Physics · Book 3 · Bachelor Year 1

University Physics — Year 1

University Physics — Year 1 · Bachelor Year 1

25Phase Changes of a Pure Substance

Water is the one substance everybody has seen in all three states, and it is the working fluid of most of the world’s power stations, the refrigerant of the first ice machines, and the engine of the weather. Ice melts at a temperature that does not budge while the heat pours in; a kettle boils at 100C100{}^{\circ}\mathrm{C} at the seaside and at 70C70{}^{\circ}\mathrm{C} on Everest; a sealed bottle of very cold water freezes solid at a tap. This chapter draws the map of the phases of a pure substance — the (T,P)(T, P) and (v,P)(v, P) diagrams — and gives the three tools that go with it: the lever rule (how much of each phase), the latent heat (what a change costs, in energy and in entropy) and the Clausius–Clapeyron relation (how the boundary lines slope). It ends where the map fails: metastable states, which are where the weather and the pressure cooker’s surprises come from.

25.1 Phases and the (T,P)(T, P) diagram

Definition 25.1 (Pure substance, phase, phase change)

A pure substance is a body of a single chemical species. A phase is a part of it that is homogeneous in its physical properties: solid, liquid, gas (vapour when it coexists with its liquid). A phase change (melting/solidification, vaporization/ condensation, sublimation/deposition) is the passage from one phase to another; at fixed pressure it occurs at a fixed temperature, with heat exchanged but no temperature change: the latent heat.

Proposition 25.2 (Equilibrium diagram)

In the (T,P)(T, P) plane each phase occupies a region; two phases coexist only along a curve (sublimation, fusion, vaporization), all three only at one point, the triple point. The vaporization curve P=Ps(T)P = P_s(T) — the saturation vapour pressure — ends at the critical point (Tc,Pc)(T_c, P_c), beyond which liquid and gas are no longer distinct. For water: triple point 273.16K273.16\,\mathrm{K}, 611Pa611\,\mathrm{Pa}; critical point 647K647\,\mathrm{K}, 221bar221\,\mathrm{bar}. The fusion curve of water leans to the left (ice is less dense than water); for almost every other substance it leans to the right.

Proof. Admitted at this level.

The phase diagram of water (not to scale). Heating at atmospheric pressure follows the dashed isobar: ice melts where it crosses the fusion curve, water boils where it crosses the vaporization curve. The fusion curve of water leans left: pressure lowers its melting point.
The phase diagram of water (not to scale). Heating at atmospheric pressure follows the dashed isobar: ice melts where it crosses the fusion curve, water boils where it crosses the vaporization curve. The fusion curve of water leans left: pressure lowers its melting point.

Remark 25.3 (Boiling, evaporation and the pressure cooker)

A liquid evaporates at any temperature from its surface, as long as the partial pressure of its vapour above it is below Ps(T)P_s(T); it boils when Ps(T)P_s(T) reaches the ambient pressure, so that bubbles of vapour can grow inside it. Water boils at 100C100{}^{\circ}\mathrm{C} because Ps(100C)=1.013barP_s(100{}^{\circ}\mathrm{C}) = 1.013\,\mathrm{bar}; at 0.33bar0.33\,\mathrm{bar} on Everest it boils near 70C70{}^{\circ}\mathrm{C}, in a pressure cooker at 1.8bar1.8\,\mathrm{bar} near 117C117{}^{\circ}\mathrm{C}. The temperature of a boiling liquid is pinned by the pressure — a fact used to define the Celsius scale for two centuries.

25.2 The (v,P)(v, P) diagram and the lever rule

Proposition 25.4 (Andrews isotherms)

In the Clapeyron plane (v,P)(v, P) of the specific volume, an isotherm T<TcT < T_c has three parts: a steep branch (liquid, almost incompressible), a horizontal plateau at P=Ps(T)P = P_s(T) where liquid and vapour coexist, and a hyperbola-like branch (vapour). The plateau ends are the specific volumes vl(T)v_l(T) and vv(T)v_v(T) of the saturated liquid and vapour; their locus is the saturation curve (the dome), whose summit is the critical point, where the isotherm TcT_c has a horizontal inflection. Above TcT_c no plateau exists.

Proof. Admitted at this level.

Theorem 25.5 (Lever rule)

A mass mm of specific volume vv on the plateau at TT splits into a vapour mass fraction x=mv/mx = m_v/m (the quality) and a liquid fraction 1x1 - x with

v=(1x)vl+xvv,i.e.x=vvlvvvl=LMLV,v = (1 - x)v_l + x\,v_v , \qquad\text{i.e.}\qquad x = \frac{v - v_l}{v_v - v_l} = \frac{LM}{LV} ,

the ratio of the segments cut on the plateau by the state point MM. The same rule holds for every extensive quantity per unit mass (uu, hh, ss): h=(1x)hl+xhvh = (1 - x)h_l + xh_v.

Proof. Volumes add: V=mlvl+mvvvV = m_lv_l + m_vv_v; divide by mm. Energy, enthalpy and entropy are extensive as well.

Andrews isotherms in the Clapeyron diagram. Under the dome the isotherm T_1 is a plateau at P_s(T_1); a state M on it is a mixture whose vapour fraction x is the ratio LM/LV. The critical isotherm touches the dome at its summit with a horizontal inflection; above T_c there is no plateau and no distinction between liquid and gas.
Andrews isotherms in the Clapeyron diagram. Under the dome the isotherm T1T_1 is a plateau at Ps(T1)P_s(T_1); a state MM on it is a mixture whose vapour fraction xx is the ratio LM/LVLM/LV. The critical isotherm touches the dome at its summit with a horizontal inflection; above TcT_c there is no plateau and no distinction between liquid and gas.

Example 25.6 (A kettle and a boiler)

Water at 100C100{}^{\circ}\mathrm{C}, 1atm1\,\mathrm{atm}: vl=1.04×103m3/kgv_l = 1.04 \times 10^{-3}\,\mathrm{m}^{3}/\mathrm{kg}, vv=1.67m3/kgv_v = 1.67\,\mathrm{m}^{3}/\mathrm{kg} — a ratio of 16001600. A closed 1.0L1.0\,\mathrm{L} vessel holding 0.50kg0.50\,\mathrm{kg} of water at that temperature has v=2.0×103m3/kgv = 2.0 \times 10^{-3}\,\mathrm{m}^{3}/\mathrm{kg} and x=(2.01.04)×103/1.67=5.8×104x = (2.0 - 1.04) \times 10^{-3}/1.67 = 5.8 \times 10^{-4}: 0.29g0.29\,\mathrm{g} of vapour occupying half the vessel. Doubling the vapour mass in a sealed vessel barely moves the state point; the pressure is fixed by the temperature alone.

25.3 Energetics of a phase change

Proposition 25.7 (Latent heat, enthalpy and entropy of transition)

At the temperature TT and pressure Ps(T)P_s(T) of coexistence, the transition of unit mass from phase 1 to phase 2 is reversible, isothermal and isobaric, and

L12(T)=h2h1,s2s1=L12T,u2u1=L12Ps(v2v1).L_{12}(T) = h_2 - h_1 , \qquad s_2 - s_1 = \frac{L_{12}}{T} , \qquad u_2 - u_1 = L_{12} - P_s(v_2 - v_1) .

L12>0L_{12} > 0 when going toward the less ordered phase (fusion, vaporization, sublimation), and L21=L12L_{21} = -L_{12}. For water at 1atm1\,\mathrm{atm}: Lf=334kJ/kgL_f = 334\,\mathrm{kJ}/\mathrm{kg} at 0C0{}^{\circ}\mathrm{C}, Lv=2257kJ/kgL_v = 2257\,\mathrm{kJ}/\mathrm{kg} at 100C100{}^{\circ}\mathrm{C}.

Proof. At constant pressure the heat received is ΔH\Delta H (Proposition 22.7); reversible and isothermal, it is TΔST\Delta S (Proposition 23.3); and U=HPVU = H - PV.

Example 25.8 (Where the heat of vaporization goes)

For water at 100C100{}^{\circ}\mathrm{C}: Ps(vvvl)=1.013×105×1.67=169kJ/kgP_s(v_v - v_l) = 1.013 \times 10^5 \times 1.67 = 169\,\mathrm{kJ}/\mathrm{kg}, so uvul=2257169=2088kJ/kgu_v - u_l = 2257 - 169 = 2088\,\mathrm{kJ}/\mathrm{kg}: 93%93\% of the latent heat goes into tearing the molecules apart, 7%7\% into pushing the atmosphere back. The entropy of vaporization, 2257/373=6.05kJ/(kgK)2257/373 = 6.05\,\mathrm{kJ}/(\mathrm{kg}\,\mathrm{K}), dwarfs that of fusion, 334/273=1.22kJ/(kgK)334/273 = 1.22\,\mathrm{kJ}/(\mathrm{kg}\,\mathrm{K}): melting loosens the molecules, boiling frees them.

Method 25.9 (Calorimetry with phase changes)

In an insulated vessel at constant pressure, ΔHi=0\sum\Delta H_i = 0. Guess the final state (which phases are present, at what temperature); write each body’s ΔH\Delta H as sensible heats mcΔTmc\,\Delta T plus latent heats ±mL\pm mL for the changes it undergoes; solve; check the guess: a body ending above its boiling point or below its melting point, or a negative mass of a phase, means the guess was wrong — the final state is then a mixture at the transition temperature, and the unknown becomes the mass transformed (Example 22.13).

Example 25.10 (Steam burns)

10g10\,\mathrm{g} of steam at 100C100{}^{\circ}\mathrm{C} condensing on skin gives 0.010×2257=22.6kJ0.010 \times 2257 = 22.6\,\mathrm{kJ} before it has cooled one degree — as much as 10g10\,\mathrm{g} of boiling water gives in cooling by 540K540\,\mathrm{K}. This is why steam scalds so much worse than water at the same temperature, and why a steam radiator needs so little mass flow.

The same dome in the entropy diagram. An isobar crosses it as a horizontal segment of length L_v/T; the area under the segment is the latent heat. Power-station cycles are drawn in this plane, and the quality at the turbine exit is read off the segment by the lever rule.
The same dome in the entropy diagram. An isobar crosses it as a horizontal segment of length Lv/TL_v/T; the area under the segment is the latent heat. Power-station cycles are drawn in this plane, and the quality at the turbine exit is read off the segment by the lever rule.

25.4 The Clausius–Clapeyron relation

Theorem 25.11 (Clausius–Clapeyron)

Along a coexistence curve of phases 1 and 2,

 ⁣dPs ⁣dT=L12(T)T(v2v1).\frac{\dd P_s}{\dd T} = \frac{L_{12}(T)}{T\,(v_2 - v_1)} .

Proof. Take unit mass round an infinitesimal Carnot cycle inside the dome: complete transition 121 \to 2 along the plateau at T+ ⁣dTT + \dd T, pressure Ps+ ⁣dPsP_s + \dd P_s (heat received L12L_{12} to first order); an infinitesimal adiabatic step down to TT; the reverse transition along the plateau at TT, PsP_s; an adiabatic step back. The cycle is reversible, ditherm between T+ ⁣dTT + \dd T and TT, so its efficiency is  ⁣dT/T\dd T/T (Theorem 24.5); its work, the area of the thin rectangle, is  ⁣dPs(v2v1)\dd P_s\,(v_2 - v_1). Hence  ⁣dPs(v2v1)/L12= ⁣dT/T\dd P_s\,(v_2 - v_1)/L_{12} = \dd T/T.

The infinitesimal Carnot cycle that proves the Clausius–Clapeyron relation: two plateaus T apart, joined by adiabatic steps too short to draw; Carnot’s theorem equates the ratio of its area to the heat received with T/T.
The infinitesimal Carnot cycle that proves the Clausius–Clapeyron relation: two plateaus  ⁣dT\dd T apart, joined by adiabatic steps too short to draw; Carnot’s theorem equates the ratio of its area to the heat received with  ⁣dT/T\dd T/T.

Corollary 25.12 (Saturation vapour pressure of a liquid)

If the vapour is a perfect gas and vvvlv_v \gg v_l, so that vvvlRT/(MPs)v_v - v_l \approx RT/(MP_s), and if LvL_v varies little,

 ⁣dPsPs=MLvR ⁣dTT2,lnPs(T)Ps(T0)=MLvR(1T01T):\frac{\dd P_s}{P_s} = \frac{ML_v}{R}\,\frac{\dd T}{T^2} , \qquad \ln\frac{P_s(T)}{P_s(T_0)} = \frac{ML_v}{R}\Bigl(\frac{1}{T_0} - \frac{1}{T}\Bigr) :

the vapour pressure rises roughly exponentially with temperature. For water near 100C100{}^{\circ}\mathrm{C}, MLv/R=0.018×2.257×106/8.314=4890KML_v/R = 0.018 \times 2.257 \times 10^6/ 8.314 = 4890\,\mathrm{K} and  ⁣dPs/ ⁣dT=2.257×106/(373×1.67)=3.6kPa/K\dd P_s/\dd T = 2.257 \times 10^6/(373 \times 1.67) = 3.6\,\mathrm{kPa}/\mathrm{K}: each kelvin of extra boiling temperature costs 36mbar36\,\mathrm{mbar} of extra pressure.

Proof. Substitute vvvlRT/(MPs)v_v - v_l \approx RT/(MP_s) in the theorem and separate variables; integrate with LvL_v constant.

The saturation vapour pressure of water. The curve is close to an exponential in -1/T; the boiling temperature is where it crosses the ambient pressure.
The saturation vapour pressure of water. The curve is close to an exponential in 1/T-1/T; the boiling temperature is where it crosses the ambient pressure.

Example 25.13 (Ice under a skate)

For ice–water, Lf=334kJ/kgL_f = 334\,\mathrm{kJ}/\mathrm{kg} and vlvs=(1.0001.091)×103=9.1×105m3/kgv_l - v_s = (1.000 - 1.091) \times 10^{-3} = -9.1 \times 10^{-5}\,\mathrm{m}^{3}/\mathrm{kg}:  ⁣dP/ ⁣dT=3.34×105/(273×(9.1×105))=1.3×107Pa/K=130bar/K\dd P/\dd T = 3.34 \times 10^5/(273 \times (-9.1 \times 10^{-5})) = -1.3 \times 10^{7}\,\mathrm{Pa}/\mathrm{K} = -130\,\mathrm{bar}/\mathrm{K}. A 70kg70\,\mathrm{kg} skater on one blade of 30cm30\,\mathrm{cm} by 3mm3\,\mathrm{mm} (9cm29\,\mathrm{cm}^{2}) exerts about 8bar8\,\mathrm{bar}, lowering the melting point by 0.06K0.06\,\mathrm{K} — pressure melting is not why skates glide (a thin surface layer of ice is liquid-like on its own, and friction heats); but the negative slope is real, and it is why a wire loaded with weights cuts through a block of ice that refreezes behind it.

25.5 Metastable states

Definition 25.14 (Supercooling, superheating)

A phase can persist beyond its equilibrium boundary: liquid water cooled below 0C0{}^{\circ}\mathrm{C} without freezing (supercooling), heated above its boiling point without boiling (superheating), vapour compressed beyond PsP_s without condensing (supersaturation). Such metastable states require the absence of nucleation sites — dust, scratches, dissolved gas, ice crystals — on which the new phase can start; a disturbance tips them suddenly and irreversibly to equilibrium.

Example 25.15 (The supercooled bottle)

Still water at 8C-8{}^{\circ}\mathrm{C} in a clean bottle, knocked: ice crystals shoot through it and the temperature jumps to 0C0{}^{\circ}\mathrm{C}. The process is adiabatic and fast, so the sensible heat cΔTc\,\Delta T freezes a fraction x=cΔT/Lf=4.18×8/334=0.10x = c\,\Delta T/L_f = 4.18 \times 8/334 = 0.10 of the water; the entropy created, cln(273/265)xLf/273=124122=+2J/(kgK)c\ln(273/265) - xL_f/273 = 124 - 122 = +2\,\mathrm{J}/(\mathrm{kg}\,\mathrm{K}), is positive as it must be. Clouds are full of supercooled droplets down to 40C-40{}^{\circ}\mathrm{C}; aircraft icing and the seeding of clouds both exploit that.

Remark 25.16 (Boiling chips and bubble chambers)

A bubble of radius rr in a liquid at pressure PP holds vapour at P+2σ/rP + 2\sigma/r (surface tension σ\sigma, Year 2 volume); it can only grow if Ps(T)>P+2σ/rP_s(T) > P + 2\sigma/r, so a clean liquid at its boiling point has no bubble small enough to start and superheats by several kelvin before erupting — the “bumping” that boiling chips prevent by offering cavities full of trapped gas. The bubble chamber of particle physics ran on the same instability in reverse: a superheated liquid boils first along the track of an ionizing particle.

Example 25.17 (Humidity and dew)

Air holds water vapour at a partial pressure PvPs(T)P_v \leq P_s(T); the relative humidity is Pv/Ps(T)P_v/P_s(T), the dew point the temperature at which PsP_s falls to PvP_v. Air at 25C25{}^{\circ}\mathrm{C} (Ps=3.17kPaP_s = 3.17\,\mathrm{kPa}) and 60%60\% humidity has Pv=1.9kPaP_v = 1.9\,\mathrm{kPa}, ρv=PvM/(RT)=14g/m3\rho_v = P_vM/(RT) = 14\,\mathrm{g}/\mathrm{m}^{3}, and dews on any surface below about 17C17{}^{\circ}\mathrm{C} — the grass at dawn, the cold bottle, the bathroom mirror. Lifted, the same air cools adiabatically at 9.8K/km9.8\,\mathrm{K}/\mathrm{km} (Problem 25.1) and reaches its dew point a kilometre or so up: that is where the flat bottoms of the cumulus are.

25.6 Exercises

Exercise 25.1

Using the diagram of the course, give the phase of water (a) at 20C20{}^{\circ}\mathrm{C} under 0.5kPa0.5\,\mathrm{kPa}; (b) at 5C-5{}^{\circ}\mathrm{C} under 1bar1\,\mathrm{bar}; (c) at 400C400{}^{\circ}\mathrm{C} under 200bar200\,\mathrm{bar}; (d) at 0.01C0.01{}^{\circ}\mathrm{C} under 611Pa611\,\mathrm{Pa}. Why does a puddle dry at 20C20{}^{\circ}\mathrm{C} although water “boils at 100”?

Solution

Solution of Exercise 25.1.

(a) Vapour: 0.5kPa0.5\,\mathrm{kPa} is below Ps(20C)=2.3kPaP_s(20{}^{\circ}\mathrm{C}) = 2.3\,\mathrm{kPa}. (b) Solid. (c) Above Tc=374CT_c = 374{}^{\circ}\mathrm{C}: supercritical fluid, no liquid–gas distinction. (d) The triple point: all three. The puddle evaporates from its surface as long as the vapour pressure in the air is below Ps(20C)P_s(20{}^{\circ}\mathrm{C}); boiling is only the case where bubbles can form inside the liquid.

Exercise 25.2

100g100\,\mathrm{g} of steam at 100C100{}^{\circ}\mathrm{C} are bubbled into 1.0kg1.0\,\mathrm{kg} of water at 20C20{}^{\circ}\mathrm{C} in an insulated vessel. Final temperature (Lv=2257kJ/kgL_v = 2257\,\mathrm{kJ}/\mathrm{kg}, c=4.18kJ/(kgK)c = 4.18\,\mathrm{kJ}/(\mathrm{kg}\,\mathrm{K})). Compare with adding 100g100\,\mathrm{g} of water at 100C100{}^{\circ}\mathrm{C}.

Solution

Solution of Exercise 25.2.

0.1×2257+0.1×4.18(100Tf)=1.0×4.18(Tf20)0.1 \times 2257 + 0.1 \times 4.18\,(100 - T_f) = 1.0 \times 4.18\,(T_f - 20): 351.1=4.60Tf351.1 = 4.60\,T_f, Tf=76CT_f = 76{}^{\circ}\mathrm{C}. With hot water instead: 100Tf=10(Tf20)100 - T_f = 10(T_f - 20), Tf=27CT_f = 27{}^{\circ}\mathrm{C} — the latent heat is worth 540K540\,\mathrm{K} of sensible heat.

Exercise 25.3

A rigid 2.0L2.0\,\mathrm{L} vessel contains 1.0kg1.0\,\mathrm{kg} of water at 150C150{}^{\circ}\mathrm{C} in liquid–vapour equilibrium (Ps=4.76barP_s = 4.76\,\mathrm{bar}, vl=1.09×103m3/kgv_l = 1.09 \times 10^{-3}\,\mathrm{m}^{3}/\mathrm{kg}, vv=0.393m3/kgv_v = 0.393\,\mathrm{m}^{3}/\mathrm{kg}). Quality, mass of vapour, volume occupied by the liquid.

Solution

Solution of Exercise 25.3.

v=2.0×103m3/kgv = 2.0 \times 10^{-3}\,\mathrm{m}^{3}/\mathrm{kg}; x=(2.01.09)×103/0.392=2.3×103x = (2.0 - 1.09) \times 10^{-3}/0.392 = 2.3 \times 10^{-3}: 2.3g2.3\,\mathrm{g} of vapour filling 0.91L0.91\,\mathrm{L}; the 0.998kg0.998\,\mathrm{kg} of liquid occupy 0.998×1.09=1.09L0.998 \times 1.09 = 1.09\,\mathrm{L}.

Exercise 25.4

Entropy of vaporization of water at 100C100{}^{\circ}\mathrm{C}, per kilogram and per mole; entropy of fusion per mole at 0C0{}^{\circ}\mathrm{C}. Many ordinary liquids have a molar entropy of vaporization near 88J/(molK)88\,\mathrm{J}/(\mathrm{mol}\,\mathrm{K}) (Trouton’s rule): is water ordinary?

Solution

Solution of Exercise 25.4.

2257/373=6.05kJ/(kgK)2257/373 = 6.05\,\mathrm{kJ}/(\mathrm{kg}\,\mathrm{K}), i.e. ×0.018=109J/(molK)\times 0.018 = 109\,\mathrm{J}/(\mathrm{mol}\,\mathrm{K}); fusion 334/273×0.018=22J/(molK)334/273 \times 0.018 = 22\,\mathrm{J}/(\mathrm{mol}\,\mathrm{K}). Water’s 109109 is well above Trouton’s 8888: hydrogen bonds make liquid water more ordered than an ordinary liquid, so vaporizing it gains more disorder.

Exercise 25.5 ★★

Boiling temperature of water on the summit of Everest, P=0.33barP = 0.33\,\mathrm{bar}, from Corollary 25.12 with MLv/R=4890KML_v/R = 4890\,\mathrm{K}; and at 2000m2000\,\mathrm{m} (P=0.80barP = 0.80\,\mathrm{bar}). What becomes of a 3min3\,\mathrm{min} egg?

Solution

Solution of Exercise 25.5.

1/T=1/373.15ln(P/P0)/48901/T = 1/373.15 - \ln(P/P_0)/4890. Everest: ln(0.33/1.013)=1.12\ln(0.33/1.013) = -1.12, 1/T=2.680×103+2.29×1041/T = 2.680 \times 10^{-3} + 2.29 \times 10^{-4}, T=344K=71CT = 344\,\mathrm{K} = 71{}^{\circ}\mathrm{C}. At 0.80bar0.80\,\mathrm{bar}: ln=0.236\ln = -0.236, T=366K=93CT = 366\,\mathrm{K} = 93{}^{\circ}\mathrm{C}. At 71C71{}^{\circ}\mathrm{C} the white sets slowly and the yolk hardly at all: the 3min3\,\mathrm{min} egg becomes a 10min10\,\mathrm{min} egg or more.

Exercise 25.6 ★★

Temperature inside a pressure cooker whose valve opens at 1.8bar1.8\,\mathrm{bar} absolute; the same if its valve were set at 2.5bar2.5\,\mathrm{bar}. Steam at 1.8bar1.8\,\mathrm{bar} has vv=0.98m3/kgv_v = 0.98\,\mathrm{m}^{3}/\mathrm{kg}: how many grams of steam does a 6L6\,\mathrm{L} cooker contain above 4L4\,\mathrm{L} of water?

Solution

Solution of Exercise 25.6.

ln(1.8/1.013)=0.575\ln(1.8/1.013) = 0.575: 1/T=2.680×1031.18×1041/T = 2.680 \times 10^{-3} - 1.18 \times 10^{-4}, T=390K=117CT = 390\,\mathrm{K} = 117{}^{\circ}\mathrm{C}; at 2.5bar2.5\,\mathrm{bar}: ln=0.903\ln = 0.903, T=401K=128CT = 401\,\mathrm{K} = 128{}^{\circ}\mathrm{C}. Steam: 2L/0.98=2.0g2\,\mathrm{L}/0.98 = 2.0\,\mathrm{g} — the cooker holds almost nothing but water and a little steam.

Exercise 25.7 ★★

Slope of the fusion curve of water at 0C0{}^{\circ}\mathrm{C} (Lf=334kJ/kgL_f = 334\,\mathrm{kJ}/\mathrm{kg}, vs=1.091×103m3/kgv_s = 1.091 \times 10^{-3}\,\mathrm{m}^{3}/\mathrm{kg}, vl=1.000×103m3/kgv_l = 1.000 \times 10^{-3}\,\mathrm{m}^{3}/\mathrm{kg}). At what pressure does ice melt at 1C-1{}^{\circ}\mathrm{C}? Ice at the bottom of a 3km3\,\mathrm{km} ice sheet (ρ=917kg/m3\rho = 917\,\mathrm{kg}/\mathrm{m}^{3}): melting temperature there, and a consequence for glacier flow.

Solution

Solution of Exercise 25.7.

 ⁣dP/ ⁣dT=3.34×105/[273×(9.1×105)]=1.3×107Pa/K=130bar/K\dd P/\dd T = 3.34 \times 10^5/[273 \times (-9.1 \times 10^{-5})] = -1.3 \times 10^{7}\,\mathrm{Pa}/\mathrm{K} = -130\,\mathrm{bar}/\mathrm{K}: ice melts at 1C-1{}^{\circ}\mathrm{C} under about 130bar130\,\mathrm{bar}. Under 3km3\,\mathrm{km} of ice, P=917×9.8×3000=270barP = 917 \times 9.8 \times 3000 = 270\,\mathrm{bar}: melting at 2C-2{}^{\circ}\mathrm{C}; a glacier bed can be at its melting point while the surface is far colder, and the film of meltwater lets the ice sheet slide.

Exercise 25.8 ★★

One kilogram of water boils away at 100C100{}^{\circ}\mathrm{C} under 1atm1\,\mathrm{atm} (vv=1.673m3/kgv_v = 1.673\,\mathrm{m}^{3}/\mathrm{kg}, vl=1.04×103m3/kgv_l = 1.04 \times 10^{-3}\,\mathrm{m}^{3}/\mathrm{kg}). Work received, heat received, ΔU\Delta U, ΔH\Delta H, ΔS\Delta S of the water; entropy created if the heat comes from a flame at 1500K1500\,\mathrm{K}.

Solution

Solution of Exercise 25.8.

W=P(vvvl)=1.013×105×1.672=169kJW = -P(v_v - v_l) = -1.013 \times 10^5 \times 1.672 = -169\,\mathrm{kJ} (the water pushes the atmosphere back); Q=Lv=2257kJQ = L_v = 2257\,\mathrm{kJ}; ΔU=2257169=2088kJ\Delta U = 2257 - 169 = 2088\,\mathrm{kJ}; ΔH=2257kJ\Delta H = 2257\,\mathrm{kJ}; ΔS=2257/373=6.05kJ/K\Delta S = 2257/373 = 6.05\,\mathrm{kJ}/\mathrm{K}. From a flame at 1500K1500\,\mathrm{K}: Sexch=2257/1500=1.50kJ/KS_{\mathrm{exch}} = 2257/1500 = 1.50\,\mathrm{kJ}/\mathrm{K}, created 4.5kJ/K4.5\,\mathrm{kJ}/\mathrm{K} — most of the flame’s quality is wasted heating water.

Exercise 25.9 ★★

Saturation pressures: 1.23kPa1.23\,\mathrm{kPa} (10C10{}^{\circ}\mathrm{C}), 1.70kPa1.70\,\mathrm{kPa} (15C15{}^{\circ}\mathrm{C}), 2.34kPa2.34\,\mathrm{kPa} (20C20{}^{\circ}\mathrm{C}), 3.17kPa3.17\,\mathrm{kPa} (25C25{}^{\circ}\mathrm{C}), 4.24kPa4.24\,\mathrm{kPa} (30C30{}^{\circ}\mathrm{C}). A room at 22C22{}^{\circ}\mathrm{C} has a relative humidity of 70%70\%: vapour pressure, dew point (interpolate), mass of water vapour in 50m350\,\mathrm{m}^{3}. A window pane at 12C12{}^{\circ}\mathrm{C}: does it fog? Heating the room to 25C25{}^{\circ}\mathrm{C} without adding water: new humidity.

Solution

Solution of Exercise 25.9.

Ps(22C)2.34+0.4×0.83=2.67kPaP_s(22{}^{\circ}\mathrm{C}) \approx 2.34 + 0.4 \times 0.83 = 2.67\,\mathrm{kPa}, Pv=0.70×2.67=1.87kPaP_v = 0.70 \times 2.67 = 1.87\,\mathrm{kPa}; dew point where Ps=1.87P_s = 1.87: 15+5×0.17/0.64=16C15 + 5 \times 0.17/0.64 = 16{}^{\circ}\mathrm{C}. Mass: ρv=1870×0.018/(8.314×295)=13.7g/m3\rho_v = 1870 \times 0.018/ (8.314 \times 295) = 13.7\,\mathrm{g}/\mathrm{m}^{3}, 0.69kg0.69\,\mathrm{kg} in the room. Pane at 12C12{}^{\circ}\mathrm{C}: Ps1.42kPa<1.87P_s \approx 1.42\,\mathrm{kPa} < 1.87, it fogs. At 25C25{}^{\circ}\mathrm{C} the humidity falls to 1.87/3.17=59%1.87/3.17 = 59\%.

Exercise 25.10 ★★★

The triple point. (a) Show from the state-function character of hh that, at the triple point, Ls=Lf+LvL_s = L_f + L_v (sublimation = fusion + vaporization). (b) Show with Clausius–Clapeyron that the sublimation curve is steeper than the vaporization curve at the triple point (neglect vsv_s, vlv_l before vvv_v). (c) Water: Lf=334kJ/kgL_f = 334\,\mathrm{kJ}/\mathrm{kg}, Lv=2500kJ/kgL_v = 2500\,\mathrm{kJ}/\mathrm{kg}, T=273.16KT = 273.16\,\mathrm{K}, P=611PaP = 611\,\mathrm{Pa}, vapour a perfect gas: both slopes in Pa/K\mathrm{Pa}/\mathrm{K}. (d) Why does snow disappear on a dry cold day without ever melting?

Solution

Solution of Exercise 25.10.

(a) hh is a state function: going solid \to liquid \to vapour at the triple point or solid \to vapour directly gives the same Δh\Delta h: Ls=Lf+LvL_s = L_f + L_v. (b) With vs,vlvvv_s, v_l \ll v_v both slopes are L/(Tvv)L/(Tv_v) at the same TT and vvv_v: their ratio is Ls/Lv>1L_s/L_v > 1. (c) vv=RT/(MP)=8.314×273.16/(0.018×611)=206m3/kgv_v = RT/(MP) = 8.314 \times 273.16/(0.018 \times 611) = 206\,\mathrm{m}^{3}/\mathrm{kg}; vaporization 2.50×106/(273.16×206)=44Pa/K2.50 \times 10^6/(273.16 \times 206) = 44\,\mathrm{Pa}/\mathrm{K}, sublimation 2.83×106/(273.16×206)=50Pa/K2.83 \times 10^6/ (273.16 \times 206) = 50\,\mathrm{Pa}/\mathrm{K}. (d) Below 0C0{}^{\circ}\mathrm{C} at 1bar1\,\mathrm{bar} no liquid exists; if the air’s vapour pressure is below PsP_s over ice (260Pa260\,\mathrm{Pa} at 10C-10{}^{\circ}\mathrm{C}) the snow sublimates — the dry cold wind eats it.

Exercise 25.11 ★★★

Superheated water. A bubble of radius rr in water at pressure P0P_0 contains vapour at P0+2σ/rP_0 + 2\sigma/r with σ=0.059N/m\sigma = 0.059\,\mathrm{N}/\mathrm{m} (admitted). (a) Minimum radius of a bubble that can grow in water at 105C105{}^{\circ}\mathrm{C} under 1.013bar1.013\,\mathrm{bar}, using  ⁣dPs/ ⁣dT=3.6kPa/K\dd P_s/\dd T = 3.6\,\mathrm{kPa}/\mathrm{K}. (b) Same at 101C101{}^{\circ}\mathrm{C}. (c) A cup of water superheated to 105C105{}^{\circ}\mathrm{C} in a microwave oven is disturbed by a spoon: fraction of the water that flashes to steam, and the volume of steam produced per litre of water — comment on the danger. (d) Why do boiling chips prevent this?

Solution

Solution of Exercise 25.11.

(a) Ps(105C)1.013+5×0.036=1.19barP_s(105{}^{\circ}\mathrm{C}) \approx 1.013 + 5 \times 0.036 = 1.19\,\mathrm{bar}: ΔP=0.18bar\Delta P = 0.18\,\mathrm{bar}, r=2×0.059/(1.8×104)=6.6µmr^\ast = 2 \times 0.059/(1.8 \times 10^4) = 6.6\,\text{µ}\mathrm{m}. (b) ΔP=3.6kPa\Delta P = 3.6\,\mathrm{kPa}, r=33µmr^\ast = 33\,\text{µ}\mathrm{m}. (c) x=cΔT/Lv=4.18×5/2257=0.93%x = c\,\Delta T/L_v = 4.18 \times 5/2257 = 0.93\%: 9.3g9.3\,\mathrm{g} per litre, i.e. 9.3×103×1.67=16L9.3 \times 10^{-3} \times 1.67 = 16\,\mathrm{L} of steam produced in a fraction of a second inside a cup — the water is blown out, boiling. (d) Chips hold air in their pores: bubbles of tens of micrometres already exist, so boiling starts as soon as PsP_s reaches P0P_0.

Exercise 25.12 ★★★

A refrigerant’s cycle. A heat pump runs R-134a round Definition 24.16: evaporation at 10C-10{}^{\circ}\mathrm{C} (2.0bar2.0\,\mathrm{bar}; hl=187kJ/kgh_l = 187\,\mathrm{kJ}/\mathrm{kg}, hv=392kJ/kgh_v = 392\,\mathrm{kJ}/\mathrm{kg}), condensation at 40C40{}^{\circ}\mathrm{C} (10.2bar10.2\,\mathrm{bar}; hl=256kJ/kgh_l = 256\,\mathrm{kJ}/\mathrm{kg}, hv=419kJ/kgh_v = 419\,\mathrm{kJ}/\mathrm{kg}). The fluid leaves the condenser as saturated liquid and the evaporator as saturated vapour; the compressor delivers it at h=430kJ/kgh = 430\,\mathrm{kJ}/\mathrm{kg}. Admit that in the valve hh is conserved and that the compressor’s work per kilogram is Δh\Delta h (steady-flow balances, Year 2 volume); in the exchangers, isobaric, q=Δhq = \Delta h (Proposition 22.7). (a) Quality at the evaporator inlet. (b) Heat taken per kilogram in the evaporator, heat given in the condenser, work of compression; check the first law. (c) epe_p and efe_f; compare with the Carnot values between the two saturation temperatures. (d) Mass flow rate for 6kW6\,\mathrm{kW} of heating.

Solution

Solution of Exercise 25.12.

(a) After the valve h=256kJ/kgh = 256\,\mathrm{kJ}/\mathrm{kg} at 10C-10{}^{\circ}\mathrm{C}: x=(256187)/(392187)=0.34x = (256 - 187)/(392 - 187) = 0.34. (b) Evaporator qc=392256=136kJ/kgq_c = 392 - 256 = 136\,\mathrm{kJ}/\mathrm{kg}; compressor w=430392=38kJ/kgw = 430 - 392 = 38\,\mathrm{kJ}/\mathrm{kg}; condenser qh=256430=174kJ/kgq_h = 256 - 430 = -174\,\mathrm{kJ}/\mathrm{kg}; 136+38174=0136 + 38 - 174 = 0. (c) ep=174/38=4.6e_p = 174/38 = 4.6, ef=136/38=3.6e_f = 136/38 = 3.6; Carnot 313/50=6.3313/50 = 6.3 and 263/50=5.3263/50 = 5.3: about 0.70.7 of the ideal. (d) m˙=6000/174000=34g/s\dot m = 6000/174000 = 34\,\mathrm{g}/\mathrm{s}, 2.1kg2.1\,\mathrm{kg} a minute.

A pressure cooker: at 1.8\, bar water boils at 117 C, and the weighted valve is what sets the pressure.
A pressure cooker: at 1.8bar1.8\,\mathrm{bar} water boils at 117C117{}^{\circ}\mathrm{C}, and the weighted valve is what sets the pressure.

25.7 Problem: Water in four scenes

Problem 25.1

Weekend problem — the pressure cooker, the cloud, the sealed vessel and the supercooled bottle: one substance, four uses of its phase diagram

Data for water: Lv=2257kJ/kgL_v = 2257\,\mathrm{kJ}/\mathrm{kg} at 100C100{}^{\circ}\mathrm{C} and about 2.2MJ/kg2.2\,\mathrm{MJ}/\mathrm{kg} at 117C117{}^{\circ}\mathrm{C}, 2.45MJ/kg2.45\,\mathrm{MJ}/\mathrm{kg} near 20C20{}^{\circ}\mathrm{C}; Lf=334kJ/kgL_f = 334\,\mathrm{kJ}/\mathrm{kg}; c=4.18kJ/(kgK)c = 4.18\,\mathrm{kJ}/(\mathrm{kg}\,\mathrm{K}) (liquid); M=18g/molM = 18\,\mathrm{g}/\mathrm{mol}; MLv/R=4890KML_v/R = 4890\,\mathrm{K} near 100C100{}^{\circ}\mathrm{C}. Saturation pressures: 0.61kPa0.61\,\mathrm{kPa} (0C0{}^{\circ}\mathrm{C}), 1.23kPa1.23\,\mathrm{kPa} (10C10{}^{\circ}\mathrm{C}), 1.70kPa1.70\,\mathrm{kPa} (15C15{}^{\circ}\mathrm{C}), 2.34kPa2.34\,\mathrm{kPa} (20C20{}^{\circ}\mathrm{C}), 3.17kPa3.17\,\mathrm{kPa} (25C25{}^{\circ}\mathrm{C}), 4.24kPa4.24\,\mathrm{kPa} (30C30{}^{\circ}\mathrm{C}), 101.3kPa101.3\,\mathrm{kPa} (100C100{}^{\circ}\mathrm{C}). Saturated specific volumes: vl=1.0×103m3/kgv_l = 1.0 \times 10^{-3}\,\mathrm{m}^{3}/\mathrm{kg} (cold water), 1.9×103m3/kg1.9 \times 10^{-3}\,\mathrm{m}^{3}/\mathrm{kg} at 360C360{}^{\circ}\mathrm{C}; vv=0.0217m3/kgv_v = 0.0217\,\mathrm{m}^{3}/\mathrm{kg} at 300C300{}^{\circ}\mathrm{C}, 0.01080.0108 at 340C340{}^{\circ}\mathrm{C}, 0.00880.0088 at 350C350{}^{\circ}\mathrm{C}; critical point 374C374{}^{\circ}\mathrm{C}, 221bar221\,\mathrm{bar}, vc=3.1×103m3/kgv_c = 3.1 \times 10^{-3}\,\mathrm{m}^{3}/\mathrm{kg}. Air: M=29g/molM = 29\,\mathrm{g}/\mathrm{mol}, cp=1.0kJ/(kgK)c_p = 1.0\,\mathrm{kJ}/(\mathrm{kg}\,\mathrm{K}), γ=1.4\gamma = 1.4; g=9.8m/s2g = 9.8\,\mathrm{m}/\mathrm{s}^{2}; R=8.314J/(molK)R = 8.314\,\mathrm{J}/(\mathrm{mol}\,\mathrm{K}).

Part I — The pressure cooker.

  1. Why can water in an open pan at sea level not be heated above 100C100{}^{\circ}\mathrm{C}, however strong the flame?
  2. Starting from the Clausius–Clapeyron relation, derive ln[Ps(T)/Ps(T0)]=(MLv/R)(1/T01/T)\ln[P_s(T)/P_s(T_0)] = (ML_v/R)(1/T_0 - 1/T), stating the approximations.
  3. Temperature in a cooker whose valve opens at 1.8bar1.8\,\mathrm{bar} absolute.
  4. The valve is a weight resting on an orifice of 20mm220\,\mathrm{mm}^{2}; atmospheric pressure 1.0bar1.0\,\mathrm{bar}: mass of the weight.
  5. 2.0L2.0\,\mathrm{L} of water are brought from 20C20{}^{\circ}\mathrm{C} to the working temperature by a 2.0kW2.0\,\mathrm{kW} plate (neglect the pot): heat and time.
  6. Once there, the plate is left at 2.0kW2.0\,\mathrm{kW}: mass of steam leaving the valve per minute. What should the cook do?
  7. Cooking reactions roughly double in rate for every 10K10\,\mathrm{K}: by what factor does the cooker shorten a 30min30\,\mathrm{min} sea-level recipe? And how long would the recipe take on Everest, where water boils at 70C70{}^{\circ}\mathrm{C}?

Part II — The cloud.

  1. Define relative humidity. Air at 25C25{}^{\circ}\mathrm{C} and 60%60\%: partial pressure of vapour, and mass of vapour per cubic metre (perfect gas).
  2. Dew point of that air (interpolate the table). Explain the dew on the grass at dawn and the drops on a cold bottle.
  3. A parcel of dry air rises without exchanging heat. From the reversible adiabatic law and the hydrostatic relation  ⁣dP/ ⁣dz=ρg\dd P/\dd z = -\rho g, show that  ⁣dT/ ⁣dz=g/cp\dd T/\dd z = -g/c_p and evaluate it.
  4. The dew point of the rising parcel itself falls by about 2K/km2\,\mathrm{K}/\mathrm{km} as the pressure drops. Height at which the parcel of question 8 becomes saturated — the base of the cloud.
  5. Above the base, the vapour that condenses releases its latent heat into the parcel. By how much does condensing 1g1\,\mathrm{g} of water per kilogram of air warm that air? What does this do to the cooling rate of the parcel as it keeps rising, and why does it matter for thunderstorms?
  6. A cumulus of 1km31\,\mathrm{km}^{3} holds 1g1\,\mathrm{g} of liquid water per cubic metre: mass of water, and the energy released by its condensation, in joules and in GWh\mathrm{GW}\mathrm{h}.
  7. A bathroom mirror at 18C18{}^{\circ}\mathrm{C}, air at 25C25{}^{\circ}\mathrm{C} and 80%80\%: does it fog? At what humidity would it stop?

Part III — The sealed vessel. A rigid steel vessel of 1.0L1.0\,\mathrm{L} is filled with a mass mm of water and sealed with no air, then heated slowly.

  1. m=0.50kgm = 0.50\,\mathrm{kg} at 20C20{}^{\circ}\mathrm{C}: pressure inside, specific volume, mass of vapour (use the perfect gas for vvv_v), fraction of the volume filled by liquid.
  2. Heated: does the liquid level rise or fall? At roughly what temperature does the liquid fill the vessel, and what happens to the pressure after that? (Use vlv_l at 360C360{}^{\circ}\mathrm{C}.)
  3. m=0.10kgm = 0.10\,\mathrm{kg}: does the liquid level rise or fall on heating? At roughly what temperature does the last drop evaporate (use the vvv_v table)?
  4. m=0.31kgm = 0.31\,\mathrm{kg}: describe what an observer sees at the meniscus as the temperature approaches 374C374{}^{\circ}\mathrm{C}.
  5. Sketch the three heating paths in the (v,P)(v, P) diagram with the saturation dome, and say which side of the critical point each passes.
  6. The same 1.0L1.0\,\mathrm{L} vessel with 0.50kg0.50\,\mathrm{kg} of water is now sealed with the air it contained at 20C20{}^{\circ}\mathrm{C}, 1.0bar1.0\,\mathrm{bar}, and heated to 100C100{}^{\circ}\mathrm{C}: total pressure inside (Dalton), and the force on a lid of 100cm2100\,\mathrm{cm}^{2}.

Part IV — The supercooled bottle.

  1. A clean, still bottle of water has cooled to 8C-8{}^{\circ}\mathrm{C} without freezing. What is this state called, why is it possible, and what happens when the bottle is knocked? Why does the temperature then settle at exactly 0C0{}^{\circ}\mathrm{C}?
  2. Fraction of the water that freezes (the process is fast, hence adiabatic).
  3. Entropy created per kilogram; sign check.
  4. The reverse surprise: a cup of water heated to 105C105{}^{\circ}\mathrm{C} in a microwave oven without boiling, then disturbed. Fraction of the water that flashes to steam, volume of steam produced per litre (vv=1.67m3/kgv_v = 1.67\,\mathrm{m}^{3}/\mathrm{kg}), and why the cup erupts.
  5. Lost work: the supercooled litre could have driven a reversible engine with the 0C0{}^{\circ}\mathrm{C} surroundings; taking T0=273KT_0 = 273\,\mathrm{K}, the work thrown away by letting it freeze on a knock is T0ScreatedT_0S_{\mathrm{created}}. Evaluate it per litre and compare with lifting the bottle by one metre. Conclude: what does a metastable state store?
Solution

Solution of Problem 25.1.

1. At 1atm1\,\mathrm{atm} water boils at 100C100{}^{\circ}\mathrm{C}; while liquid remains, any heat supplied makes vapour at that temperature (latent heat) instead of warming the liquid: the temperature is pinned by the pressure.

2.  ⁣dPs/ ⁣dT=Lv/[T(vvvl)]\dd P_s/\dd T = L_v/[T(v_v - v_l)] with vlvv=RT/(MPs)v_l \ll v_v = RT/(MP_s) (perfect-gas vapour):  ⁣dPs/Ps=(MLv/R) ⁣dT/T2\dd P_s/P_s = (ML_v/R)\,\dd T/T^2; with LvL_v taken constant, integrate: ln(Ps/P0)=(MLv/R)(1/T01/T)\ln(P_s/P_0) = (ML_v/R)(1/T_0 - 1/T).

3. 1/T=1/373.15ln(1.8/1.013)/4890=2.562×1031/T = 1/373.15 - \ln(1.8/1.013)/4890 = 2.562 \times 10^{-3}: T=390K=117CT = 390\,\mathrm{K} = 117{}^{\circ}\mathrm{C}.

4. m=ΔPA/g=0.8×105×2.0×105/9.8=0.16kgm = \Delta P\,A/g = 0.8 \times 10^5 \times 2.0 \times 10^{-5}/9.8 = 0.16\,\mathrm{kg}.

5. Q=2.0×4.18×97=811kJQ = 2.0 \times 4.18 \times 97 = 811\,\mathrm{kJ}; t=811/2.0=405s7mint = 811/2.0 = 405\,\mathrm{s} \approx 7\,\mathrm{min}.

6. 2000/(2.2×106)=0.91g/s=55g/min2000/(2.2 \times 10^6) = 0.91\,\mathrm{g}/\mathrm{s} = 55\,\mathrm{g}/\mathrm{min} — two litres gone in 37min37\,\mathrm{min}. Turn the plate down to the least that keeps the valve hissing: the temperature is set by the pressure, not by the flame.

7. +17K+17\,\mathrm{K}: 21.7=3.22^{1.7} = 3.2 times faster, 30min30\,\mathrm{min} \to 9min9\,\mathrm{min}. Everest, 30K-30\,\mathrm{K}: 232^{-3}, four hours.

8. Relative humidity =Pv/Ps(T)= P_v/P_s(T). Pv=0.60×3.17=1.90kPaP_v = 0.60 \times 3.17 = 1.90\,\mathrm{kPa}; ρv=PvM/(RT)=1900×0.018/(8.314×298)=13.8g/m3\rho_v = P_vM/(RT) = 1900 \times 0.018/(8.314 \times 298) = 13.8\,\mathrm{g}/\mathrm{m}^{3}.

9. Ps(Td)=1.90kPaP_s(T_d) = 1.90\,\mathrm{kPa}: between 15C15{}^{\circ}\mathrm{C} (1.70kPa1.70\,\mathrm{kPa}) and 20C20{}^{\circ}\mathrm{C} (2.34kPa2.34\,\mathrm{kPa}): Td=15+5×0.20/0.64=16.6CT_d = 15 + 5 \times 0.20/0.64 = 16.6{}^{\circ}\mathrm{C}. Grass radiating to the night sky, or a bottle from the refrigerator, falls below TdT_d: the vapour in contact with it is then above saturation and condenses.

10. TP(1γ)/γ=constTP^{(1-\gamma)/\gamma} = \text{const}:  ⁣dT/T=γ1γ ⁣dP/P\dd T/T = \frac{\gamma - 1}{\gamma} \dd P/P;  ⁣dP=ρg ⁣dz\dd P = -\rho g\,\dd z with ρ=PM/(RT)\rho = PM/(RT):  ⁣dT/T=γ1γMgRT ⁣dz\dd T/T = -\frac{\gamma - 1}{\gamma}\frac{Mg}{RT}\dd z, so  ⁣dT/ ⁣dz=γ1γMgR=g/cp\dd T/\dd z = -\frac{\gamma - 1}{\gamma}\frac{Mg}{R} = -g/c_p since cp=γR/[(γ1)M]c_p = \gamma R/[(\gamma - 1)M]. Value 9.8/1000=9.8K/km9.8/1000 = 9.8\,\mathrm{K}/\mathrm{km}.

11. TTdT - T_d closes at 9.82=7.8K/km9.8 - 2 = 7.8\,\mathrm{K}/\mathrm{km}: z=(2516.6)/7.8=1.1kmz = (25 - 16.6)/ 7.8 = 1.1\,\mathrm{km}.

12. 1×2.45=2.45kJ1 \times 2.45 = 2.45\,\mathrm{kJ} per kilogram of air: ΔT=2.45K\Delta T = 2.45\,\mathrm{K}. The release offsets part of the adiabatic cooling: a saturated parcel cools at only 5 to 6K/km5\text{ to }6\,\mathrm{K}/\mathrm{km}, stays warmer and lighter than its surroundings and keeps rising — the latent heat is the fuel of the thunderstorm.

13. 109×1g=1000t10^9 \times 1\,\mathrm{g} = 1000\,\mathrm{t}; 106×2.45×106=2.5×1012J=0.68GWh10^6 \times 2.45 \times 10^6 = 2.5 \times 10^{12}\,\mathrm{J} = 0.68\,\mathrm{GW}\mathrm{h} — forty minutes of a large power plant.

14. Pv=0.80×3.17=2.54kPaP_v = 0.80 \times 3.17 = 2.54\,\mathrm{kPa}; Ps(18C)1.70+0.6×0.64=2.08kPa<2.54P_s(18{}^{\circ}\mathrm{C}) \approx 1.70 + 0.6 \times 0.64 = 2.08\,\mathrm{kPa} < 2.54: it fogs, until the humidity drops below 2.08/3.17=66%2.08/3.17 = 66\%.

15. P=Ps(20C)=2.3kPaP = P_s(20{}^{\circ}\mathrm{C}) = 2.3\,\mathrm{kPa}; v=2.0×103m3/kgv = 2.0 \times 10^{-3}\,\mathrm{m}^{3}/\mathrm{kg}; vv=RT/(MPs)=8.314×293/(0.018×2340)=58m3/kgv_v = RT/(MP_s) = 8.314 \times 293/(0.018 \times 2340) = 58\,\mathrm{m}^{3}/\mathrm{kg}; x=(2.01.0)×103/58=1.7×105x = (2.0 - 1.0) \times 10^{-3}/58 = 1.7 \times 10^{-5}: 9mg9\,\mathrm{mg} of vapour; liquid 0.50×103=0.50L0.50 \times 10^{-3} = 0.50\,\mathrm{L}, half the vessel.

16. v=2.0×103m3/kg<vcv = 2.0 \times 10^{-3}\,\mathrm{m}^{3}/\mathrm{kg} < v_c: the isochore meets the liquid branch of the dome — the liquid expands faster than it evaporates, the level rises, and the vessel is full of liquid when vl(T)=2.0×103m3/kgv_l(T) = 2.0 \times 10^{-3}\,\mathrm{m}^{3}/\mathrm{kg}, a little above 360C360{}^{\circ}\mathrm{C} (about 190bar190\,\mathrm{bar}). Beyond, a nearly incompressible liquid heated at constant volume: the pressure climbs by tens of bar per kelvin — the vessel bursts. Never seal a vessel full of liquid.

17. v=1.0×102m3/kg>vcv = 1.0 \times 10^{-2}\,\mathrm{m}^{3}/\mathrm{kg} > v_c: the level falls; the last drop goes when vv(T)=0.010v_v(T) = 0.010, between 340C340{}^{\circ}\mathrm{C} (0.01080.0108) and 350C350{}^{\circ}\mathrm{C} (0.00880.0088): about 344C344{}^{\circ}\mathrm{C}, 150bar150\,\mathrm{bar}.

18. v=3.2×103m3/kgvcv = 3.2 \times 10^{-3}\,\mathrm{m}^{3}/\mathrm{kg} \approx v_c: the meniscus stays near mid-height, grows flatter and fainter as the two densities converge, the fluid turns milky (critical opalescence), and at 374C374{}^{\circ}\mathrm{C}, 221bar221\,\mathrm{bar} the meniscus vanishes: one phase.

19. Three vertical lines: v=2.0×103v = 2.0 \times 10^{-3} leaves the dome through the liquid branch, left of C; 10210^{-2} through the vapour branch, right of C; 3.2×1033.2 \times 10^{-3} through the summit.

20. Air: 0.5L0.5\,\mathrm{L} at 1.0bar1.0\,\mathrm{bar}, 293K293\,\mathrm{K}, same volume at 373K373\,\mathrm{K}: Pair=1.0×373/293=1.27barP_{\text{air}} = 1.0 \times 373/293 = 1.27\,\mathrm{bar}; plus Ps=1.01barP_s = 1.01\,\mathrm{bar}: 2.3bar2.3\,\mathrm{bar} inside, 1.3bar1.3\,\mathrm{bar} above the outside: 1.3×105×102=1.3kN1.3 \times 10^5 \times 10^{-2} = 1.3\,\mathrm{kN} on the lid — the weight of 130kg130\,\mathrm{kg}.

21. Supercooled, metastable: no nucleation site (clean water, no dust, no motion) for the first crystal. A knock nucleates ice, which grows through the bottle releasing LfL_f; the temperature rises to 0C0{}^{\circ}\mathrm{C} and stops there, the only temperature at which ice and water coexist at 1atm1\,\mathrm{atm}: the freezing halts as soon as the released heat has brought the mixture to it.

22. x=cΔT/Lf=4.18×8/334=0.10x = c\,\Delta T/L_f = 4.18 \times 8/334 = 0.10.

23. Δs=cln(273/265)xLf/273=124.3122.3=+2.0J/(kgK)\Delta s = c\ln(273/265) - xL_f/273 = 124.3 - 122.3 = +2.0\,\mathrm{J}/(\mathrm{kg}\,\mathrm{K}): adiabatic, hence all created; positive, as a spontaneous process must be.

24. x=4.18×5/2257=0.93%x = 4.18 \times 5/2257 = 0.93\%: 9.3g9.3\,\mathrm{g} of steam per litre, 9.3×103×1.67=16L9.3 \times 10^{-3} \times 1.67 = 16\,\mathrm{L} of vapour born in the bulk in a fraction of a second: the cup erupts.

25. T0Screated=273×2.0=550JT_0S_{\mathrm{created}} = 273 \times 2.0 = 550\,\mathrm{J} per litre, against mgh=9.8Jmgh = 9.8\,\mathrm{J}: fifty-six times more. A metastable state stores work — what a reversible path could have extracted — and a knock turns it all into entropy.

Terms defined in this chapter

See all 393 terms in the glossary