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Thermomechanical processes, balance laws and the Clausius–Duhem inequalities

Definition
ClausiusDuhem_thermo_process

by Lucas · Oct 9, 2026 · Mathlib 0df444a (Lean v4.33.1)

continuum-mechanicsmathematical-physicsthermodynamics

A thermomechanical process on R3\mathbb R^3R3 is a collection of fields of time ttt and position xxx: mass density ρ\rhoρ, specific entropy η\etaη, velocity v\mathbf vv, heat flux q\mathbf qq, energy source per unit mass sss, absolute temperature TTT, specific internal energy eee and Cauchy stress σ\boldsymbol\sigmaσ. With the operators of the field-calculus definition:

  1. Regularity: ρ,η,v,q,T,e\rho,\eta,\mathbf v,\mathbf q,T,eρ,η,v,q,T,e are C1C^1C1 jointly in (t,x)(t,x)(t,x) and sss is jointly continuous.
  2. Integral Clausius–Duhem inequality on every fixed control volume, here every box Ω=[a,b]\Omega=[a,b]Ω=[a,b] with ai<bia_i<b_iai​<bi​:
ddt∫Ωρη dV≥−∫∂Ωρη v⋅n dA−∫∂Ωq⋅nT dA+∫ΩρsT dV.\frac{d}{dt}\int_\Omega\rho\eta\,dV\ge-\int_{\partial\Omega}\rho\eta\,\mathbf v\cdot\mathbf n\,dA-\int_{\partial\Omega}\frac{\mathbf q\cdot\mathbf n}{T}\,dA+\int_\Omega\frac{\rho s}{T}\,dV.dtd​∫Ω​ρηdV≥−∫∂Ω​ρηv⋅ndA−∫∂Ω​Tq⋅n​dA+∫Ω​Tρs​dV.
  1. Conservation of mass: ρ˙+ρ ∇⋅v=0\dot\rho+\rho\,\nabla\cdot\mathbf v=0ρ˙​+ρ∇⋅v=0.
  2. Balance of energy: ρe˙−σ:∇v+∇⋅q−ρs=0\rho\dot e-\boldsymbol\sigma:\nabla\mathbf v+\nabla\cdot\mathbf q-\rho s=0ρe˙−σ:∇v+∇⋅q−ρs=0.
  3. Differential (entropy) form: ρη˙≥−∇⋅(q/T)+ρs/T\rho\dot\eta\ge-\nabla\cdot(\mathbf q/T)+\rho s/Tρη˙​≥−∇⋅(q/T)+ρs/T.
  4. Internal-energy form: ρ(e˙−Tη˙)−σ:∇v≤−q⋅∇T/T\rho(\dot e-T\dot\eta)-\boldsymbol\sigma:\nabla\mathbf v\le-\mathbf q\cdot\nabla T/Tρ(e˙−Tη˙​)−σ:∇v≤−q⋅∇T/T.
  5. Dissipation: D=ρ(Tη˙−e˙)+σ:∇v−q⋅∇T/T\mathcal D=\rho(T\dot\eta-\dot e)+\boldsymbol\sigma:\nabla\mathbf v-\mathbf q\cdot\nabla T/TD=ρ(Tη˙​−e˙)+σ:∇v−q⋅∇T/T.

Conditions 3–6 are required at every time and every point.

Formalization Note The control volumes are the non-degenerate boxes; the source's general moving-boundary form (normal velocity unu_nun​) is specialised to fixed control volumes, un=0u_n=0un​=0, which is the case the source's derivation uses. Division by TTT is Lean division (with x/0=0x/0=0x/0=0); every theorem of the mission that divides by TTT in an essential way assumes T>0T>0T>0.

Definition code
import Definitions.Def_ClausiusDuhem_field_calculus

/-!
Thermomechanical processes of a continuum and the balance laws / inequalities appearing in
the Wikipedia article "Clausius–Duhem inequality" (oldid=1182390552).
-/

namespace ClausiusDuhem

/-- A thermomechanical process of a continuum body occupying `ℝ³`: every field is a function
of time `t` and of the spatial point `x`. -/
structure ThermoProcess where
  /-- mass density `ρ` -/
  rho : ℝ → Space → ℝ
  /-- specific entropy (entropy per unit mass) `η` -/
  eta : ℝ → Space → ℝ
  /-- velocity of the particles `v` -/
  vel : ℝ → Space → Fin 3 → ℝ
  /-- heat flux vector `q` -/
  heatFlux : ℝ → Space → Fin 3 → ℝ
  /-- energy source per unit mass `s` -/
  source : ℝ → Space → ℝ
  /-- absolute temperature `T` -/
  temp : ℝ → Space → ℝ
  /-- specific internal energy (internal energy per unit mass) `e` -/
  energy : ℝ → Space → ℝ
  /-- Cauchy stress tensor `σ` -/
  stress : ℝ → Space → Matrix (Fin 3) (Fin 3) ℝ

/-- A time-dependent field is `C¹` jointly in time and space. -/
def IsC1Field {β : Type} [NormedAddCommGroup β] [NormedSpace ℝ β]
    (φ : ℝ → Space → β) : Prop :=
  ContDiff ℝ 1 (fun p : ℝ × Space => φ p.1 p.2)

/-- Standing regularity of a process: `ρ, η, v, q, T, e` are continuously differentiable
jointly in `(t, x)`, and the source `s` is jointly continuous. -/
def ThermoProcess.Smooth (P : ThermoProcess) : Prop :=
  IsC1Field P.rho ∧ IsC1Field P.eta ∧ IsC1Field P.vel ∧ IsC1Field P.heatFlux ∧
    IsC1Field P.temp ∧ IsC1Field P.energy ∧
    Continuous (fun p : ℝ × Space => P.source p.1 p.2)

/-- The integral Clausius–Duhem inequality for every fixed control volume (so the normal
velocity of the boundary is `u_n = 0`), with control volumes the non-degenerate closed
rectangular boxes `Ω = [a, b]`:
`d/dt ∫_Ω ρη dV ≥ ∫_{∂Ω} ρη(0 - v·n) dA - ∫_{∂Ω} (q·n)/T dA + ∫_Ω ρs/T dV`. -/
def ThermoProcess.IntegralEntropyInequality (P : ThermoProcess) : Prop :=
  ∀ (a b : Space), (∀ i, a i < b i) → ∀ t : ℝ,
    deriv (fun τ => ∫ x in Set.Icc a b, P.rho τ x * P.eta τ x) t ≥
      -boxOutwardFlux (fun x => (P.rho t x * P.eta t x) • P.vel t x) a b
      - boxOutwardFlux (fun x => (P.temp t x)⁻¹ • P.heatFlux t x) a b
      + ∫ x in Set.Icc a b, P.rho t x * P.source t x / P.temp t x

/-- Conservation of mass: `ρ̇ + ρ ∇·v = 0` at every time and point. -/
def ThermoProcess.MassConservation (P : ThermoProcess) : Prop :=
  ∀ t x, materialDeriv P.rho P.vel t x + P.rho t x * div (P.vel t) x = 0

/-- Balance of energy: `ρ ė - σ : ∇v + ∇·q - ρ s = 0` at every time and point. -/
def ThermoProcess.EnergyBalance (P : ThermoProcess) : Prop :=
  ∀ t x, P.rho t x * materialDeriv P.energy P.vel t x
      - doubleDot (P.stress t x) (velocityGradient (P.vel t) x)
      + div (P.heatFlux t) x - P.rho t x * P.source t x = 0

/-- The Clausius–Duhem inequality in differential form (in terms of the specific entropy):
`ρ η̇ ≥ -∇·(q/T) + ρ s / T` at every time and point. -/
def ThermoProcess.EntropyInequality (P : ThermoProcess) : Prop :=
  ∀ t x, P.rho t x * materialDeriv P.eta P.vel t x ≥
    -div (fun y => (P.temp t y)⁻¹ • P.heatFlux t y) x + P.rho t x * P.source t x / P.temp t x

/-- The Clausius–Duhem inequality in terms of the specific internal energy:
`ρ (ė - T η̇) - σ : ∇v ≤ -(q · ∇T)/T` at every time and point. -/
def ThermoProcess.InternalEnergyInequality (P : ThermoProcess) : Prop :=
  ∀ t x, P.rho t x * (materialDeriv P.energy P.vel t x
        - P.temp t x * materialDeriv P.eta P.vel t x)
      - doubleDot (P.stress t x) (velocityGradient (P.vel t) x) ≤
    -(dot (P.heatFlux t x) (grad (P.temp t) x) / P.temp t x)

/-- The dissipation `𝒟 = ρ (T η̇ - ė) + σ : ∇v - (q · ∇T)/T`. -/
noncomputable def ThermoProcess.dissipation (P : ThermoProcess) (t : ℝ) (x : Space) : ℝ :=
  P.rho t x * (P.temp t x * materialDeriv P.eta P.vel t x - materialDeriv P.energy P.vel t x)
    + doubleDot (P.stress t x) (velocityGradient (P.vel t) x)
    - dot (P.heatFlux t x) (grad (P.temp t) x) / P.temp t x

end ClausiusDuhem
Source
Wikipedia, "Clausius–Duhem inequality", revision oldid=1182390552, https://en.wikipedia.org/w/index.php?title=Clausius%E2%80%93Duhem_inequality&oldid=1182390552, sections "Clausius–Duhem inequality in terms of the specific entropy" (integral form with u_n = 0, differential form, conservation of mass), "Clausius–Duhem inequality in terms of specific internal energy" (balance of energy, internal-energy form) and "Dissipation".
Read-back

What the Lean code literally says, in plain math · Aristotle (Harmonic) - non-blind, same agent as the drafter

Non-blind read-back — not independent testimony. This read-back was written by the same agent (Aristotle, by Harmonic) that drafted the Lean statements, with full knowledge of the source article and of the intended meaning. It was not produced by a blind, independent auditor, so it must not be mistaken for independent testimony; reviewers should compare it against the Lean code themselves.

This file (importing the field-calculus file, whose operators ∂j,∇,∇⋅,⋅,∇v,:,∂t,( )˙,Φ[a,b]\partial_j,\nabla,\nabla\cdot,\cdot,\nabla v, :,\partial_t,\dot{(\ )},\Phi_{[a,b]}∂j​,∇,∇⋅,⋅,∇v,:,∂t​,( )˙​,Φ[a,b]​ are used below with the meanings given there) defines, in namespace ClausiusDuhem:

  1. ThermoProcess: a record of eight functions of (t,x)∈R×R3(t,x)\in\mathbb R\times\mathbb R^3(t,x)∈R×R3: real-valued ρ\rhoρ (rho), η\etaη (eta), sss (source), TTT (temp), eee (energy); R3\mathbb R^3R3-valued vvv (vel), qqq (heatFlux); and 3×33\times33×3-matrix-valued σ\sigmaσ (stress). No sign, positivity or regularity condition is part of the record.
  2. IsC1Field φ\varphiφ: the map (t,x)↦φ(t,x)(t,x)\mapsto\varphi(t,x)(t,x)↦φ(t,x) on R×R3\mathbb R\times\mathbb R^3R×R3 is once continuously differentiable (jointly).
  3. Smooth PPP: ρ,η,v,q,T,e\rho,\eta,v,q,T,eρ,η,v,q,T,e are all IsC1Field, and (t,x)↦s(t,x)(t,x)\mapsto s(t,x)(t,x)↦s(t,x) is continuous. Nothing is assumed about σ\sigmaσ.
  4. IntegralEntropyInequality PPP: for all a,b∈R3a,b\in\mathbb R^3a,b∈R3 with ai<bia_i<b_iai​<bi​ for i=0,1,2i=0,1,2i=0,1,2, and every t∈Rt\in\mathbb Rt∈R,
ddτ∣τ=t∫[a,b]ρ(τ,x)η(τ,x) dx  ≥  −Φ[a,b](x↦ρη v (t,x))−Φ[a,b](x↦T(t,x)−1q(t,x))+∫[a,b]ρ(t,x)s(t,x)T(t,x) dx,\frac{d}{d\tau}\Big|_{\tau=t}\int_{[a,b]}\rho(\tau,x)\eta(\tau,x)\,dx\;\ge\;-\Phi_{[a,b]}\big(x\mapsto\rho\eta\,v\,(t,x)\big)-\Phi_{[a,b]}\big(x\mapsto T(t,x)^{-1}q(t,x)\big)+\int_{[a,b]}\frac{\rho(t,x)s(t,x)}{T(t,x)}\,dx,dτd​​τ=t​∫[a,b]​ρ(τ,x)η(τ,x)dx≥−Φ[a,b]​(x↦ρηv(t,x))−Φ[a,b]​(x↦T(t,x)−1q(t,x))+∫[a,b]​T(t,x)ρ(t,x)s(t,x)​dx,

with [a,b][a,b][a,b] the closed box and dxdxdx Lebesgue measure. The derivative is the one-variable derivative (equal to 000 where it does not exist); integrals are 000 for non-integrable integrands; T−1T^{-1}T−1 and /T/T/T give 000 where T=0T=0T=0. 5. MassConservation PPP: for all t,xt,xt,x: ρ˙(t,x)+ρ(t,x) (∇⋅v(t,⋅))(x)=0\dot\rho(t,x)+\rho(t,x)\,(\nabla\cdot v(t,\cdot))(x)=0ρ˙​(t,x)+ρ(t,x)(∇⋅v(t,⋅))(x)=0. 6. EnergyBalance PPP: for all t,xt,xt,x: ρ e˙−σ:∇v+∇⋅q−ρs=0\rho\,\dot e-\sigma:\nabla v+\nabla\cdot q-\rho s=0ρe˙−σ:∇v+∇⋅q−ρs=0, everything evaluated at (t,x)(t,x)(t,x), with e˙\dot ee˙ the material derivative of eee along vvv, ∇v\nabla v∇v and ∇⋅q\nabla\cdot q∇⋅q taken in xxx at fixed ttt. 7. EntropyInequality PPP: for all t,xt,xt,x:

ρ η˙  ≥  −∇⋅(y↦T(t,y)−1q(t,y))(x)+ρsT.\rho\,\dot\eta\;\ge\;-\nabla\cdot\big(y\mapsto T(t,y)^{-1}q(t,y)\big)(x)+\frac{\rho s}{T}.ρη˙​≥−∇⋅(y↦T(t,y)−1q(t,y))(x)+Tρs​.
  1. InternalEnergyInequality PPP: for all t,xt,xt,x:
ρ (e˙−Tη˙)−σ:∇v  ≤  −q⋅∇T(t,⋅)(x)T.\rho\,(\dot e-T\dot\eta)-\sigma:\nabla v\;\le\;-\frac{q\cdot\nabla T(t,\cdot)(x)}{T}.ρ(e˙−Tη˙​)−σ:∇v≤−Tq⋅∇T(t,⋅)(x)​.
  1. dissipation P t xP\,t\,xPtx :=ρ(Tη˙−e˙)+σ:∇v−q⋅∇TT:=\rho(T\dot\eta-\dot e)+\sigma:\nabla v-\dfrac{q\cdot\nabla T}{T}:=ρ(Tη˙​−e˙)+σ:∇v−Tq⋅∇T​, all at (t,x)(t,x)(t,x) (a real number; the last term is 000 if T(t,x)=0T(t,x)=0T(t,x)=0).

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