θ = θ (s,υ). (1.4) θ (s,υ) υ υ
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1 1.1 Thermodynamics of Fluids 1 Specific Heats of Fluids Elastic Solids Using the free energy per unit mass ψ as a thermodynamic potential we have the caloric equation of state ψ = ψ ˆ (θυ) (1.1.1) the thermal equations of state s = ŝ(θυ) = ψ ˆ (θυ) p = ˆp(θυ) = (1.1.2) ψ ˆ (θυ) where θ is the absolute temperature s is the entropy per unit mass υ is the specific volume p is the pressure. Other combinations of thermodynamic state variables may be used. The internal energy per unit mass is u =ψ + sθ. (1.3) Solving the relation s = ŝ(θυ) for θ we have Therefore u can be expressed by θ = θ (sυ). (1.4) u(sυ) u = ˆ ψ ( θ (sυ)υ) + s θ (sυ) = u(sυ) (1.1.5) u(sυ) = ψ ˆ (θυ) = s θ (sυ) θ (sυ) = ψ ˆ (θυ) υ + s θ (sυ) = p s θ (sυ) + s θ (sυ) + ψ ˆ (θυ) + θ (sυ) + θ (sυ) = θ (sυ) θ (sυ) + s θ (sυ) + s θ (sυ) = p(sυ) (1.1.6) (1.7) where we have used (1.1.2). That is corresponding to the caloric equation of state we have thermal equations of state u = u(sυ) (1.1.8) 1 For the derivation of the general equations see the book Continuum Mechanics by Ellis H. Dill CRC Press 2007: Section for fluids Section 2.1 for elastic solids. 1
2 θ = θ (sυ) = u(sυ) p = p(sυ) = u(sυ). (1.1.9) The enthalpy per unit mass is h = u + pυ. (1.10) Solving the equation of state p = p(sυ) forυ : The enthalpy can therefore be expressed as υ = υ(s p). (1.11) h(s p) h(s p) h = u(sυ(s p)) + pυ(s p) = h(s p) (1.1.12) = u(sυ) + u(sυ) (s p) s s (s p) (s p) = θ p + p s s = u(sυ) (s p) (s p) + p s = θ (s p) (s p) + p +υ(s p) (s p) (s p) = p + p +υ(s p) = υ(s p). (1.1.13) (1.14) That is corresponding to the caloric equation of state we have thermal equations of state h = h(s p) (1.15) h(s p) θ = θ (s p) = h(s p) υ = υ(s p) =. (1.16) The free enthalpy per unit mass (Gibbs function) is g = h sθ (1.17) Solving the equation of state θ = θ (s p) for s : s = s(θ p). (1.18) Therefore the free enthalpy can be expressed as 2
3 g(θ p) g = h( s(θ p) p) θ s(θ p) = g(θ p) (1.1.19) = g(θ p) h(s p) s s(θ p) θ s(θ p) s(θ p) = θ s(θ p) θ s(θ p) s(θ p) = s(θ p) = h(s p) + h(s p) s s(θ p) θ s(θ p) = υ +θ s(θ p) θ s(θ p) = υ(s p) (1.1.20) (1.21) That is corresponding to the caloric equation of state we have thermal equations of state g = g(θ p) (1.22) s = s(θ p) = g(θ p) υ = υ(s p) = g(θ p). (1.23) Relations between the various equations of state are expressed by Maxwell s reciprocal relations: = 2 ψ θ = υ = 2 u s = υ = + 2 h s = p (1.1.24) The specific heat at constant volume is The specific heat at constant pressure is = 2 g θ =. p c υ = u υ = u υ υ = θ υ. (1.1.25) 3
4 c p = h p = h s p s p = θ p. (1.1.26) The relation between the specific heats is found by using (1.1.12): c p = u υ + u θ p + p p = c υ + u + u s + p s s υ θ p = c υ + p +θ s + p θ p = c υ +θ υ p where we have used the Maxwell reciprocal relation s θ = υ. (1.27) The (volumetric) coefficient of thermal expansion is defined by α = 1. (1.28) υ p The coefficient of thermal stress at constant volume is Therefore the specific heats are related by β = υ. (1.29) c p c υ = θυαβ. (1.30) 4
5 1.2 Thermoelasticity The free energy per unit mass is a function of absolute temperature the strain tensor E: ψ = ˆ ψ (θe). (2.1) The Kirchhoff stress tensor S the entropy per unit mass are determined by s = ψ ˆ (θe) ψ ˆ (θe) S = ρ 0. (2.2) Let us introduce measures per unit reference volume: Then Ψ = ρ 0 ψ η = ρ 0 s U = ρ 0 u H = ρ 0 h G = ρ 0 g. (2.3) η = ˆΨ(θE) S = + ˆΨ(θE) = ˆη(θE) = Ŝ(θE). (2.4) Solve the thermal equation of state η = ˆη(θE) for θ : The internal energy per unit volume is then given by θ = θ (ηe) (2.5) U (ηe) U = Ψ + ηθ = ˆΨ( θ (ηe)e) + η θ (ηe) = U (ηe) (2.6) U (ηe) = ˆΨ(θE) = η θ (ηe) = ˆΨ( θ (ηe)e) = S η θ (ηe) θ (ηe) + η θ (ηe) + η θ (ηe) + ˆΨ( θ (ηe)e) + η θ (ηe) + η + θ (ηe) = θ (ηe). = S(ηE). θ (ηe) + η θ (ηe) (2.7) (2.8) 5
6 That is θ = U (ηe) S = U (ηe) = θ (ηe) = S(ηE). Solve the equation of state S = S(ηE) for E to obtain E = E(ηS) (2.9) The enthalpy per unit volume is then given by That is H = U S :E = U (ηe(ηs)) S :E(ηS) = H(ηS) (2.10) H(ηS) H(ηS) = U (ηe) = θ + S : (ηs) = U (ηe) = S : (ηs) + U (ηe) : (ηs) θ = H(ηS) (ηs) S : (ηs) S : (ηs) E = H(ηS) S : (ηs) = θ (ηs) = E(ηS). S : (ηs) = θ (ηs) E(ηS) E(ηS) = E(ηS). (2.11) (2.12) (2.13) Invert the equation θ = θ (ηs) to obtain η = η(θs) (2.14) The free enthalpy per unit volume is then given by G = H ηθ = H( η(θs)s) θ η(θs) = G(θS) (2.15) G(θS) = H( η(θs)s) (θs) θ η(θs) η(θs) = θ η(θs) θ η(θs) η(θs) = η(θs) (2.16) 6
7 That is G(θS) = H(ηS) + H(ηS) (θs) θ η(θs) = E +θ η(θs) θ η(θs) = E(θS). η = G(θS) E = G(θS) = η(θs) = E(θS). (2.17) (2.18) The Maxwell reciprocal relations for elasticity are = ˆΨ(θE) = ˆΨ(θE) = θ E = U (ηe) = U (ηe) = η E = H(ηS) = H(ηS) = η S = G(θS) = G(θS) =. θ S (2.19) The specific heat at constant strain is The specific heat at constant stress is C E = U = U (ηe) E ˆη(θE) = θ E. (2.20) C S = H = H(ηS) (θs) = θ. (2.21) S S Alternative constitutive formulas for the internal energy are U = U (ηe) = U ( ˆη(θE)E) = U ˆ (θe) = U ˆ (θ E(θS)) = U (θs) = U (θ (ηs)s) = U (ηs). (2.22) From (2.10) 7
8 Using a Maxwell reciprocal relation C S = U (θs) S : E(θS) = U ˆ (θe) + U ˆ (θe) : E(θS) S : E(θS) = C E + U (ηe) + U (ηe) ˆη(θE) S : E(θS) = C E + S +θ ˆη(θE) S : E(θS) = C E +θ ˆη(θE) : E(θS). C S C E = θ Ŝ(θE) : E(θS) (2.23) (2.24) 1.3 Small Deformations 2 Let θ 0 denote the reference temperature T = θ θ 0 denote the temperature change. We consider the case when T << θ 0 E = ε << 1. The constitutive relation for the free energy is Ψ = ˆΨ(T E). (3.1) Exp the constitutive function ˆΨ as a power series in the strain retain quadratic terms: Ψ = ˆΨ 0 (θ) ˆβ(θ) :E + 1 E :Ĉ(θ) :E (3.2) 2 where From (2.4) From (2.20) ˆΨ 0 (T ) = ˆΨ(T 0) ˆβ(T ) = ˆΨ(T E) E=0 Ĉ(T ) = 2 ˆΨ(T E) 2. E=0 S = Ŝ(T E) = ˆβ(T ) + Ĉ(T ) : E η = ˆη(T E) = ˆΨ 0 (T ) T (3.3) + ˆβ(T ) T :E 1 2 E : Ĉ(T ) T :E. (3.4) 2 Sections of my Continuum Mechanics. 8
9 For isotropic materials ( ) 2 ˆΨ0 (T ) C E = T +θ 0 T 2 ˆβ(T ) = ˆβ(T )1 + 2 ˆβ(T ) T 2 :E 1 2 E : 2 Ĉ(T ) T 2 :E Ĉ(T ) = 2 ˆµ(T )I + ˆλ(T )11. (3.5) Consider the special case when the dependence of the moduli µ λ on temperature is neglected ˆβ(T ) is a linear function: Then ˆβ(T ) = 3καT (3.6) κ = λ µ. (3.7) S = 3καT1 + λ ( tre)1 + 2µE (3.8) η = ˆΨ 0 (T ) T + 3κα ( tre). (3.9) The inverse of (3.8) is λ E = αt1 2µ + 3λ tr S 2µ 1 + S 2µ (3.10) so that α is the coefficient of thermal expansion. From (3.5) C E = θ 0 2 ˆΨ0 (T ) T 2 (3.11) for T << θ 0. From (2.24) C S = C E + 9κα 2 θ 0. (3.12) where θ is the absolute temperature κ is the bulk modulus α is the coefficient of lineal expansion. 9
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