\vb{u}} + (\grad{\vb{u}})^{\mathsf{T}}) - \frac{1}{3}(\div{\vb{u}}) \vb{I} \right) \end{align*}

There exists separate viscosities for volumetric part and deviatoric part: bulk viscosity \(\zeta\) and shear viscosity \(2\mu\).

1.3. Modulus

From Latin modus 'measure'

Moduli are only defined in the elastic region of the stress-strain curve.

1.3.1. Young's Modulus

\[ E := \frac{\sigma}{\varepsilon} \] where \(\sigma\) is the tensile stress, and \(\varepsilon\) is the extensional strain.

It is directly related to the stiffness (or spring constant, rigidity) \(k\): \[ k = \frac{EA}{L}. \] where \(A\) is the cross-sectional area, and \(L\) is the length of the element.

1.3.2. Bulk Modulus

The ratio of pressure to the volumetric strain: \[ K := -V\dv{p}{V} \] where \( p \) is pressure, and \( V \) is the initial volume of system.

1.3.3. Shear Modulus

  • Modulus of Rigidity

The ratio of shear stress to the shear strain: \[ G := \frac{\tau}{\gamma}. \] The shear stress \( \tau \) shears the material by the angle of \( \gamma \) which is the shear strain.

1.3.3.1. In Shaft

For torsion of a shaft, \[ G = \frac{TL}{\theta J} \] where \( T \) is torque, \( L \) is the length along the axis, \( \theta \) is the angle of torsion, and \( J \) is the polar moment of inertia (or torsion constant). Polar moment of inertia is the second moment of area that is perpendicular to the axis.

The shear strain at radius \( \rho \) from the axis is given by: \[ \gamma = \frac{\rho \theta}{L}, \] and the torque on a cross section can be obtained by integrating the shear stress: \[ T = \int_0^r \tau \rho \dd{A} = \int_0^r G\gamma \rho \dd{A} = \frac{G\theta}{L} \int_0^r \rho^2\dd{A}. \] The claimed equation is found.

1.3.4. Elasticity Tensor

  • \( \mathbf{C}, \mathbf{Y} \)
  • Elastic Modulus Tensor, Stiffness Tensor

Rank-4 tensor \( C^{ijkl} \) that relates the linear stress-strain relation: \[ \sigma^{ij} = C^{ijkl}\varepsilon_{jk}. \]

1.3.4.1. Voigt Notation

The rank is reduced by indexing pairs of indices.

Elasticity and compliance tensor gets reduced to 6 by 6 matrices, with each index from 1 to 6 representing 11, 22, 33, 23, 13, 12 in the original matrix.

1.3.5. Compliance Tensor

  • \( \mathbf{S}, \mathbf{K} \)

The "inverse" of elasticity tensor satisfying: \[ S_{ijpq}C^{pqkl} = \frac{1}{2} \left( \delta_i^k\delta_j^l + \delta_i^l\delta_j^k \right). \]

It describe the inverse stress-strain relation: \[ \varepsilon_{ij} = S_{ijkl}\sigma^{jk}. \]

1.3.6. Poisson's Ratio

Assume that there is stress only along a single axis. The Poisson's ratio here is the ratio of transverse strain to the axial strain, with negative sign: \[ \nu := -\frac{\varepsilon_{\rm trans}}{\varepsilon_{\rm axial}}. \]

The strain in one direction can be created by stress in multiple axes: \[ \varepsilon_{ii} = \frac{1}{E} \sigma_{ii} - \sum_{j\neq i}\frac{\nu}{E} \sigma_{jj} \] where \( E \) is the Young's modulus. The material is stretched by the axial stress, but squished by transverse stress because it is being stretched in other direction.

Using Voigt notation, we can write the stress-strain relation in two ways:

\begin{align} \begin{bmatrix} \varepsilon_{xx} \\ \varepsilon_{yy} \\ \varepsilon_{zz} \end{bmatrix} &= \frac{1}{E} \begin{bmatrix} 1 & -\nu & -\nu \\ -\nu & 1 & -\nu \\ -\nu & -\nu & 1 \end{bmatrix} \begin{bmatrix} \sigma_{xx} \\ \sigma_{yy} \\ \sigma_{zz} \end{bmatrix}, \\ \begin{bmatrix} \sigma_{xx} \\ \sigma_{yy} \\ \sigma_{zz} \end{bmatrix} &= \begin{bmatrix} K + \frac{4}{3}G & K - \frac{2}{3}G & K - \frac{2}{3}G \\ K - \frac{2}{3}G & K + \frac{4}{3}G & K - \frac{2}{3}G \\ K - \frac{2}{3}G & K - \frac{2}{3}G & K + \frac{4}{3}G \end{bmatrix} \begin{bmatrix} \varepsilon_{xx} \\ \varepsilon_{yy} \\ \varepsilon_{zz} \end{bmatrix}. \end{align}

Notice that we are assuming linear isotropic material here.

These matrices are inverses of each other. In order to relate \( \nu, E \) to \( K, G \), let us the inverse of the second matrix. The determinant can be factorized with the formula \( a^3 -3ab^2 + 2b^3 = (a-b)(a^2 + ab - 2b^2) \) in mind, (The determinant is \( 2G ( 6 KG ) \).) and we obtain: \[ \frac{1}{E} = \frac{2K + \frac{2}{3}G}{6KG},\qquad \frac{\nu}{E} = \frac{K - \frac{2}{3}G}{6KG}. \]

Now any one of them can be expressed in terms of other two:

\begin{align*} \nu &= \frac{K - \frac{2}{3}G}{2K + \frac{2}{3}G} = \frac{E}{2G} - 1 = \frac{1}{2}\left( 1- \frac{E}{3K} \right),\\ E &= \frac{6KG}{2K + \frac{2}{3}G} = 2G(1+\nu) = 3K(1-2\nu), \\ G &= \frac{E}{2(1+\nu)}, \\ K &= \frac{E}{3(1-2\nu)}. \end{align*}

The volumetric strain is also related to the Poisson's ratio: \[ \varepsilon_v := \sum_i\varepsilon_{ii} = \frac{1-2\nu}{E}(\sigma_{xx} + \sigma_{yy} + \sigma_{zz}). \] Notice that it is zero when \( \nu = 0.5 \), which indicate that there is no volume change when stretched. Rubber is a good example that has similar Poisson's ratio. On the other hand cork has Poisson's ratio close to zero; they almost don't expand laterally.

1.4. Stiffness

  • Rigidity
  • 강성

\[ k := \frac{F}{\delta} \] where \(F\) is the force on the body, and \(\delta\) is the displacement along the same degree of freedom.

The inverse is called flexibility, or pliabilit.

  • Rotational stiffness: moment / rotation angle
  • Shear stiffness: shear force / shear deformation
  • Torsional stiffness: torsion moment / angle of twist

1.5. Hardness

Resistance to local plastic deformation, such as indentation, scratching, or abrasion.

Hardness can be increased by .

1.6. Strength

  • 강도

Material is susceptible to various failure modes. Strength is the ability to withstand an applied load without failure or plastic deformation.

1.6.1. Yield Strength

  • 항복강도

Lowest stress that that produce a permanent deformation. Usually defined as the stress required to cause 0.2% plastic strain (0.2% proff stain).

1.6.2. Compressive Strength

Limit state of compressive stress that leads to ductile failure or brittle failure (rupture by crack propagation, sliding along a weak plane).

1.6.3. Tensile Strength

  • Ultimate tensile strenght, ultimate strength, true stress, engineering stress.

Limit state of tensile stress that leads to ductile failure or brittle failure.

1.6.4. Fatigue Stength

Failure within service period. In the case of cyclic loading, it is expressed as amplitude and number of cycles to failure.

1.6.5. Impact Strength

Capability to withstand a sudden load, expressed in terms of energy.

  • Izod impact strenght test
  • Charpy impact test

1.7. Failure

1.7.1. Factor of Safety

It is a design criteria. \[ \mathrm{FS} = \frac{\mathrm{UAS}}{F} \] where \(\mathrm{UAS}\) is the ultimate alloable stress, \(F\) is applied stress.

1.7.2. Macroscopic Failure

1.7.2.1. Stress or Strain Failure
  • Hydrostatic (isotropic) stress do not cause yielding in ductile material
1.7.2.1.1. Maximum Principal Stress Theory
  • Rankine Theory, Maximum normal stress theory

Yield occurs when the largest principal stress exceeds the uniaxial tensile yield strength.

\[ \sigma_1 = \sigma_y \] Limit on the x axis of Mohr's circle.

Applied to ductile material but not good. Applies to brittle material.

1.7.2.1.2. Maximum Shear Stress Theory
  • Tresca Theory

Failure occur if the maximum shear stress exceeds the shear strength of the material in uniaxial testing.

\[ \frac{\sigma_1 - \sigma_3}{2} = \tau_y\] Limit on the y axis of Mohr's circle Hexagonal prism of stress yield surface.

More conservative than von Mises.

Applies to ductile material.

1.7.2.1.3. Mohr-Coulomb Theory
  • Coulomb-Mohr theory

In brittle material the tensile failure and compressive failure happens at different magnitude of stress. The yield surface touches the two circles to the each failure point from the origin in Mohr's circle.

It forms a hexagonal cone in stres yield surface.

1.7.2.2. Energy Type Failure
1.7.2.2.1. Maximum Strain Energy Theory

Failure occur when the strain energy per unit volume equals the strain energy per unit volume at the yield point in uniaxial testing.

Applies to ductile material.

1.7.2.2.2. Maximum Distortion Energy Theory
  • Von Mises Theory
  • Maximum distortion energy theory of failure, von Mises-Hencky theory, Maxwell-Hubert-Hencky-von Mises theory

\[ \sqrt{\frac{1}{2} \left[ (\sigma_1 - \sigma_2)^2 + (\sigma_2 - \sigma_3)^2 + (\sigma_3 - \sigma_1)^2 \right]} = \sigma_y \]

The left hand side is called the equivalent von Mises stress \(\sigma_{\rm eq}\).

Cylinder of stress yield surface.

Applies to ductile material.

1.7.3. Microscopic Failure

  • Fracture Mechanics
1.7.3.1. Griffiths' Theory

Critical stress of mode I opening of a crack propagation is given by: \[ \sigma = \sqrt{\frac{2E\gamma}{\pi a}} \] where \(E\) is Young's modulus, \(\gamma\) is the surface energy per unit area of the crack, and \(a\) is the crack length for edge cracks or \(2a\) is the crack length for plane cracks.

Fracture toughness \(K\) is postulated to be a material parameter. Mode I fracture toughness for plane strain is defined as \[ K_{\rm Ic} = Y \sigma_c \sqrt{\pi a} \] where \(\sigma_c\) is a critical value of the far field stress, \( Y \) is a dimensionless factor that depends on the geometry, material properties, and loading condition.

1.8. Toughness

  • 인성
  • Both strong and ductile

Toughness is defined to be the area under the stress-strain curve. \[ U_T = \int_0^{\varepsilon_f} \sigma \dd{\varepsilon} \] where \(\varepsilon_f\) is the strain upon failure.

It is the energy of mechanical deformation per unit volume prior to fracture.

If yield point can be defined, the absorbed energy per unit volume until the yield point is known as the modulus of resilience. \[ U_r := \frac{1}{2} \sigma_{\rm yield} \varepsilon_{\rm yield} = \frac{1}{2} \frac{\sigma_{\rm yield}^2}{E} = \frac{1}{2} E \varepsilon_{\rm yield}^2. \]

1.9. Viscosity

1.9.1. Newton's Law of Viscosity

The linear relation between deviatoric stress and deviatoric strain: \[ \boldsymbol{\tau} = \mu \left[\nabla \mathbf{u} + (\nabla \mathbf{u})^{\mathsf{T}} - \frac{2}{3}(\nabla\cdot \vb{u})\vb{I}\right] \] where \(\boldsymbol{\tau}\) is the deviatoric stress, \( \mu \) is the dynamic viscosity, and \(\mathbf{u}\) is the flow velocity.

Coordinate representation would be \[ \tau_{ij} = \mu \left(\frac{\partial u_i}{\partial x_j} + \frac{\partial u_j}{\partial x_i} \right). \]

The fluid that satisfies the Newton's law of viscosity is called the Newtonian fluid.

1.9.2. Dynamic Viscosity

  • \(\mu\), \( \eta \)
  • Shear Viscosity

The relational constant between stress and momentum change. It has the unit of \(\rm Pa\cdot s\) in SI, poise in cgs.

1.9.3. Kinematic Viscosity

  • Momentum Diffusivity

\[ \nu = \frac{\mu}{\rho}. \]

1.9.4. Bulk Viscosity

  • Volume Viscosity
  • \(\zeta\)

The ratio of isotropic axial stress to the volumetric strain: \[ \vb{\sigma} = \zeta \vb{\varepsilon}_{\rm vol} + 2\mu \vb{\varepsilon}_{\rm dev} \]

\[ \zeta = \lambda + \frac{2}{3}\mu \] where \( \lambda \) is the second viscosity, and \( \mu \) is the dynamic viscosity.

1.9.5. Second Viscosity

  • Second Coefficient of Viscosity
  • \( \lambda \)

The ratio of additional axial stress due to the volumetric strain, compared to the naive approach \(2\mu\varepsilon\): \[ \vb{\sigma} = 2\mu \vb{\varepsilon} + \lambda \vb{\varepsilon}_{\rm vol}. \]

The stress occurs due to irreversible resistance, over the reversible resistance by isentropic bulk modulus.

1.9.6. Effective Viscosity

For an object moving in a fluid with viscosity \( \mu \), if the size of the object is smaller than the mean free path of the fluid particles, the effective viscosity \( \mu_{\mathrm{eff}} \) deviates from the macroscopic viscosity \( \mu \). \[ \eta_{\mathrm{eff}} = \eta \frac{1}{1+\frac{b}{pr}} \] where \( p \) is the pressure, \( b = 8.22\times 10^{-3}\ \mathrm{Pa\cdot m}\) is a constant, and \( r \) is the radius of the particle.

This quantity is used when establishing the mechanical equalibrium using the Stokes' law: \[ 6\pi r \eta_{\mathrm{eff}} v = F. \] From the equalibrium, the radius \( r \) can be obtained. \[ r = \sqrt{\frac{9\eta_{\mathrm{eff}} v_t}{2g\rho}}. \] where \( v_t \) is the terminal velocity of free falling particle, \( g \) is the gravitational constant, \( \rho \) is the density of the fluid.

1.9.7. Anisotropic Fluid

The viscosity for anisotropic fluid is given by a tensor \( \mu_{ij} \).

2. Constitutive Equation

  • 구성 방정식

2.1. Linear Isotropic Stress-Strain

\[ \vb*{\sigma} = 3K \left(\frac{1}{3}\tr(\vb*{\varepsilon}) \mathbf{I}\right) + 2G \left( \vb*{\varepsilon} - \frac{1}{3}\tr(\vb*{\varepsilon}) \mathbf{I} \right), \] where \( K \) is the bulk modulus, \( G \) is the shear modulus.

This provide a realistic description, since real material change their shape more easily than their volume.

The is three times the isotropic strain in each axis. The isotropic part of the constitutive equation looks like: \[ p = \frac{\sigma_{xx} + \sigma_{yy} +\sigma_{zz} }{3} = 3K \frac{\varepsilon_{xx} + \varepsilon_{yy} + \varepsilon_{zz}}{3} = K\varepsilon_v. \]

The shear strain is double the deviatoric strain by definition. A shear strain in one direction consists of rotation and deviatoric strain, each taking half of it.

2.2. Linear Stress-Rate of Strain

We assume:

  • The Cauchy stress tensor is Galilean invariant
  • \( p \) is independent of the strain \( \boldsymbol{\varepsilon} \)
  • The fluid is isotropic.

The relation (constitutive equation) between the strain and stress is given as: \[ \boldsymbol{\sigma} = -p\mathbf{I} + \frac{1}{3}\lambda \operatorname{tr}(\boldsymbol{\varepsilon}) \mathbf{I} + 2\mu \boldsymbol{\varepsilon} \] where \( \lambda \) is the second viscosity.

The equation can also be written as: \[ \boldsymbol{\sigma} = -(p - \zeta \nabla\cdot \mathbf{u})\mathbf{I} + \mu \left( \nabla \mathbf{u} + (\nabla \mathbf{u})^{\mathsf{T}} - \frac{2}{3}(\nabla \cdot \mathbf{u})\mathbf{I} \right) \] using the bulk viscosity.

3. Fick's Laws of Diffusion

3.1. First Law

\[ \mathbf{J} = -D\nabla \varphi \] where \(\mathbf{J}\) is the diffusion flux, amount of substance per area per time, and \(D\) is the diffusion coefficient of diffusivity, and \(\nabla\varphi\) is the concentration gradient.

  • \(D\) has the unit of area per time.
  • \(\varphi\) has the unit of concentration, the amount of substance per volume.

3.2. Second Law

  • \[ \frac{\partial \varphi}{\partial t} = D\nabla^{\cdot 2}\varphi. \]
  • This is the same form as the heat equation.

4. Thermal Properties

4.1. Fourier's Law

  • The Law of Heat Conduction

\[ \mathbf{q} = -k\nabla T \] where \(\mathbf{q}\) is the heat flux density, \(k\) is the thermal conductivity.

4.2. Thermal Conductivity

  • \(k\), \(\lambda\), \(\kappa\)

[W/m/K]

Heat flux per temperature gradient.

4.3. Heat Equation

\[ \frac{\partial u}{\partial t} = \alpha \nabla^{\cdot 2} u \] where \(\alpha\) is the thermal diffusivity.

4.4. Thermal Diffusivity

\[ \alpha = \frac{k}{\rho c} \] where \(k\) is the thermal conductivity, \(\rho\) is the density of the material, \(c\) is the specific heat capacity of the material.

4.5. Thermal Effusivity

\[ e := \frac{k}{\sqrt{\alpha}} = \sqrt{k\rho c} \]

Product of material's intensive heat transport and storage properties. In contrast to the thermal diffusivity, which is the ratio of trasport and storage properties.

It measures the ability to absorb heat from surrounding through diffusion, for example metal has high effusivity compared to plastic. This property is directly sensed by human thermoreceptors.

The interface temparature between two reservoir is given by the weighted average: \[ T_m = \frac{e_1T_1 + e_2 T_2}{e_1 + e_2} \]

4.6. Thermal Contact Conductance

  • \(h_c\)

Heat flux per temperature difference.

Temperature drops abruptly at contact surface. This quantity represent the conductance of that contact.

The conductance of series of conductor adds like parallel resistance.

4.7. Heat Kernel

4.7.1. Example

\[ K(t, x, y) = \exp(t \nabla^{\cdot 2})(x, y) = \frac{1}{(4\pi t)^{d/2}}e^{-\|x-y\|^2/4t}. \] For every smooth function \(\phi\) of compact support: \[ \lim_{t\to 0}\int_{\mathbb{R}^d}K(t, x, y)\phi(y)\,dy = \phi(x). \]

4.8. Thermal emittance

  • Thermal emissivity
  • \(\varepsilon\)

Ratio of radiant emittance of heat to that of a standard black body.

Emissivity and emittivity, where emissivity refers to a material property, while emittivity refers to specific objects.

Ratio of radiant exitance to the radiant exitance of equivalent black body. \[ \varepsilon = \frac{M_{\rm e}}{M_{\rm e}^{\circ}}. \] where \(M_{\rm e}\) is the radiant exitance of the object which is measured in radiant power per unit surface area.

5. Coordinate Specification

5.1. Lagrange Specification

  • Material Coordinates

Lagrangian specification of the flow field represents individual fluid parcels. \[ \mathbf{X}(\mathbf{x}_0, t) \]

5.2. Eulerian Specification

  • Specification at fixed location.
  • \[ \mathbf{u}(\mathbf{x}, t) \]

6. Knudsen Number

\[ \mathrm{Kn} := \frac{\lambda}{L} \] where \( \lambda \) is the mean free path of particles, and \( L \) is the representative physical length scale of a system.

If Knudsen number is near or greater than one, statistical methods should be used instead of treating the system as a continuum.

6.1. Properties

It is related to Mach number and Reynolds number by \[ \mathrm{Kn} = \frac{\mathrm{Ma}}{\mathrm{Re}} \sqrt{\frac{\gamma \pi}{2}}. \]

7. Material Derivative

Advective Derivative, Convective Derivative, Derivative Following the Motion, Hydrodynamic Derivative, Lagrangian Derivative, Particle Derivative, Substantial Derivative, Substantive Derivative, Stokes Derivative, Total Derivative

7.1. Definition

\[ \frac{D}{Dt} := \frac{\partial }{\partial t} + \mathbf{u}\cdot\nabla. \]

The first term describes the change due to time at a fixed position, and the second term describes the change due to movement in space at a fixed time, which combine to describe the rate of change while moving along with the flow.

8. Boltzmann Equation

  • Boltzmann Transport Equation (BTE)

For a conservative system, \[ \frac{\partial f}{\partial t} + \frac{\mathbf{p}}{m}\cdot \frac{\partial f}{\partial \mathbf{r}} + \mathbf{F}\cdot \frac{\partial f}{\partial \mathbf{p}} = \left( \frac{\partial f}{\partial t} \right)_{\mathrm{coll}} \] where \( f \) is the probability density function, and the derivatives are written in the denominator layout convention.

8.1. Probability Density Function

For a system in which the velocity of the particles are not equilibrated, not even locally, the probability density function \( f(\mathbf{r}, \mathbf{p}, t) \) is a good description of the system.

It is the number density in the phase space, satisfying \[ dN = f(\mathbf{r}, \mathbf{p}, t)\, \mathrm{d}^3 \mathbf{r}\, \mathrm{d}^3 \mathbf{p} \] where \( \mathrm{d}N \) is the number of particles in a small chunk of the phase space \( \mathrm{d}^3\mathbf{r}\,\mathrm{d}^3\mathbf{p} \).

8.2. Derivation

According to the Liouville's theorem, the density of state in the phase space does not change in a conservative system. When one is interested in the microscopic behavior, the force once called friction disappears and just molecular interactions remains, constituting a conservative system.

There's still collisions that can disturb the probability density function. So, \[ \frac{\mathrm{d}f}{\mathrm{d}t} = \left( \frac{\partial f}{\partial t} \right)_{\mathrm{coll}}. \] The change of \( f \) due to collision is swept under the simple looking collision term, and it is not an easy task to find the exact form of this term. The total derivative is taken along the trajectory of physical parcel in the phase space, therefore when expanded

\begin{align*} \frac{\partial f}{\partial t} &+ \frac{\mathrm{d}\mathbf{r}}{\mathrm{d} t} \cdot \frac{\partial f}{\partial \mathbf{r}} + \frac{\mathrm{d} \mathbf{p}}{\mathrm{d} t}\cdot \frac{\partial f}{\partial \mathbf{p}} = \left( \frac{\partial f}{\partial t} \right)_{\mathrm{coll}} \\ \implies \frac{\partial f}{\partial t} &+ \frac{\mathbf{p}}{m}\cdot \frac{\partial f}{\partial \mathbf{r}} + \mathbf{F}\cdot \frac{\partial f}{\partial \mathbf{p}} = \left( \frac{\partial f}{\partial t} \right)_{\mathrm{coll}}. \end{align*}

8.3. Derived Definitions

  • Velocity \( \mathbf{v} := \mathbf{p}/m \)
  • Flow Velocity \[ \mathbf{u} := \langle \mathbf{v} \rangle = \int \mathbf{v} f(\mathbf{r}, \mathbf{v}, t)\, \mathrm{d}^3 \mathbf{v}. \]
  • Peculiar Velocity \[ \mathbf{w} := \mathbf{v} - \mathbf{u}. \]
  • Pressure \[ p := \frac{1}{3} \rho \langle w^2 \rangle. \]
  • Pressure Tensor \[ \mathbf{P} := -\boldsymbol{\sigma} = \rho \langle \mathbf{w} \mathbf{w}^{\mathsf{T}}\rangle \] where \( \boldsymbol{\sigma} \) is the stress tensor.
  • Heat Flux \[ \mathbf{h} := \frac{1}{2} \rho \langle w^2 \mathbf{w} \rangle. \]

9. Continuity Equations

  • Transport Equation

They are often derived form the Boltzmann equation.

9.1. Mass Continuity

\[ \frac{\partial \rho}{\partial t} = -\nabla\cdot(\rho\mathbf{u}). \] It arises from the global mass conservation.

9.2. Momentum Continuity

\[ \rho \frac{\mathrm{D}\mathbf{u}}{\mathrm{D}t} = \vec{f}_m(\rho, \mathbf{u}, p, T) \] where \(D/Dt\) is the material derivative, the rate of change while moving along with the flow.

9.3. Energy Continuity

\[ \rho\frac{\mathrm{D}}{\mathrm{D}t}f(\mathbf{u}, T) = f_e(\rho, \mathbf{u}, p, T) \] where the \(f\) is the local energy function.

9.4. Equations of States

  • \[ f_{s,1}(p, \rho, T) = 0 \]
  • \[ f_{s,2}(\mu, T) = 0 \]

10. Navier-Stokes Equation

10.1. General

Assuming the fluid is isothermal, \[ \rho\frac{\mathrm{D}\mathbf{u}}{\mathrm{D}t}=\nabla\cdot\boldsymbol{\sigma}+\rho\mathbf{f} \] where \( \rho \) is the mass density, \( \mathbf{u} \) is the flow velocity, \( \mathrm{D}/\mathrm{D} t \) is the material derivative, \(\boldsymbol{\sigma}\) is Cauchy stress tensor, and \( \mathbf{f} \) is the body force.

The divergence is applied to the index that represent the normal direction. The exact definition differs by author.

10.2. Compressible

We assume the . Substituting, we get: \[ \rho \frac{\mathrm{D} \mathbf{u}}{\mathrm{D} t} = - \nabla p + \nabla \cdot \left[ \mu \left( \nabla \mathbf{u} + (\nabla \mathbf{u})^{\mathsf{T}} - \frac{2}{3}(\nabla \cdot \mathbf{u})\mathbf{I} \right) \right] + \nabla (\zeta \nabla \cdot \mathbf{u}) + \rho \mathbf{f}. \]

10.3. Incompressible

For a incompressible fluid \( \nabla\cdot \mathbf{u} = 0 \), simplifying the equation: \[ \rho\frac{\mathrm{D}\mathbf{u}}{\mathrm{D}t}=-\nabla p+\mu\nabla^2\mathbf{u}+\rho\mathbf{f}. \]

Note that \(\nabla\cdot \boldsymbol{\tau} = \mu\nabla^{\cdot 2}\mathbf{u}\) here, and this fluid can be called Newtonian.

10.4. Solutions

The existence of smooth solution is proven for 2D, with the help of critical quantity that is invariant under scaling.

11. Reynolds Number

Determining factor for the generation of turbulent flow.

\[ \mathrm{Re} := \frac{u L}{\nu} \] where \( u \) is the mean velocity of the fluid, \( L \) is the characteristic length of the system, and \( \nu \) is the kinematic viscosity.

Turbulence occurs when the momentum is not transferred fast enough, with high velocity, long distance, and low momentum diffusion. Turbulence starts to form around \( \mathrm{Re} \sim 10^{3} \).

12. Lamb Vector

  • Named after physicist Horace Lamb

12.1. Vorticity

\[ \boldsymbol{\omega} = \nabla\times \mathbf{u}. \]

12.2. Definition

  • The cross product of vorticity vector \(\boldsymbol{\omega}\) and velocity vector \(\mathbf{u}\) of the flow field: \[ \mathbf{l} = \mathbf{u}\times \boldsymbol{\omega}. \]
  • This appears in the convective acceleration term of the material derivative in the Navier-Stokes equation.

12.3. Beltrami Flow

  • Flow in which the vorticity vector and the velocity vector are parallel.
  • Flow in which the Lamb vector is zero.

13. Boussinesq Approximation

Used for fields of buoyancy-driven flow.

14. Young-Laplace Equation

\[ \Delta p = -\gamma \div{\hat{\vb{n}}} \] Laplace pressure \( \Delta p \) is developed across a surface with surface tension \( \gamma \).

15. References

Author: Jeemin Kim

Created: 2026-09-10 Thu 22:08