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Question: One mole of an ideal monatomic gas is taken round the cyclic process \(ABCA\) as shown in the figure...

One mole of an ideal monatomic gas is taken round the cyclic process ABCAABCA as shown in the figure, calculate the heat rejected by the gas in the path CACA and the heat absorbed by the gas in the path ABAB.

Explanation

Solution

The use of Cp{C_p} and Cv{C_v} will simplify the problem. Also, since CACA and ABAB processes are isobaric and isochoric respectively, equations can be used using these two properties of the gas in the respective paths.

Complete step by step solution:
Since the gas is monatomic, therefore the value of number of moles i.e. nn will be 11. The specific heat capacities at constant volume and constant pressure are:
Cv=32R{C_v} = \dfrac{3}{2}R
CvR=32\Rightarrow \dfrac{{{C_v}}}{R} = \dfrac{3}{2}
Cp=52R{C_p} = \dfrac{5}{2}R
CpR=52\Rightarrow \dfrac{{{C_p}}}{R} = \dfrac{5}{2}
Where Cp{C_p} and Cv{C_v} are the molar specific heat capacities of the gas at constant pressure and constant volume respectively of an ideal gas. Specific heat capacity of a substance is defined as the heat supplied per unit mass of that particular substance per unit rise in temperature.
Since the process CACA is isobaric i.e. the pressure remains constant throughout the process for this path, therefore the heat rejected by the gas in the path CACA will be:
dhCA=Cp(TfinalTinitial)\Rightarrow d{h_{CA}} = {C_p}({T_{final}} - {T_{initial}})
dhCA=Cp(P0V0R2P0V0R)\Rightarrow d{h_{CA}} = {C_p}(\dfrac{{{P_0}{V_0}}}{R} - \dfrac{{2{P_0}{V_0}}}{R})
dhCA=CpR(P0V02P0V0)\Rightarrow d{h_{CA}} = \dfrac{{{C_p}}}{R}({P_0}{V_0} - 2{P_0}{V_0})
dhCA=52(P0V02P0V0)\Rightarrow d{h_{CA}} = \dfrac{5}{2}({P_0}{V_0} - 2{P_0}{V_0})
Where dhCAd{h_{CA}} is the heat rejected during the process.
dhCA=52(P0V0)\Rightarrow d{h_{CA}} = - \dfrac{5}{2}({P_0}{V_0})
Since the process ABAB is isochoric, i.e. the volume remains constant throughout the process for this path, therefore the heat rejected by the gas in the path ABAB will be:
dhAB=CvdT\Rightarrow d{h_{AB}} = {C_v}dT
Where dhABd{h_{AB}} is the heat absorbed by the monatomic gas in the process ABAB.
dhAB=Cv(TfinalTinitial)\Rightarrow d{h_{AB}} = {C_v}({T_{final}} - {T_{initial}})
Cv(PfVfRPiViR)\Rightarrow {C_v}(\dfrac{{{P_f}{V_f}}}{R} - \dfrac{{{P_i}{V_i}}}{R})
CvR(PfVfPiVi)\Rightarrow \dfrac{{{C_v}}}{R}({P_f}{V_f} - {P_i}{V_i})
32(PfVfPiVi)\Rightarrow \dfrac{3}{2}({P_f}{V_f} - {P_i}{V_i})
32(3P0V0P0V0)\Rightarrow \dfrac{3}{2}(3{P_0}{V_0} - {P_0}{V_0})
3P0V0\Rightarrow 3{P_0}{V_0}
Therefore, the heat rejected by the gas in the path CACA is 52(P0V0) - \dfrac{5}{2}({P_0}{V_0}) and the heat absorbed by the gas in the path ABAB is 3P0V03{P_0}{V_0}.

Note: If the heat rejected in the path CACA is negative, then this implies that no heat is rejected in this process but there is heat absorption in the process. In the process ABAB no such negative sign is encountered therefore the process has absorbed heat.