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Question: Find the efficiency of the cycle. ![](https://www.vedantu.com/question-sets/a438482c-26b2-4ccd-9db...

Find the efficiency of the cycle.

Explanation

Solution

Hint
To answer this question, we need to find the heat transfer and work done for all the three processes in the cycle. Then, we need to put these into the efficiency formula.
- PV=nRTPV = nRT , where PP is the pressure, VV is the volume, nn is the number of moles and TT is the temperature
- n=MM0n = \dfrac{M}{{{M_0}}} , where MM is the mass of the gas and M0{M_0} is the molar mass of the gas.
- Cp=γRγ1{C_p} = \dfrac{{\gamma R}}{{\gamma - 1}} , where Cp{C_p} is the heat capacity at constant pressure and γ=CpCv\gamma = \dfrac{{{C_p}}}{{{C_v}}}

Complete step by step answer
We know that the ideal gas equation is given by
PV=nRT\Rightarrow PV = nRT
We know that n=MM0n = \dfrac{M}{{{M_0}}} . Putting this in the ideal gas equation, we get
PV=MM0RT\Rightarrow PV = \dfrac{M}{{{M_0}}}RT
Dividing by VV we get
P=MVM0RT\Rightarrow P = \dfrac{M}{{V{M_0}}}RT
Now ρ=MV\rho = \dfrac{M}{V}
P=ρRTM0\therefore P = \dfrac{{\rho RT}}{{{M_0}}} (1)
Now, we calculate the temperatures at the three states given.
Applying (1) at the state 1, we get
P0=ρ0RT1M0\Rightarrow {P_0} = \dfrac{{{\rho _0}R{T_1}}}{{{M_0}}}
Separating T1{T_1} , we get
T1=P0M0ρ0R\Rightarrow {T_1} = \dfrac{{{P_0}{M_0}}}{{{\rho _0}R}}
Similarly, applying equation (1) on state 2 and state 3, we get
T2=P0M0ρ0R\Rightarrow {T_2} = \dfrac{{{P_0}{M_0}}}{{{\rho _0}R}}
T3=2P0M0ρ0R\Rightarrow {T_3} = \dfrac{{2{P_0}{M_0}}}{{{\rho _0}R}}
Now, for calculating the efficiency, we have to make the calculation for the work done and heat transfer for the three processes.
For process 121 - 2 :
T1=T2\because {T_1} = {T_2} so the process 121 - 2 is isothermal.
We know that for an isothermal process, the work done is given by
W=nRTloge(P1P2)\Rightarrow W = nRT{\log _e}\left( {\dfrac{{{P_1}}}{{{P_2}}}} \right)
Therefore work done for this process
W12=nRT1loge(P1P2)\Rightarrow {W_{1 - 2}} = nR{T_1}{\log _e}\left( {\dfrac{{{P_1}}}{{{P_2}}}} \right)
Substituting the values of T1{T_1} , P1&P2{P_1}\& {P_2}
W12=nRP0M0ρ0Rloge(P02P0)\Rightarrow {W_{1 - 2}} = nR\dfrac{{{P_0}{M_0}}}{{{\rho _0}R}}{\log _e}\left( {\dfrac{{{P_0}}}{{2{P_0}}}} \right)
On simplifying, we get
W12=nP0M0ρ0loge(12)\Rightarrow {W_{1 - 2}} = \dfrac{{n{P_0}{M_0}}}{{{\rho _0}}}{\log _e}\left( {\dfrac{1}{2}} \right)
We know that log(1x)=logx\log \left( {\dfrac{1}{x}} \right) = - \log x
W12=nP0M0ρ0loge2\therefore {W_{1 - 2}} = - \dfrac{{n{P_0}{M_0}}}{{{\rho _0}}}{\log _e}2 (2)
From the first law of thermodynamics, we have
Q=ΔU+W\Rightarrow Q = \Delta U + W
We know that ΔU=0\Delta U = 0 for an isothermal process, so we have
Q=W\Rightarrow Q = W
Q12=W12=nP0M0ρ0loge2\therefore {Q_{1 - 2}} = {W_{1 - 2}} = - \dfrac{{n{P_0}{M_0}}}{{{\rho _0}}}{\log _e}2 (3)
The negative sign shows that heat is released in this process.
For process 232 - 3 :
As we can see from the plot given, the process 232 - 3 is an isobaric process.
We know that work done in an isobaric process is given by
W=PΔV\Rightarrow W = P\Delta V (4)
From the ideal gas equation
PV=nRT\Rightarrow PV = nRT
Taking delta both the sides
PΔV+VΔP=nRΔT\Rightarrow P\Delta V + V\Delta P = nR\Delta T
For an isobaric process, we have ΔP=0\Delta P = 0
PΔV=nRΔT\Rightarrow \therefore P\Delta V = nR\Delta T
From (4), work done for an isobaric process
W=nRΔT\Rightarrow W = nR\Delta T
So, for the process 232 - 3
W23=nR(T3T2)\Rightarrow {W_{2 - 3}} = nR({T_3} - {T_2})
Putting the values of T2&T3{T_2}\& {T_3} , we get
W23=nR(2P0M0ρ0RP0M0ρ0R)\Rightarrow {W_{2 - 3}} = nR\left( {\dfrac{{2{P_0}{M_0}}}{{{\rho _0}R}} - \dfrac{{{P_0}{M_0}}}{{{\rho _0}R}}} \right)
W23=nRP0M0ρ0R\Rightarrow {W_{2 - 3}} = nR\dfrac{{{P_0}{M_0}}}{{{\rho _0}R}}
On simplifying, we get
W23=nP0M0ρ0\Rightarrow {W_{2 - 3}} = \dfrac{{n{P_0}{M_0}}}{{{\rho _0}}} (5)
Now, we know that heat transfer in an isobaric process is given by
Q=nCpΔT\Rightarrow Q = n{C_p}\Delta T
So, for the process 232 - 3
Q23=nCp(T3T2)\Rightarrow {Q_{2 - 3}} = n{C_p}({T_3} - {T_2})
Q23=nCp(2P0M0ρ0RP0M0ρ0R)\Rightarrow {Q_{2 - 3}} = n{C_p}\left( {\dfrac{{2{P_0}{M_0}}}{{{\rho _0}R}} - \dfrac{{{P_0}{M_0}}}{{{\rho _0}R}}} \right)
Simplifying, we get
Q23=nP0M0ρ0RCp\Rightarrow {Q_{2 - 3}} = \dfrac{{n{P_0}{M_0}}}{{{\rho _0}R}}{C_p} (6)
For process 313 - 1 :
From the plot, we can see that the density ρ\rho is constant for this process. For a fixed mass of the gas, the volume of the gas also has to be constant to make the density constant. So, the process 313 - 1 is an isochoric process.
We know that the work done in an isochoric process is zero.
W31=0\therefore {W_{3 - 1}} = 0 (7)
Also, the heat transfer in an isochoric process is given as
Q=nCvΔT\Rightarrow Q = n{C_v}\Delta T
Q31=nCv(T1T3)\therefore {Q_{3 - 1}} = n{C_v}({T_1} - {T_3})
Putting the values of T1&T3{T_1}\& {T_3}
Q31=nCv(P0M0ρ0R2P0M0ρ0R)\Rightarrow {Q_{3 - 1}} = n{C_v}\left( {\dfrac{{{P_0}{M_0}}}{{{\rho _0}R}} - \dfrac{{2{P_0}{M_0}}}{{{\rho _0}R}}} \right)
Q31=nP0M0ρ0RCv\Rightarrow {Q_{3 - 1}} = - \dfrac{{n{P_0}{M_0}}}{{{\rho _0}R}}{C_v} (8)
The negative sign shows that heat is released in this process.
Now, the efficiency, η=Total work doneTotal heat supplied\eta = \dfrac{{{\text{Total work done}}}}{{{\text{Total heat supplied}}}}
η=W12+W23+W31Q23\Rightarrow \eta = \dfrac{{{W_{1 - 2}} + {W_{2 - 3}} + {W_{3 - 1}}}}{{{Q_{2 - 3}}}}
Total work done, W=W12+W23+W31W = {W_{1 - 2}} + {W_{2 - 3}} + {W_{3 - 1}}
From (2), (5) and (7)
W=nP0M0ρ0loge2+nP0M0ρ0+0\Rightarrow W = - \dfrac{{n{P_0}{M_0}}}{{{\rho _0}}}{\log _e}2 + \dfrac{{n{P_0}{M_0}}}{{{\rho _0}}} + 0
W=nP0M0ρ0(1loge2)\Rightarrow W = \dfrac{{n{P_0}{M_0}}}{{{\rho _0}}}(1 - {\log _e}2)
Total heat supplied, Q=Q23Q = {Q_{2 - 3}}
From (6)
Q=nP0M0ρ0RCp\Rightarrow Q = \dfrac{{n{P_0}{M_0}}}{{{\rho _0}R}}{C_p}
η=WQ=nP0M0ρ0(1loge2)nP0M0ρ0RCp\therefore \eta = \dfrac{W}{Q} = \dfrac{{\dfrac{{n{P_0}{M_0}}}{{{\rho _0}}}(1 - {{\log }_e}2)}}{{\dfrac{{n{P_0}{M_0}}}{{{\rho _0}R}}{C_p}}}
Simplifying, we get
η=R(1loge2)γRγ1\therefore \eta = \dfrac{{R(1 - {{\log }_e}2)}}{{\dfrac{{\gamma R}}{{\gamma - 1}}}}
We know that Cp=γRγ1{C_p} = \dfrac{{\gamma R}}{{\gamma - 1}}
η=R(1loge2)γRγ1\therefore \eta = \dfrac{{R(1 - {{\log }_e}2)}}{{\dfrac{{\gamma R}}{{\gamma - 1}}}}
η=(γ1)(1loge2)γ\Rightarrow \eta = \dfrac{{(\gamma - 1)(1 - {{\log }_e}2)}}{\gamma }
Finally, we have
η=(11γ)(1loge2)\Rightarrow \eta = \left( {1 - \dfrac{1}{\gamma }} \right)(1 - {\log _e}2)

Note
We know that the efficiency cannot be more than or equal to one. It is always less than one. So, we should always check that the final expression of efficiency which we are getting should be less than unity. If it is more than unity, then this means that there is some mistake in the solution.