Question 1. The diagram shows adiabats
AB and
CD, BC on the hot isotherm and
DA on the cold isotherm. The cycle runs clockwise. Along adiabat
AB, the adiabatic relation gives
TCVAγ−1=THVBγ−1,(VBVA)γ−1=TCTH.
Raising to the power 1/(γ−1) and setting b=(TH/TC)1/(γ−1) gives VA=bVB. Similarly, along CD,
THVCγ−1=TCVDγ−1⟹VD=bVC=brVB.
Thus VD/VA=(brVB)/(bVB)=r: the isotherms have the same volume ratio, traversed in opposite directions.
Question 2. Along each reversible adiabat,
δQrev=0 and
dS=δQrev/T=0:
QAB=QCD=0,ΔSAB=ΔSCD=0.
Along an ideal-gas isotherm, dU=0, so δQrev=PdV=nRTdV/V. For the expansion at the hot temperature,
QBCΔSBC=nRTH∫VBrVBVdV=nRTH[lnV]VBrVB=nRTHlnr>0,=THQBC=nRlnr.
For the compression at the cold temperature, VA/VD=1/r:
QDAΔSDA=nRTC∫VDVAVdV=nRTC[lnV]VDVA=nRTClnVDVA=−nRTClnr<0,=TCQDA=−nRlnr.
In the (S,T) diagram, entropy is constant along AB and CD: these branches are vertical. Isotherms BC and DA are horizontal. Taking SA as the relative origin, the coordinates are
StateABCDS−SA00nRlnrnRlnrTTCTHTHTC
This gives a clockwise rectangle of width nRlnr and height TH−TC.
Question 3. Over a cycle,
ΔU=0. Counting received energy as positive, the first law gives
W=−(QAB+QBC+QCD+QDA)=−nR(TH−TC)lnr<0.
The work delivered is −W>0 and the heat received from the hot reservoir is QBC>0. The efficiency is therefore
η=QBC−W=nRTHlnrnR(TH−TC)lnr=THTH−TC=1−THTC.
Each reservoir receives the opposite of the heat it supplies to the gas:
ΔSth,H=TH−QBC=−nRlnr,ΔSth,C=TC−QDA=nRlnr.
The gas returns to its initial state, so ΔSgas=0. The three changes sum to zero: no entropy is produced. Work delivered to the surroundings carries no entropy.
Question 4. Retain the received-energy sign convention for the machine:
QH>0 is the heat received from the hot reservoir,
QC<0 that received from the cold reservoir, and
W<0 the work received over a cycle. The reservoirs receive the opposite heats,
−QH and
−QC. Their total entropy change is the entropy produced, since the machine returns to its initial state and only work is transferred to the surroundings:
Si=−THQH−TCQC.
Multiplying by TC and isolating QC gives
TCSi=−THTCQH−QC,QC=−THTCQH−TCSi.
The first law gives 0=QH+QC+W. The recovered work is ∣W∣=−W=QH+QC, hence
η=QH∣W∣=1+QHQC=1−THTC−QHTCSi.
Since TC>0 and QH>0, positive entropy production reduces the efficiency.
Question 5. The heat received from the hot reservoir is the same for both engines. From question 2,
QH=nRTHlnr=1,0×8,314×500×ln3,4≃5087 J.
The reversible engine's efficiency is
ηCarnot=1−THTC=1−500300=0,40=40%.
Question 4 gives the difference between the two efficiencies:
Δη=ηCarnot−ηirr=QHTCSi≃5087300×2,0=0,118.
The numerator TCSi=600 J is an energy, so the ratio is dimensionless. The reduction is 100Δη≃11,8 percentage points. Thus,
ηirr=0,40−0,118≃0,282=28,2%.
The efficiency falls from 40% to 28,2%; a reduction of 11,8 points is not a relative reduction of 11,8%.