Physics · Book 4 · Bachelor Year 2

University Physics — Year 2

University Physics — Year 2 · Bachelor Year 2

28Thermodynamic Potentials

Stretch a rubber band quickly and touch it to your lip: it is warm; let it contract and it is cool. Hang a weight on it and warm it with a hair-dryer: it shortens. No steel spring behaves so, and the reason is that a rubber band’s tension is not a matter of energy but of entropy — the stretched chains have fewer ways to arrange themselves. To reason about such things one needs to know what a system at fixed temperature, or at fixed temperature and pressure, tends to do, and how much work can be drawn from it: questions the internal energy and the entropy answer only clumsily, because they speak the language of an isolated system. This chapter introduces the two functions built for the laboratory’s conditions, the Helmholtz free energy F=UTSF = U - TS and the Gibbs free enthalpy G=HTSG = H - TS, shows that they measure the recoverable work and decrease toward equilibrium, extracts from their differentials the Maxwell relations that link quantities no one would have thought related, and applies the whole to the equilibrium of two phases, where GG decides which phase wins and gives back Clapeyron’s formula.

Ice and water coexisting on a lake at dawn: at the melting point the two phases have the same free enthalpy per kilogram, and a small change of pressure or temperature tips the balance — the Clapeyron slope tells by how much.
Ice and water coexisting on a lake at dawn: at the melting point the two phases have the same free enthalpy per kilogram, and a small change of pressure or temperature tips the balance — the Clapeyron slope tells by how much.

28.1 The fundamental identity and its variables

Proposition 28.1 (Fundamental identity)

For a closed system of fixed composition, the internal energy, regarded as a function of the entropy and the volume, satisfies

 ⁣dU=T ⁣dSP ⁣dV,T=(US)V,P=(UV)S,\dd U = T\,\dd S - P\,\dd V, \qquad T = \Big(\frac{\partial U}{\partial S}\Big)_V, \quad P = -\Big(\frac{\partial U}{\partial V}\Big)_S ,

and the enthalpy H=U+PVH = U + PV satisfies  ⁣dH=T ⁣dS+V ⁣dP\dd H = T\,\dd S + V\,\dd P. Each function, in its natural variables(S,V)(S,V) for UU, (S,P)(S,P) for HH — contains the whole thermodynamics of the system: its partial derivatives give the other state variables. The second law selects the equilibrium of an isolated system (fixed UU, VV) as the state of maximum SS.

Proof. The first law for a reversible transformation,  ⁣dU=δQrev+δWrev=T ⁣dSP ⁣dV\dd U = \delta Q_{\text{rev}} + \delta W_{\text{rev}} = T\,\dd S - P\,\dd V, involves only state functions and therefore holds for any infinitesimal change between equilibrium states. Add  ⁣d(PV)\dd(PV) for HH.

Remark 28.2 (Why new functions)

Experiments are not done at fixed entropy. A chemist’s flask sits at the temperature of the room and the pressure of the atmosphere; a piston in a thermostat works at fixed TT. One wants functions whose natural variables are (T,V)(T,V) and (T,P)(T,P), and which play, under those conditions, the role that SS plays for an isolated system: to tell which way the system evolves and how much work it can give. A Legendre transform — subtracting TSTS to trade SS for TT as the independent variable — builds them.

28.2 Free energy and free enthalpy

Definition 28.3 (Helmholtz free energy, Gibbs free enthalpy)

F=UTS(free energy),G=HTS=U+PVTS(free enthalpy).F = U - TS \quad\text{(\emph{free energy})}, \qquad G = H - TS = U + PV - TS \quad\text{(\emph{free enthalpy})}.

Both are extensive state functions, measured in joules.

Theorem 28.4 (Differentials and derived quantities)

 ⁣dF=S ⁣dTP ⁣dV, ⁣dG=S ⁣dT+V ⁣dP;\dd F = -S\,\dd T - P\,\dd V, \qquad \dd G = -S\,\dd T + V\,\dd P ;

hence, in the natural variables (T,V)(T,V) of FF and (T,P)(T,P) of GG,

S=(FT)V,P=(FV)T,S=(GT)P,V=(GP)T,S = -\Big(\frac{\partial F}{\partial T}\Big)_V, \quad P = -\Big(\frac{\partial F}{\partial V}\Big)_T, \qquad S = -\Big(\frac{\partial G}{\partial T}\Big)_P, \quad V = \Big(\frac{\partial G}{\partial P}\Big)_T ,

and (Gibbs–Helmholtz) U=FT(F/T)V=T2(F/T)/TU = F - T(\partial F/\partial T)_V = -T^2\,\partial(F/T)/\partial T, H=T2(G/T)/TH = -T^2\,\partial(G/T)/\partial T. Knowing F(T,V)F(T,V) or G(T,P)G(T,P) is knowing everything: the equation of state, the entropy, the energy, the heat capacities.

Proof.  ⁣dF= ⁣dUT ⁣dSS ⁣dT=S ⁣dTP ⁣dV\dd F = \dd U - T\dd S - S\dd T = -S\dd T - P\dd V; likewise for GG from  ⁣dH\dd H. Read off the partial derivatives; for Gibbs–Helmholtz, FTTF=F+TS=UF - T\,\partial_TF = F + TS = U and T(F/T)=(TTFF)/T2=U/T2\partial_T(F/T) = (T\partial_TF - F)/T^2 = -U/T^2.

Example 28.5 (The perfect gas)

For nn moles, U=ncVT+U0U = nc_{V}T + U_0 and S=ncVlnT+nRlnV+S0S = nc_V\ln T + nR\ln V + S_0 give F(T,V)=nRTlnV+f(T)F(T,V) = -nRT\ln V + f(T): then P=VF=nRT/VP = -\partial_VF = nRT/V — the equation of state comes out of FF — and S=TFS = -\partial_TF gives back the entropy. In the variables (T,P)(T,P), G(T,P)=nRTlnP+g(T)G(T,P) = nRT\ln P + g(T), so V=PG=nRT/PV = \partial_PG = nRT/P, and the molar free enthalpy μ(T,P)=μ(T)+RTln(P/P)\mu(T,P) = \mu^\circ(T) + RT\ln(P/P^\circ) — the chemical potential of the gas, which grows with its pressure: gas flows from high to low μ\mu, here from high to low pressure.

28.3 Maximum work and the direction of evolution

Theorem 28.6 (Monothermal transformations)

A system exchanging heat with a single thermostat at T0T_0, and whose initial and final temperatures equal T0T_0, receives during any transformation the work

WΔF,i.e.Wrecovered=WΔF:W \ge \Delta F , \qquad\text{i.e.}\qquad W_{\text{recovered}} = -W \le -\Delta F :

the decrease of FF is the maximum work recoverable from the system at fixed temperature (reached for a reversible transformation) — hence “free” energy: the part of UU that can be turned into work, the rest, TSTS, being bound. If moreover the transformation is monobaric (pressure P0P_0 outside, initial and final pressure P0P_0), the work other than that of the atmosphere (useful work, e.g. electrical) satisfies WuΔGW_{\text{u}} \ge \Delta G: ΔG-\Delta G is the maximum useful work recoverable at fixed TT and PP (the work of a fuel cell, of a battery).

Proof. First law: ΔU=W+Q\Delta U = W + Q. Second law with one thermostat: ΔS=Q/T0+Sc\Delta S = Q/T_0 + S_{\text{c}}, Sc0S_{\text{c}} \ge 0, so QT0ΔSQ \le T_0\Delta S. Hence W=ΔUQΔUT0ΔS=Δ(UT0S)=ΔFW = \Delta U - Q \ge \Delta U - T_0\Delta S = \Delta(U - T_0S) = \Delta F, using T=T0T = T_0 at both ends. With the atmosphere’s work P0ΔV-P_0\Delta V separated, W=WuP0ΔVW = W_{\text{u}} - P_0\Delta V and WuΔU+P0ΔVT0ΔS=ΔGW_{\text{u}} \ge \Delta U + P_0 \Delta V - T_0\Delta S = \Delta G.

Theorem 28.7 (Criteria of evolution and equilibrium)

A system held at fixed TT and VV and receiving no work can only evolve so that FF decreases; its equilibrium is the state of minimum FF. A system held at fixed TT and PP and receiving no useful work can only evolve so that GG decreases; its equilibrium is the state of minimum GG. (More generally, for a system in contact with a surrounding at T0T_0, P0P_0, the quantity UT0S+P0VU - T_0S + P_0V decreases.)

Proof. Take W=0W = 0 (resp. Wu=0W_{\text{u}} = 0) in the previous theorem: ΔF0\Delta F \le 0 (resp. ΔG0\Delta G \le 0), with equality for a reversible, i.e. equilibrium, evolution.

Example 28.8 (Isothermal expansion, real and ideal)

One mole of gas at 300K300\,\mathrm{K} expands from 1L1\,\mathrm{L} to 10L10\,\mathrm{L} in contact with the thermostat: ΔF=RTln10=5.7kJ\Delta F = -RT\ln 10 = -5.7\,\mathrm{kJ}. A reversible expansion recovers 5.7kJ5.7\,\mathrm{kJ}; an expansion against the atmosphere at 1bar1\,\mathrm{bar} recovers only P0ΔV=0.9kJP_0\Delta V = 0.9\,\mathrm{kJ}; a free expansion into vacuum, nothing. The 5.7kJ5.7\,\mathrm{kJ} is the maximum the gas and its thermostat can give for this change of state, however clever the machine.

28.4 Maxwell relations

Theorem 28.9 (Maxwell relations)

Because  ⁣dF\dd F and  ⁣dG\dd G are exact differentials (Schwarz’s theorem on mixed second derivatives),

(SV)T=(PT)V,(SP)T=(VT)P.\Big(\frac{\partial S}{\partial V}\Big)_T = \Big(\frac{\partial P}{\partial T}\Big)_V, \qquad \Big(\frac{\partial S}{\partial P}\Big)_T = -\Big(\frac{\partial V}{\partial T}\Big)_P .

They express the unmeasurable (how the entropy varies with volume or pressure at fixed temperature) through the equation of state. Two consequences:

(UV)T=T(PT)VP,CPCV=T(PT)V(VT)P=TVα2κT,\Big(\frac{\partial U}{\partial V}\Big)_T = T\Big(\frac{\partial P}{\partial T}\Big)_V - P, \qquad C_P - C_V = T\Big(\frac{\partial P}{\partial T}\Big)_V\Big(\frac{\partial V}{\partial T}\Big)_P = \frac{TV\alpha^2}{\kappa_T} ,

with α=V1(V/T)P\alpha = V^{-1}(\partial V/\partial T)_P the expansion coefficient and κT=V1(V/P)T\kappa_T = -V^{-1}(\partial V/\partial P)_T the isothermal compressibility.

Proof. 2F/TV\partial^2F/\partial T\partial V computed in both orders: VS=TP-\partial_VS = -\partial_TP. Same for GG. Then  ⁣dU=T ⁣dSP ⁣dV\dd U = T\dd S - P\dd V at fixed TT gives (VU)T=T(VS)TP(\partial_VU)_T = T(\partial_VS)_T - P; and CPCVC_P - C_V follows from writing S(T,V(T,P))S(T,V(T,P)): (TS)P=(TS)V+(VS)T(TV)P(\partial_TS)_P = (\partial_TS)_V + (\partial_VS)_T(\partial_TV)_P, multiplied by TT.

Example 28.10 (What the relations reveal)

For a perfect gas, T(TP)VP=0T(\partial_TP)_V - P = 0: the energy does not depend on the volume (Joule’s law recovered) and CPCV=nRC_P - C_V = nR. For a van der Waals gas, (VU)T=a/Vm2(\partial_VU)_T = a/V_{\text{m}}^2: the internal pressure of the attractions. For liquid water, (TP)V=α/κT=2.1×104/4.6×1010=4.6×105Pa/K(\partial_TP)_V = \alpha/\kappa_T = 2.1 \times 10^{-4}/4.6 \times 10^{-10} = 4.6 \times 10^{5}\,\mathrm{Pa}/\mathrm{K}: heating water in a rigid full vessel by one kelvin raises the pressure by 4.6bar4.6\,\mathrm{bar} (never seal a full bottle), and (VU)T1400bar(\partial_VU)_T \approx 1400\,\mathrm{bar} — the cohesion of the liquid; yet cPcV=Tvα2/κT30J/kg/Kc_P - c_V = Tv\alpha^2/\kappa_T \approx 30\,\mathrm{J}/\mathrm{kg}/\mathrm{K}, less than 1%1\% of cPc_P: for condensed matter the two heat capacities nearly coincide.

Proposition 28.11 (Entropic elasticity of rubber)

For a band of length LL under the tension ff,  ⁣dU=T ⁣dS+f ⁣dL\dd U = T\dd S + f\dd L and  ⁣dF=S ⁣dT+f ⁣dL\dd F = -S\dd T + f\dd L, so that (S/L)T=(f/T)L(\partial S/\partial L)_T = -(\partial f/\partial T)_L and (U/L)T=fT(f/T)L(\partial U/\partial L)_T = f - T(\partial f/ \partial T)_L. Rubber obeys, to a good approximation, f=Tφ(L)f = T\,\varphi(L) with φ>0\varphi > 0 for L>L0L > L_0: then (U/L)T=0(\partial U/\partial L)_T = 0 — the energy does not change on stretching — and (S/L)T=φ(L)<0(\partial S/\partial L)_T = -\varphi(L) < 0: the tension is entropic, f=T(S/L)Tf = -T(\partial S/\partial L)_T, the band pulls back because its stretched chains have fewer configurations. Consequences: stretched isothermally it gives off heat (Q=TΔS<0Q = T\Delta S < 0); stretched adiabatically it warms; heated under constant load it contracts (f/Tf/T fixed means φ(L)\varphi(L) fixed, so at fixed ff, φ\varphi must fall as TT rises).

Proof. Maxwell relation from  ⁣dF\dd F; the rest is substitution. The microscopic origin is the random walk of Chapter 24: a chain of NN links of length aa has its end-to-end distance distributed as a Gaussian of variance Na2Na^2, so the number of configurations at extension LL is ΩeL2/2Na2\Omega \propto \eu^{-L^2/2Na^2}, S=S0kBL2/2Na2S = S_0 - k_BL^2/2Na^2 and f=kBTL/Na2f = k_BTL/Na^2: a spring whose stiffness is proportional to the temperature.

Tension at fixed extension against temperature. Left: rubber, f T — the tension is entropic, ( f/ T)_L > 0, so stretching lowers the entropy and the band warms. Right: a steel spring, whose tension comes from the bonds’ energy and falls slightly as the metal softens.
Tension at fixed extension against temperature. Left: rubber, fTf \propto T — the tension is entropic, (f/T)L>0(\partial f/\partial T)_L > 0, so stretching lowers the entropy and the band warms. Right: a steel spring, whose tension comes from the bonds’ energy and falls slightly as the metal softens.

28.5 Equilibrium between two phases

Theorem 28.12 (Condition of coexistence)

A pure substance at fixed TT and PP, split between two phases of masses m1m_1, m2m_2 with free enthalpies per unit mass g1(T,P)g_1(T,P), g2(T,P)g_2(T,P), has G=m1g1+m2g2G = m_1g_1 + m_2g_2; at equilibrium GG is minimal, so

  • if g1<g2g_1 < g_2 all the matter goes into phase 1 (the stable phase is the one of lower gg);
  • the two phases coexist only where

    g1(T,P)=g2(T,P),g_1(T,P) = g_2(T,P) ,

    a relation between TT and PP: the coexistence curve of the phase diagram.

Along that curve (Clapeyron),

 ⁣dP ⁣dT=s2s1v2v1=L12T(v2v1).\frac{\dd P}{\dd T} = \frac{s_2 - s_1}{v_2 - v_1} = \frac{L_{1\to2}}{T\,(v_2 - v_1)} .

Proof.  ⁣dG=(g1g2) ⁣dm1\dd G = (g_1 - g_2)\dd m_1 at fixed TT, PP (with m1+m2m_1 + m_2 fixed): GG decreases by moving mass to the phase of lower gg, until that phase is alone or until g1=g2g_1 = g_2. Differentiate g1=g2g_1 = g_2 along the curve with  ⁣dg=s ⁣dT+v ⁣dP\dd g = -s\,\dd T + v\,\dd P for each phase: s1 ⁣dT+v1 ⁣dP=s2 ⁣dT+v2 ⁣dP-s_1\dd T + v_1\dd P = -s_2\dd T + v_2\dd P; and s2s1=L/Ts_2 - s_1 = L/T since the transition at fixed TT, PP is reversible. The Year 1 volume obtained this formula from a Carnot cycle; here it falls out of GG.

Free enthalpy per unit mass of the three phases at fixed pressure: each falls with temperature with the slope -s, the gas fastest; the stable phase is the lowest line, and the transitions occur where the lines cross. The upper branches beyond a crossing are the metastable states (supercooled liquid, superheated liquid).
Free enthalpy per unit mass of the three phases at fixed pressure: each falls with temperature with the slope s-s, the gas fastest; the stable phase is the lowest line, and the transitions occur where the lines cross. The upper branches beyond a crossing are the metastable states (supercooled liquid, superheated liquid).

Example 28.13 (Water: slopes and metastability)

Fusion: L=334kJ/kgL = 334\,\mathrm{kJ}/\mathrm{kg}, vliqvice=9.1×105m3/kgv_{\text{liq}} - v_{\text{ice}} = -9.1 \times 10^{-5}\,\mathrm{m}^{3}/\mathrm{kg}:  ⁣dP/ ⁣dT=1.3×107Pa/K\dd P/\dd T = -1.3 \times 10^{7}\,\mathrm{Pa}/\mathrm{K}, negative — ice melts under pressure, but 130bar130\,\mathrm{bar} per kelvin: a skater’s 70bar70\,\mathrm{bar} lower the melting point by half a degree only (skating works by friction and a premelted surface layer), while the 270bar270\,\mathrm{bar} under three kilometres of ice sheet melt its base and let it slide. Vaporisation at 100C100\,{}^{\circ}\mathrm{C}: L=2.26MJ/kgL = 2.26\,\mathrm{MJ}/\mathrm{kg}, Δv=1.67m3/kg\Delta v = 1.67\,\mathrm{m}^{3}/\mathrm{kg}: 3.6kPa/K3.6\,\mathrm{kPa}/\mathrm{K}92C92\,{}^{\circ}\mathrm{C} at 0.7bar0.7\,\mathrm{bar} on a mountain, 120C120\,{}^{\circ}\mathrm{C} in a pressure cooker at 2bar2\,\mathrm{bar}. Below 0C0\,{}^{\circ}\mathrm{C}, liquid water has gliqgice(L/Tfus)(TfusT)=1.2kJ/kgg_{\text{liq}} - g_{\text{ice}} \approx (L/T_{\text{fus}})(T_{\text{fus}} - T) = 1.2\,\mathrm{kJ}/\mathrm{kg} per kelvin of supercooling: it is metastable, not unstable, and pure droplets in clouds stay liquid down to 40C-40\,{}^{\circ}\mathrm{C} for want of a nucleus.

A van der Waals isotherm below the critical temperature and Maxwell’s construction: the real isotherm follows the horizontal P_ sat placed so that the two shaded areas are equal — the condition g_ liq = g_ vap, since g = v\, P at fixed T. The rising parts of the loop near the ends are the metastable superheated liquid and supersaturated vapour.
A van der Waals isotherm below the critical temperature and Maxwell’s construction: the real isotherm follows the horizontal PsatP_{\text{sat}} placed so that the two shaded areas are equal — the condition gliq=gvapg_{\text{liq}} = g_{\text{vap}}, since  ⁣dg=v ⁣dP\dd g = v\,\dd P at fixed TT. The rising parts of the loop near the ends are the metastable superheated liquid and supersaturated vapour.

Remark 28.14 (Van der Waals and Maxwell’s construction)

The van der Waals equation (P+a/v2)(vb)=RT(P + a/v^2)(v - b) = RT gives, below its critical temperature Tc=8a/27RbT_{\text{c}} = 8a/27Rb, isotherms with a loop. The real fluid does not follow the loop: at Psat(T)P_{\text{sat}}(T) it jumps from the liquid to the vapour branch, and PsatP_{\text{sat}} is fixed by gliq=gvapg_{\text{liq}} = g_{\text{vap}}, i.e. liqvapv ⁣dP=0\int_{\text{liq}}^{\text{vap}}v\,\dd P = 0 along the loop: the horizontal line cuts off equal areas. The parts of the loop where (P/v)T>0(\partial P/\partial v)_T > 0 are mechanically unstable; the parts between them and the line are metastable — the superheated liquid that “bumps” in a microwave, the supersaturated vapour of the cloud chamber.

Method 28.15 (Using the potentials)

(1) Identify the constraints: isolated \to SS max; fixed T,VT,V \to FF min; fixed T,PT,P \to GG min. (2) Maximum work: ΔF-\Delta F at fixed TT, ΔG-\Delta G of useful work at fixed T,PT,P. (3) Need a derivative of SS at fixed TT? Use a Maxwell relation and the equation of state. (4) Two phases: compare gg; coexistence g1=g2g_1 = g_2; Clapeyron for the slope; sign of Δv\Delta v for the sign of the slope. (5) Chemical potential μ=g\mu = g per mole: matter flows toward lower μ\mu.

28.6 Exercises

Exercise 28.1

For nn moles of perfect gas, write F(T,V)F(T,V) and G(T,P)G(T,P) up to functions of TT alone; recover the equation of state from each; show that S=TFS = -\partial_TF gives the known entropy.

Solution

Solution of Exercise 28.1.

F=nRTlnV+f(T)F = -nRT\ln V + f(T), G=nRTlnP+g(T)G = nRT\ln P + g(T); P=VF=nRT/VP = -\partial_VF = nRT/V, V=PG=nRT/PV = \partial_PG = nRT/P; TF=nRlnVf(T)-\partial_TF = nR\ln V - f'(T), the entropy nCVlnT+nRlnV+constnC_V\ln T + nR\ln V + \text{const} if f=nCVlnT+f' = -nC_V\ln T + \dots

Exercise 28.2

One mole of gas, 300K300\,\mathrm{K}, from 1L1\,\mathrm{L} to 10L10\,\mathrm{L} in a thermostat: ΔF\Delta F, ΔU\Delta U, ΔS\Delta S; work recovered if reversible; if against 1bar1\,\mathrm{bar}; if into vacuum; the entropy created in each case.

Solution

Solution of Exercise 28.2.

ΔF=RTln10=5.7kJ\Delta F = -RT\ln 10 = -5.7\,\mathrm{kJ}, ΔU=0\Delta U = 0, ΔS=19.1J/K\Delta S = 19.1\,\mathrm{J}/\mathrm{K}. Reversible: 5.7kJ5.7\,\mathrm{kJ}, Sc=0S_{\text{c}} = 0; against 1bar1\,\mathrm{bar}: 0.9kJ0.9\,\mathrm{kJ}, Sc=19.1900/300=16J/KS_{\text{c}} = 19.1 - 900/300 = 16\,\mathrm{J}/\mathrm{K}; vacuum: nothing, Sc=19.1J/KS_{\text{c}} = 19.1\,\mathrm{J}/\mathrm{K}.

Exercise 28.3

Water and ice at 1bar1\,\mathrm{bar}: show that gliqgice(L/Tfus)(TfusT)g_{\text{liq}} - g_{\text{ice}} \approx (L/T_{\text{fus}})(T_{\text{fus}} - T) near 0C0\,{}^{\circ}\mathrm{C} and compute it at 5-5\, and +5C+5\,{}^{\circ}\mathrm{C} (L=334kJ/kgL = 334\,\mathrm{kJ}/\mathrm{kg}). Which phase is stable in each case; is the other impossible?

Solution

Solution of Exercise 28.3.

Δg=ΔhTΔs\Delta g = \Delta h - T\Delta s with ΔhL\Delta h \approx L, ΔsL/Tfus\Delta s \approx L/T_{\text{fus}}. At 5C-5\,{}^{\circ}\mathrm{C}: gliqgice=+6.1kJ/kgg_{\text{liq}} - g_{\text{ice}} = +6.1\,\mathrm{kJ}/\mathrm{kg}, ice stable, liquid metastable (supercooling exists); at +5C+5\,{}^{\circ}\mathrm{C}: 6.1kJ/kg-6.1\,\mathrm{kJ}/\mathrm{kg}, liquid stable — superheated ice is not observed, its surface melts first.

Exercise 28.4

Clapeyron slopes of water: fusion (Δv=9.1×105m3/kg\Delta v = -9.1 \times 10^{-5}\,\mathrm{m}^{3}/\mathrm{kg}) and vaporisation at 100C100\,{}^{\circ}\mathrm{C} (L=2.26MJ/kgL = 2.26\,\mathrm{MJ}/\mathrm{kg}, Δv=1.67m3/kg\Delta v = 1.67\,\mathrm{m}^{3}/\mathrm{kg}). Melting point under 70bar70\,\mathrm{bar}; boiling point at 0.7bar0.7\,\mathrm{bar} and at 2bar2\,\mathrm{bar}.

Solution

Solution of Exercise 28.4.

Fusion 1.3×107Pa/K-1.3 \times 10^{7}\,\mathrm{Pa}/\mathrm{K}; vaporisation 3.6kPa/K3.6\,\mathrm{kPa}/\mathrm{K}. 70bar70\,\mathrm{bar}: 0.5K-0.5\,\mathrm{K}; 0.7bar0.7\,\mathrm{bar}: 92C92\,{}^{\circ}\mathrm{C}; 2bar2\,\mathrm{bar}: 127C\approx 127\,{}^{\circ}\mathrm{C} by the local slope (120C120\,{}^{\circ}\mathrm{C} in fact: the slope grows).

Exercise 28.5 ★★

Maxwell. (a) Derive the two Maxwell relations of the chapter and the two from  ⁣dU\dd U and  ⁣dH\dd H. (b) Show (U/V)T=T(P/T)VP(\partial U/\partial V)_T = T(\partial P/\partial T)_V - P; evaluate it for a perfect gas and a van der Waals gas. (c) Liquid water: α=2.1×104K1\alpha = 2.1 \times 10^{-4}\,\mathrm{K}^{-1}, κT=4.6×1010Pa1\kappa_T = 4.6 \times 10^{-10}\,\mathrm{Pa}^{-1}: pressure rise per kelvin in a rigid full vessel, and (U/V)T(\partial U/\partial V)_T. (d) A full, sealed glass bottle is warmed by 10K10\,\mathrm{K}: comment.

Solution

Solution of Exercise 28.5.

(a) Also (T/V)S=(P/S)V(\partial T/\partial V)_S = -(\partial P/\partial S)_V and (T/P)S=(V/S)P(\partial T/\partial P)_S = (\partial V/\partial S)_P. (b) 00; a/v2a/v^2. (c) α/κT=4.6bar/K\alpha/\kappa_T = 4.6\,\mathrm{bar}/\mathrm{K}; Tα/κTP1400barT\alpha/\kappa_T - P \approx 1400\,\mathrm{bar}. (d) 46bar46\,\mathrm{bar}: the bottle bursts.

Exercise 28.6 ★★

CPCVC_P - C_V. (a) Derive CPCV=TVα2/κTC_P - C_V = TV\alpha^2/\kappa_T. (b) Perfect gas. (c) Water at 300K300\,\mathrm{K}; copper (α=5×105K1\alpha = 5 \times 10^{-5}\,\mathrm{K}^{-1}, κT=7×1012Pa1\kappa_T = 7 \times 10^{-12}\,\mathrm{Pa}^{-1}, ρ=8900kg/m3\rho = 8900\,\mathrm{kg}/\mathrm{m}^{3}); compare with cPc_P (41804180\, and 385J/kg/K385\,\mathrm{J}/\mathrm{kg}/\mathrm{K}). (d) Why can one speak of “the” heat capacity of a solid?

Solution

Solution of Exercise 28.6.

(a) Theorem 28.9. (b) nRnR. (c) Water 29J/kg/K29\,\mathrm{J}/\mathrm{kg}/\mathrm{K} (0.7%0.7\%); copper 12J/kg/K12\,\mathrm{J}/\mathrm{kg}/\mathrm{K} (3%3\%). (d) The difference is negligible for condensed matter.

Exercise 28.7 ★★

Rubber. A band obeys f=CT(LL0)f = CT(L - L_0) with C=1N/m/KC = 1\,\mathrm{N}/\mathrm{m}/\mathrm{K}. (a) (S/L)T(\partial S/\partial L)_T and (U/L)T(\partial U/\partial L)_T. (b) Entropy change, heat and work when stretched isothermally at 300K300\,\mathrm{K} from L0L_0 to L0+0.1mL_0 + 0.1\,\mathrm{m}. (c) Stretched adiabatically instead (heat capacity 4J/K4\,\mathrm{J}/\mathrm{K}): temperature change. (d) Hung with a fixed weight and warmed by 30K30\,\mathrm{K}: relative change of LL0L - L_0.

Solution

Solution of Exercise 28.7.

(a) C(LL0)-C(L - L_0); 00. (b) ΔS=C(LL0)2/2=5×103J/K\Delta S = -C(L - L_0)^2/2 = -5 \times 10^{-3}\,\mathrm{J}/\mathrm{K}; Q=1.5JQ = -1.5\,\mathrm{J}; W=+1.5JW = +1.5\,\mathrm{J}. (c) +0.4K+0.4\,\mathrm{K}. (d) (LL0)1/T(L - L_0) \propto 1/T: 9%-9\%.

Exercise 28.8 ★★

Evaporation of a puddle. The chemical potential of water vapour at partial pressure pp is μv=μv(T)+RTln(p/p)\mu_{\text{v}} = \mu_{\text{v}}^\circ(T) + RT\ln(p/p^\circ), and equals that of the liquid when p=psat(T)p = p_{\text{sat}}(T). (a) Show that liquid evaporates when p<psatp < p_{\text{sat}} and vapour condenses when p>psatp > p_{\text{sat}}; define the relative humidity. (b) μliqμv\mu_{\text{liq}} - \mu_{\text{v}} at 50%50\% humidity, 293K293\,\mathrm{K}. (c) Why does washing dry even at 20C20\,{}^{\circ}\mathrm{C}, and never at 100%100\% humidity? (d) Dew: on what surfaces does it form first, and why?

Solution

Solution of Exercise 28.8.

(a) Matter goes to the lower μ\mu: μv<μliq\mu_{\text{v}} < \mu_{\text{liq}} when p<psatp < p_{\text{sat}}; humidity =p/psat= p/p_{\text{sat}}. (b) RTln0.5=1.7kJ/mol-RT\ln 0.5 = 1.7\,\mathrm{kJ}/\mathrm{mol} in favour of the vapour. (c) Evaporation needs only p<psatp < p_{\text{sat}}, not boiling; at 100%100\% the potentials are equal. (d) On the coldest surfaces, whose psat(Ts)p_{\text{sat}}(T_{\text{s}}) has dropped below the air’s pp — those radiating to the night sky.

Exercise 28.9 ★★

Van der Waals. (P+a/v2)(vb)=RT(P + a/v^2)(v - b) = RT (molar). (a) Find the critical point (vP=v2P=0\partial_vP = \partial_v^2P = 0): vc=3bv_{\text{c}} = 3b, Tc=8a/27RbT_{\text{c}} = 8a/27Rb, Pc=a/27b2P_{\text{c}} = a/27b^2. (b) Carbon dioxide, Tc=304KT_{\text{c}} = 304\,\mathrm{K}, Pc=73.8barP_{\text{c}} = 73.8\,\mathrm{bar}: aa and bb. (c) Justify Maxwell’s equal-area rule from gg. (d) Which parts of the loop are unstable, which metastable, and what phenomena show the metastable ones?

Solution

Solution of Exercise 28.9.

(a) Standard. (b) b=RTc/8Pc=4.3×105m3/molb = RT_{\text{c}}/8P_{\text{c}} = 4.3 \times 10^{-5}\,\mathrm{m}^{3}/\mathrm{mol}, a=27R2Tc2/64Pc=0.36Pam6/mol2a = 27R^2T_{\text{c}}^2/64P_{\text{c}} = 0.36\,\mathrm{Pa}\,\mathrm{m}^{6}/\mathrm{mol}^{2}. (c)  ⁣dg=v ⁣dP\dd g = v\,\dd P at fixed TT and gg equal at the two ends: v ⁣dP=0\int v\,\dd P = 0 around the loop. (d) Unstable where vP>0\partial_vP > 0; metastable between: the superheated liquid (bumping) and the supersaturated vapour (fog that waits for nuclei, cloud chamber).

Exercise 28.10 ★★★

Clausius–Clapeyron integrated. For vaporisation, neglect vliqv_{\text{liq}} and treat the vapour as perfect. (a) Show  ⁣dlnP/ ⁣dT=Lm/RT2\dd\ln P/\dd T = L_{\text{m}}/RT^2 (LmL_{\text{m}} molar) and integrate for constant LmL_{\text{m}}. (b) Water, Lm=40.7kJ/molL_{\text{m}} = 40.7\,\mathrm{kJ}/\mathrm{mol}: PsatP_{\text{sat}} at 20C20\,{}^{\circ}\mathrm{C} from the 1bar1\,\mathrm{bar} at 100C100\,{}^{\circ}\mathrm{C}; compare with the measured 23mbar23\,\mathrm{mbar}. (c) Predict the triple-point pressure (0.01C0.01\,{}^{\circ}\mathrm{C}) and compare with 611Pa611\,\mathrm{Pa}. (d) Show the same law follows from Gibbs–Helmholtz applied to Δg\Delta g.

Solution

Solution of Exercise 28.10.

(a)  ⁣dP/ ⁣dT=LmP/RT2\dd P/\dd T = L_{\text{m}}P/RT^2: ln(P/P0)=(Lm/R)(1/T1/T0)\ln(P/P_0) = -(L_{\text{m}}/R)(1/T - 1/T_0). (b) 28mbar28\,\mathrm{mbar} against 23mbar23\,\mathrm{mbar}LL is larger at 20C20\,{}^{\circ}\mathrm{C}. (c) 820Pa820\,\mathrm{Pa} against 611Pa611\,\mathrm{Pa}. (d) (Δg/T)/T=L/T2\partial(\Delta g/T)/\partial T = -L/T^2 and Δg=0\Delta g = 0 along the curve give the same slope.

Exercise 28.11 ★★★

Osmosis. A solvent’s chemical potential is lowered by a dilute solute: μ=μRTxs\mu = \mu^\circ - RTx_{\text{s}} (xsx_{\text{s}} the solute mole fraction). A membrane lets only the solvent through; pure solvent on one side, solution on the other, same TT. (a) Show that equilibrium requires an extra pressure Π\Pi on the solution with Πvm=RTxs\Pi v_{\text{m}} = RTx_{\text{s}}, i.e. Π=cRT\Pi = cRT (van ’t Hoff). (b) Sea water, c1.1mol/Lc \approx 1.1\,\mathrm{mol}/\mathrm{L} of dissolved particles, 293K293\,\mathrm{K}: Π\Pi. (c) Minimum work to extract a cubic metre of fresh water; compare with real plants (3kWh/m33\,\mathrm{kWh}/\mathrm{m}^{3}). (d) Why do plant cells burst in pure water and shrivel in brine?

Solution

Solution of Exercise 28.11.

(a) Equal μ\mu across the membrane: μ(P+Π)RTxs=μ(P)\mu^\circ(P + \Pi) - RTx_{\text{s}} = \mu^\circ(P), i.e. vmΠ=RTxsv_{\text{m}}\Pi = RTx_{\text{s}}, Π=cRT\Pi = cRT. (b) 27bar27\,\mathrm{bar}. (c) ΠV=2.7MJ=0.75kWh\Pi V = 2.7\,\mathrm{MJ} = 0.75\,\mathrm{kWh} per cubic metre; real plants four times more. (d) Water flows to the lower potential: into the solute-rich cell, out of it in brine.

Exercise 28.12 ★★★

The chain. A polymer chain of NN links of length aa: the number of configurations with end-to-end vector of length LL along the band is ΩeL2/2Na2\Omega \propto \eu^{-L^2/2Na^2} (the random walk). (a) S(L)S(L) and, at fixed UU, the tension f=TS/Lf = -T\,\partial S/\partial L. (b) The chain’s stiffness and its temperature dependence. (c) N=1000N = 1000, a=0.5nma = 0.5\,\mathrm{nm}, 300K300\,\mathrm{K}, L=10nmL = 10\,\mathrm{nm}: ff; how many chains in parallel give 30N30\,\mathrm{N}? (d) Estimate the Young’s modulus of a rubber with 102610^{26} chains per cubic metre, each of N=100N = 100.

Solution

Solution of Exercise 28.12.

(a) S=S0kBL2/2Na2S = S_0 - k_BL^2/2Na^2; f=kBTL/Na2f = k_BTL/Na^2. (b) kBT/Na2Tk_BT/Na^2 \propto T. (c) 1.7×1013N1.7 \times 10^{-13}\,\mathrm{N}; 1.8×10141.8 \times 10^{14}. (d) EnkBT0.4MPaE \sim nk_BT \approx 0.4\,\mathrm{MPa}.

28.7 Problem: The rubber band and the phase diagram of water

Problem 28.1

Weekend problem — entropy that pulls, and phases that compete

Part I — The rubber band. A band of mass 2g2\,\mathrm{g} (heat capacity 4J/K4\,\mathrm{J}/\mathrm{K}) has the tension f=CT(LL0)f = CT(L - L_0) with C=1N/m/KC = 1\,\mathrm{N}/\mathrm{m}/\mathrm{K}; at 300K300\,\mathrm{K} and LL0=0.1mL - L_0 = 0.1\,\mathrm{m}, f=30Nf = 30\,\mathrm{N}.

  1. Write  ⁣dU\dd U and  ⁣dF\dd F for the band ( ⁣dU=T ⁣dS+f ⁣dL\dd U = T\dd S + f\dd L).
  2. Derive the Maxwell relation (S/L)T=(f/T)L(\partial S/\partial L)_T = -(\partial f/\partial T)_L.
  3. Show that (U/L)T=0(\partial U/\partial L)_T = 0 for this band: what does it mean?
  4. Isothermal stretching from L0L_0 to L0+0.1mL_0 + 0.1\,\mathrm{m} at 300K300\,\mathrm{K}: ΔS\Delta S, heat QQ, work WW; check ΔU=0\Delta U = 0.
  5. Same stretching done adiabatically: temperature change.
  6. The band holds a fixed weight; it is warmed by 30K30\,\mathrm{K}: new LL0L - L_0. Describe the “rubber engine” (a wheel with rubber spokes heated on one side).
  7. A chain of NN links of length aa has ΩeL2/2Na2\Omega \propto \eu^{-L^2/2Na^2}: S(L)S(L) and f(L,T)f(L,T); why does the stiffness grow with TT?
  8. N=1000N = 1000, a=0.5nma = 0.5\,\mathrm{nm}, L=10nmL = 10\,\mathrm{nm}, 300K300\,\mathrm{K}: ff for one chain and the number of chains for 30N30\,\mathrm{N}.
  9. Why does a steel spring behave oppositely (tension falling with TT at fixed length)?

Part II — The phase diagram of water. Data: Lfus=334kJ/kgL_{\text{fus}} = 334\,\mathrm{kJ}/\mathrm{kg}, vice=1.091×103m3/kgv_{\text{ice}} = 1.091 \times 10^{-3}\,\mathrm{m}^{3}/\mathrm{kg}, vliq=1.000×103m3/kgv_{\text{liq}} = 1.000 \times 10^{-3}\,\mathrm{m}^{3}/\mathrm{kg}; Lvap=2.26MJ/kgL_{\text{vap}} = 2.26\,\mathrm{MJ}/\mathrm{kg} at 100C100\,{}^{\circ}\mathrm{C}, vvap=1.67m3/kgv_{\text{vap}} = 1.67\,\mathrm{m}^{3}/\mathrm{kg}; Lm=40.7kJ/molL_{\text{m}} = 40.7\,\mathrm{kJ}/\mathrm{mol}; triple point 0.01C0.01\,{}^{\circ}\mathrm{C}, 611Pa611\,\mathrm{Pa}; critical point 647K647\,\mathrm{K}, 221bar221\,\mathrm{bar}.

  1. Sketch g(T)g(T) for ice, liquid and vapour at 1bar1\,\mathrm{bar}; justify the order of the slopes and locate the transitions.
  2. Derive Clapeyron’s formula from g1=g2g_1 = g_2.
  3. Slope of the fusion curve; its sign, and why it is unusual.
  4. A skater: 700N700\,\mathrm{N} on 1cm21\,\mathrm{cm}^{2}: change of the melting point; conclude about the popular explanation of skating.
  5. Under 3km3\,\mathrm{km} of ice (ρ=917kg/m3\rho = 917\,\mathrm{kg}/\mathrm{m}^{3}): pressure and melting point; consequence for the ice sheet.
  6. Slope of the vaporisation curve at 100C100\,{}^{\circ}\mathrm{C}; boiling point at 0.7bar0.7\,\mathrm{bar} and at 2bar2\,\mathrm{bar}.
  7. Integrate Clausius–Clapeyron with a perfect vapour and constant LmL_{\text{m}}; PsatP_{\text{sat}} at 20C20\,{}^{\circ}\mathrm{C} and at the triple point; comment on the accuracy.
  8. At the triple point, compare the slopes of the sublimation and vaporisation curves (Lsub=Lfus+LvapL_{\text{sub}} = L_{\text{fus}} + L_{\text{vap}}).
  9. Supercooled water at 10C-10\,{}^{\circ}\mathrm{C}: gliqgiceg_{\text{liq}} - g_{\text{ice}}; why can cloud droplets stay liquid to 40C-40\,{}^{\circ}\mathrm{C}?
  10. What happens to Δv\Delta v, LL and the slope at the critical point; what is a supercritical fluid?

Part III — Applications.

  1. Explain Maxwell’s equal-area construction on a van der Waals isotherm from the continuity of gg.
  2. Superheated water in a microwave “bumps”: which branch of the isotherm, and why the danger?
  3. Freeze-drying: describe the path in the (P,T)(P,T) diagram and why the water leaves without melting.
  4. Why does a dish of water evaporate at 20C20\,{}^{\circ}\mathrm{C} in dry air and stop in saturated air — in terms of chemical potentials?
  5. A pressure cooker at 2bar2\,\mathrm{bar}: why does food cook so much faster (the rate of the chemistry roughly doubles every 10K10\,\mathrm{K})?
  6. Summarise: which potential for which constraint, and what the Maxwell relations buy.
Solution

Solution of Problem 28.1.

1.  ⁣dU=T ⁣dS+f ⁣dL\dd U = T\dd S + f\dd L;  ⁣dF=S ⁣dT+f ⁣dL\dd F = -S\dd T + f\dd L.

2. Schwarz on  ⁣dF\dd F.

3. fTTf=CT(LL0)CT(LL0)=0f - T\partial_Tf = CT(L - L_0) - CT(L - L_0) = 0: the energy does not change; the pull is entropic.

4. ΔS=5×103J/K\Delta S = -5 \times 10^{-3}\,\mathrm{J}/\mathrm{K}; Q=1.5JQ = -1.5\,\mathrm{J}; W=+1.5JW = +1.5\,\mathrm{J}; sum zero.

5. +0.4K+0.4\,\mathrm{K}.

6. LL01/TL - L_0 \propto 1/T: 9.1cm9.1\,\mathrm{cm}, a contraction of 9mm9\,\mathrm{mm}; the heated spokes shorten, the rim’s centre of mass shifts, the wheel turns.

7. S=S0kBL2/2Na2S = S_0 - k_BL^2/2Na^2; f=kBTL/Na2f = k_BTL/Na^2; the entropy penalty is paid in kBTk_BT.

8. 1.7×1013N1.7 \times 10^{-13}\,\mathrm{N}; 1.8×10141.8 \times 10^{14} chains.

9. Its force is energetic (LU0\partial_LU \ne 0); warming softens the bonds, so ff falls with TT.

10. Slopes s-s, with sgas>sliq>sices_{\text{gas}} > s_{\text{liq}} > s_{\text{ice}}; the lowest line is the stable phase; crossings at TfusT_{\text{fus}} and TvapT_{\text{vap}}.

11. Theorem 28.12.

12. 1.3×107Pa/K-1.3 \times 10^{7}\,\mathrm{Pa}/\mathrm{K}; negative because vliq<vicev_{\text{liq}} < v_{\text{ice}}.

13. 70bar70\,\mathrm{bar}: 0.5K-0.5\,\mathrm{K} — not how one skates at 10C-10\,{}^{\circ}\mathrm{C}; friction and the liquid-like surface layer do it.

14. 270bar270\,\mathrm{bar}, 2K-2\,\mathrm{K}: with the geothermal flux, the base melts and the sheet slides.

15. 3.6kPa/K3.6\,\mathrm{kPa}/\mathrm{K}; 92C92\,{}^{\circ}\mathrm{C}; about 127C127\,{}^{\circ}\mathrm{C} (120120\, in fact).

16. 28mbar28\,\mathrm{mbar} (2323\,), 820Pa820\,\mathrm{Pa} (611611\,): LL grows as TT falls; errors of 202030%30\%.

17. Same Δv\Delta v, so the ratio of slopes is Lsub/Lvap=1.15L_{\text{sub}}/L_{\text{vap}} = 1.15: the sublimation curve is steeper — a kink at the triple point.

18. 12kJ/kg12\,\mathrm{kJ}/\mathrm{kg}; ice must nucleate, and a small nucleus costs more surface energy than it gains: pure droplets wait, down to 40C-40\,{}^{\circ}\mathrm{C}.

19. Δv0\Delta v \to 0, L0L \to 0, their ratio finite: the curve ends; beyond, one fluid passing continuously from liquid-like to gas-like.

20.  ⁣dg=v ⁣dP\dd g = v\,\dd P at fixed TT; gg equal at the two ends of the horizontal: v ⁣dP=0\int v\,\dd P = 0, equal areas.

21. The superheated-liquid branch: no bubble nucleus in a smooth cup; a disturbance boils it at once.

22. Freeze, pump below 611Pa611\,\mathrm{Pa}, warm gently: the path crosses the sublimation curve, never the fusion curve; the structure is preserved.

23. μv(p)<μliq\mu_{\text{v}}(p) < \mu_{\text{liq}} when p<psatp < p_{\text{sat}}; equal at saturation.

24. 120C120\,{}^{\circ}\mathrm{C} instead of 100100\,: four times faster.

25. SS for isolated, FF for fixed T,VT,V, GG for fixed T,PT,P; ΔF-\Delta F, ΔG-\Delta G the recoverable work; the Maxwell relations turn derivatives of SS into the equation of state.

Terms defined in this chapter

See all 393 terms in the glossary