Level 4 — ApplicationThermodynamics

Thermodynamics

60 minutes50 marksprintable — key stays hidden on paper

Level 4: Application (Novel Problems, No Hints)

Time limit: 60 minutes Total marks: 50 Instructions: Answer all questions. Use R=8.314 Jmol1K1R = 8.314\ \mathrm{J\,mol^{-1}K^{-1}}, σ=5.67×108 Wm2K4\sigma = 5.67\times10^{-8}\ \mathrm{W\,m^{-2}K^{-4}}, kB=1.38×1023 J/Kk_B = 1.38\times10^{-23}\ \mathrm{J/K}, NA=6.022×1023 mol1N_A = 6.022\times10^{23}\ \mathrm{mol^{-1}}. Show all working.


Question 1 — Calorimetry with phase change (10 marks)

A sealed copper vessel of mass 0.150 kg0.150\ \mathrm{kg} contains 0.200 kg0.200\ \mathrm{kg} of water, all at 18.0C18.0^\circ\mathrm{C}. A block of ice of mass 0.0800 kg0.0800\ \mathrm{kg} at 12.0C-12.0^\circ\mathrm{C} is dropped in and the system sealed.

Data: cCu=386c_\text{Cu}=386, cwater=4186c_\text{water}=4186, cice=2100c_\text{ice}=2100 (all Jkg1K1\mathrm{J\,kg^{-1}K^{-1}}), latent heat of fusion Lf=3.34×105 J/kgL_f=3.34\times10^{5}\ \mathrm{J/kg}.

(a) Determine the final equilibrium temperature of the system, showing that not all the ice necessarily melts (or that it does). (7) (b) State the final composition (masses of ice and liquid water present). (3)


Question 2 — Adiabatic + heat transfer chain (12 marks)

0.400 mol0.400\ \mathrm{mol} of an ideal diatomic gas (γ=7/5\gamma = 7/5) initially at 300 K300\ \mathrm{K} and volume 8.00×103 m38.00\times10^{-3}\ \mathrm{m^3} is compressed adiabatically and reversibly to one quarter of its volume.

(a) Find the final temperature and pressure. (4) (b) Find the work done on the gas during this compression. (3) (c) The gas (now at the compressed state) is placed in contact with a reservoir and allowed to cool at constant volume back to 300 K300\ \mathrm{K}. Find the heat expelled in this step. (3) (d) The compressed hot gas, before cooling, is contained by a spherical steel shell of surface area 0.0300 m20.0300\ \mathrm{m^2} and emissivity 0.600.60. Treating it as a grey body radiating into surroundings at 300 K300\ \mathrm{K}, find the net instantaneous radiated power at the instant compression ends. (2)


Question 3 — Kinetic theory / Maxwell–Boltzmann (10 marks)

(a) For a gas of molecular mass mm at temperature TT, starting from the Maxwell–Boltzmann speed distribution f(v)=4πn(m2πkBT)3/2v2emv2/2kBT,f(v) = 4\pi n\left(\frac{m}{2\pi k_B T}\right)^{3/2} v^2 e^{-mv^2/2k_B T}, derive expressions for the most probable speed vpv_p and show that vrms/vp=3/2v_{rms}/v_p = \sqrt{3/2}. (5)

(b) Nitrogen gas (M=28.0 g/molM = 28.0\ \mathrm{g/mol}) is at 350 K350\ \mathrm{K}. Compute vpv_p, the mean speed vˉ\bar v, and vrmsv_{rms} numerically. (3)

(c) A rocket propulsion designer wants the fraction of molecules with speed above some threshold. Without full integration, explain qualitatively (using the distribution) why heating the gas from 350 K350\ \mathrm{K} to 700 K700\ \mathrm{K} increases the high-speed tail population more than proportionally, and what happens to the peak height of f(v)f(v). (2)


Question 4 — Cycle efficiency and entropy (12 marks)

An inventor claims a heat engine operating between reservoirs at TH=620 KT_H = 620\ \mathrm{K} and TC=310 KT_C = 310\ \mathrm{K} that absorbs QH=1000 JQ_H = 1000\ \mathrm{J} per cycle and delivers 560 J560\ \mathrm{J} of work.

(a) Compute the claimed efficiency and the Carnot efficiency; state whether the claim is possible and justify using the second law. (4)

(b) For the claimed engine, compute the total entropy change of the universe per cycle (ΔSuniv\Delta S_{univ}) and comment. (4)

(c) A valid engine on the same reservoirs is instead run as a Carnot engine. It is then reversed to act as a refrigerator extracting heat from the 310 K310\ \mathrm{K} space. Compute the coefficient of performance (COP) of this refrigerator. (2)

(d) If the refrigerator in (c) must extract 2000 J2000\ \mathrm{J} from the cold space per cycle, find the work input required. (2)


Question 5 — Thermal expansion (short applied) (6 marks)

A steel measuring tape is calibrated correct at 20C20^\circ\mathrm{C} (αsteel=1.2×105 K1\alpha_\text{steel} = 1.2\times10^{-5}\ \mathrm{K^{-1}}). On a hot day at 42C42^\circ\mathrm{C} a surveyor reads a distance as 86.400 m86.400\ \mathrm{m} using this tape.

(a) Is the true distance greater or less than the reading? Explain in one sentence. (2) (b) Compute the true distance. (4)

Answer keyMark scheme & solutions

Question 1 (10 marks)

Strategy: Compare heat available from cooling water+vessel to 00^\circC against heat needed to warm ice to 00^\circC and melt it.

(a) Heat released by water + copper cooling from 18018\to0^\circC: Qavail=(mwcw+mCucCu)(18.0)=(0.2004186+0.150386)(18.0)Q_\text{avail} = (m_wc_w + m_{Cu}c_{Cu})(18.0) = (0.200\cdot4186 + 0.150\cdot386)(18.0) =(837.2+57.9)(18.0)=895.1×18.0=1.6112×104 J= (837.2 + 57.9)(18.0) = 895.1\times18.0 = 1.6112\times10^4\ \mathrm{J} (2)

Heat to warm ice from 120-12\to0^\circC: Qwarm=micice(12.0)=0.0800210012.0=2016 JQ_\text{warm} = m_i c_\text{ice}(12.0) = 0.0800\cdot2100\cdot12.0 = 2016\ \mathrm{J} (1)

Heat to melt all ice: Qmelt,all=miLf=0.08003.34×105=2.672×104 JQ_\text{melt,all} = m_i L_f = 0.0800\cdot3.34\times10^5 = 2.672\times10^4\ \mathrm{J} (1)

Remaining after warming ice: 1.6112×1042016=1.4096×104 J1.6112\times10^4 - 2016 = 1.4096\times10^4\ \mathrm{J}. Since 1.4096×104<2.672×1041.4096\times10^4 < 2.672\times10^4, not all ice melts — system settles at 00^\circC. (2)

Final temperature =0C= 0^\circ\mathrm{C} (1)

(b) Mass of ice melted: mmelt=1.4096×1043.34×105=0.0422 kgm_\text{melt} = \frac{1.4096\times10^4}{3.34\times10^5} = 0.0422\ \mathrm{kg} Ice remaining =0.08000.0422=0.0378 kg= 0.0800 - 0.0422 = 0.0378\ \mathrm{kg}. Liquid water =0.200+0.0422=0.2422 kg= 0.200 + 0.0422 = 0.2422\ \mathrm{kg}. (3) (Composition: ≈0.0378 kg ice + ≈0.242 kg water at 0°C.)


Question 2 (12 marks)

(a) Adiabatic: TVγ1=TV^{\gamma-1}=const, γ1=0.4\gamma-1=0.4, Vf/Vi=1/4V_f/V_i=1/4. Tf=Ti(Vi/Vf)γ1=30040.4=3001.7411=522.3 KT_f = T_i(V_i/V_f)^{\gamma-1} = 300\cdot4^{0.4} = 300\cdot1.7411 = 522.3\ \mathrm{K} (2) Initial pressure Pi=nRTi/Vi=0.4008.314300/8.00×103=1.2471×105 PaP_i = nRT_i/V_i = 0.400\cdot8.314\cdot300/8.00\times10^{-3} = 1.2471\times10^5\ \mathrm{Pa}. Pf=Pi(Vi/Vf)γ=1.2471×10541.4=1.2471×1056.9644=8.686×105 PaP_f = P_i(V_i/V_f)^{\gamma} = 1.2471\times10^5\cdot4^{1.4} = 1.2471\times10^5\cdot6.9644 = 8.686\times10^5\ \mathrm{Pa} (2)

(b) Adiabatic Q=0Q=0, so work on gas =ΔU=nCVΔT= \Delta U = nC_V\Delta T, CV=52RC_V=\tfrac52R. Won=nCV(TfTi)=0.400528.314(522.3300)W_\text{on} = nC_V(T_f-T_i) = 0.400\cdot\tfrac52\cdot8.314\cdot(522.3-300) =0.40020.785222.3=1848 J= 0.400\cdot20.785\cdot222.3 = 1848\ \mathrm{J} (3)

(c) Constant-volume cooling 522.3300522.3\to300 K: Q=nCVΔT=0.40020.785(300522.3)=1848 JQ = nC_V\Delta T = 0.400\cdot20.785\cdot(300-522.3) = -1848\ \mathrm{J} Heat expelled 1848 J\approx 1848\ \mathrm{J} (magnitude). (3)

(d) Net radiated power: P=εσA(Tf4Ts4)=0.605.67×1080.0300(522.343004)P = \varepsilon\sigma A(T_f^4 - T_s^4) = 0.60\cdot5.67\times10^{-8}\cdot0.0300\cdot(522.3^4 - 300^4) 522.34=7.442×1010522.3^4 = 7.442\times10^{10}, 3004=8.10×109300^4=8.10\times10^{9}, difference =6.632×1010=6.632\times10^{10}. P=0.605.67×1080.03006.632×1010=67.7 WP = 0.60\cdot5.67\times10^{-8}\cdot0.0300\cdot6.632\times10^{10} = 67.7\ \mathrm{W} (2)


Question 3 (10 marks)

(a) vpv_p: maximise f(v)f(v); set ddv(v2emv2/2kBT)=0\frac{d}{dv}(v^2 e^{-mv^2/2k_BT})=0: 2ve+v2(mv/kBT)e=02=mv2kBTvp=2kBTm2v e^{-\cdots} + v^2(-mv/k_BT)e^{-\cdots}=0 \Rightarrow 2 = \frac{mv^2}{k_BT} \Rightarrow v_p=\sqrt{\frac{2k_BT}{m}} (2) vrms=v2=3kBT/mv_{rms}=\sqrt{\langle v^2\rangle}=\sqrt{3k_BT/m} (standard result / from v2fdv\int v^2 f\,dv). (2) vrmsvp=3kBT/m2kBT/m=3/2.\frac{v_{rms}}{v_p}=\sqrt{\frac{3k_BT/m}{2k_BT/m}}=\sqrt{3/2}. (1)

(b) M=0.0280 kg/molM=0.0280\ \mathrm{kg/mol}; use kBT/m=RT/Mk_BT/m = RT/M, RT/M=8.314350/0.0280=1.0393×105RT/M = 8.314\cdot350/0.0280 = 1.0393\times10^5. vp=21.0393×105=456 m/sv_p=\sqrt{2\cdot1.0393\times10^5}=456\ \mathrm{m/s} vˉ=8kBTπm=8/πRT/M=1.5958322.4=514 m/s\bar v=\sqrt{\frac{8k_BT}{\pi m}}=\sqrt{8/\pi}\,\sqrt{RT/M}=1.5958\cdot322.4=514\ \mathrm{m/s} vrms=31.0393×105=558 m/sv_{rms}=\sqrt{3\cdot1.0393\times10^5}=558\ \mathrm{m/s} (3)

(c) Raising TT shifts vpTv_p\propto\sqrt T to higher speed and broadens the distribution; the exponential emv2/2kBTe^{-mv^2/2k_BT} decays more slowly, so the tail beyond a fixed threshold grows disproportionately (exponentially sensitive). Normalisation (area fixed) plus broadening means the peak height decreases. (2)


Question 4 (12 marks)

(a) Claimed η=560/1000=0.560\eta = 560/1000 = 0.560 (56.0%). Carnot ηC=1TC/TH=1310/620=0.500\eta_C = 1 - T_C/T_H = 1 - 310/620 = 0.500 (50.0%). (2) Since claimed η>ηC\eta > \eta_C, the engine violates the second law (Kelvin–Planck / Carnot's theorem: no engine can exceed Carnot efficiency between the same reservoirs). Impossible. (2)

(b) For claimed engine, QC=QHW=1000560=440 JQ_C = Q_H - W = 1000-560 = 440\ \mathrm{J} dumped to cold reservoir. ΔSuniv=QHTH+QCTC=1000620+440310=1.6129+1.4194=0.1935 J/K\Delta S_{univ}=-\frac{Q_H}{T_H}+\frac{Q_C}{T_C}=-\frac{1000}{620}+\frac{440}{310}=-1.6129+1.4194=-0.1935\ \mathrm{J/K} (3) ΔSuniv<0\Delta S_{univ}<0 violates the second law (entropy of universe must not decrease) — confirms impossibility. (1)

(c) Reversed Carnot refrigerator: COP=TCTHTC=310620310=310310=1.00\mathrm{COP}=\dfrac{T_C}{T_H-T_C}=\dfrac{310}{620-310}=\dfrac{310}{310}=1.00. (2)

(d) COP=QC/WW=QC/COP=2000/1.00=2000 J\mathrm{COP}=Q_C/W \Rightarrow W = Q_C/\mathrm{COP} = 2000/1.00 = 2000\ \mathrm{J}. (2)


Question 5 (6 marks)

(a) At 4242^\circC the steel tape has expanded, so each marked interval is longer than nominal; the tape under-reads, hence the true distance is greater than the reading. (2)

(b) ΔT=22 K\Delta T = 22\ \mathrm{K}. Each division length scales by (1+αΔT)(1+\alpha\Delta T): Ltrue=Lread(1+αΔT)=86.400(1+1.2×10522)L_\text{true}=L_\text{read}(1+\alpha\Delta T)=86.400(1+1.2\times10^{-5}\cdot22) =86.400(1+2.64×104)=86.400+0.02281=86.423 m=86.400(1+2.64\times10^{-4})=86.400+0.02281 = 86.423\ \mathrm{m} (4)


[
  {"claim":"Q1: heat available (16112 J) < warm+melt-all (2016+26720), and melted ice mass ~0.0422 kg",
   "code":"Qav=(0.200*4186+0.150*386)*18.0; Qwarm=0.0800*2100*12.0; Qmeltall=0.0800*3.34e5; mmelt=(Qav-Qwarm)/3.34e5; result = (Qav < Qwarm+Qmeltall) and abs(mmelt-0.0422)<0.001"},
  {"claim":"Q2a: adiabatic final T = 300*4**0.4 ≈ 522.3 K",
   "code":"Tf=300*4**0.4; result = abs(Tf-522.3)<0.5"},
  {"claim":"Q2b: work on gas ≈1848 J and equals Q2c magnitude",
   "code":"Tf=300*4**0.4; W=0.400*2.5*8.314*(Tf-300); result = abs(W-1848)<3"},
  {"claim":"Q4a: claimed eff 0.56 exceeds Carnot 0.50",
   "code":"eta=560/1000; etac=1-310/620; result = (eta>etac) and abs(etac-0.5)<1e-9"},
  {"claim":"Q4b: dS_univ negative ≈ -0.1935 J/K",
   "code":"dS=-1000/620+440/310; result = (dS<0) and abs(dS+0.1935)<0.001"},
  {"claim":"Q5b: true distance ≈86.423 m",
   "code":"L=86.400*(1+1.2e-5*22); result = abs(L-86.4228)<0.001"}
]