Irreversible Processes and Entropy — Question 4

Section 20-1 · Physics pages 3238–3239

Question 4 Viscous stirring converts organized work into internal energy A rigid insulated vessel contains liquid with constant heat capacity C = 1000 J/K, initially at 300 K. A paddle supplies 6000 J of shaft work to the liquid. The paddle has no net energy storage. Use ∆S = C ln(Tf/Ti). liquid shaft work in Schematic; labels, not drawing lengths, specify the data. (a) Find final temperature and entropy change of the liquid. (b) Compute the heat that a reversible heating path would transfer between the same endpoint temperatures. Explain why work input does not carry entropy into the actual insulated vessel.
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Question 4 - Solution Viscous stirring converts organized work into internal energy liquid shaft work in (a) Method and calculation Q = 0, Wby = −6000 J, C(Tf −300) = 6000 ⇒Tf = 306 K. ∆S = 1000 ln(306/300) ≈19.8026 J/K. (b) Interpretation and further calculation Qrev = ∫306 300 C dT = 6000 J, ∫δQrev T = C ln(306/300). Sgenerated = ∆S − ∫δQactual Tb = 19.8026 J/K. Actual heat transfer is zero. Dissipation generates entropy inside the liquid while work transfers energy across the boundary. Physical check Equal transferred energies as heat and work need not correspond to equal entropy transfers.

Question 4

Viscous stirring converts organized work into internal energy

A rigid insulated vessel contains liquid with constant heat capacity C=1000C=1000 J/K, initially at 300 K. A paddle supplies 6000 J of shaft work to the liquid. The paddle has no net energy storage. Use ΔS=Cln⁡(Tf/Ti)\Delta S=C\ln(T_f/T_i).

Diagram shown in the original SVG worksheet.

  1. Find final temperature and entropy change of the liquid.

  2. Compute the heat that a reversible heating path would transfer between the same endpoint temperatures. Explain why work input does not carry entropy into the actual insulated vessel.

Question 4 - Solution

Viscous stirring converts organized work into internal energy

Diagram shown in the original SVG worksheet.

(a) Method and calculation

Q=0,Wby=−6000J,C(Tf−300)=6000⇒Tf=306K.Q=0,\quad W_{\mathrm{by}}=-6000\,\mathrm J,\quad C(T_f-300)=6000\ \Rightarrow\ T_f=306\,\mathrm K.ΔS=1000ln⁡(306/300)≈19.8026J/K.\Delta S=1000\ln(306/300)\approx19.8026\,\mathrm{J/K}.

(b) Interpretation and further calculation

Qrev=∫300306CdT=6000J,∫δQrevT=Cln⁡(306/300).Q_{\mathrm{rev}}=\int_{300}^{306}C\,dT=6000\,\mathrm J,\quad\int\frac{\delta Q_{\mathrm{rev}}}T=C\ln(306/300).Sgenerated=ΔS−∫δQactualTb=19.8026J/K.S_{\mathrm{generated}}=\Delta S-\int\frac{\delta Q_{\mathrm{actual}}}{T_b}=19.8026\,\mathrm{J/K}.Actual heat transfer is zero. Dissipation generates entropy inside the liquid while work transfers energy across the boundary.

Physical check

Equal transferred energies as heat and work need not correspond to equal entropy transfers.