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Question: : A gas is enclosed in a cylinder with a movable frictionless piston. Its initial thermodynamics sta...

: A gas is enclosed in a cylinder with a movable frictionless piston. Its initial thermodynamics state at pressure Pi=105Pa{P_i} = {10^5}Pa and volume Vi=103m3{V_i} = {10^{ - 3}}{m^3} changes to a final state at Pf=132×105Pa{P_f} = \dfrac{1}{{32}} \times {10^5}Pa and Vf=8×103m3{V_f} = 8 \times {10^{ - 3}}{m^3} in an adiabatic quasi-static process such that P3V5=constant{P^3}{V^5} = {\rm{constant}}. Consider another thermodynamic process that brings the system from the same initial state to the same final state in two steps: an isobaric expansion at Pi{P_i} followed by an isochoric (isovolumetric) process at volume Vf{V_f}.The amount of heat supplied to the system in the two-step process is approximately:
A. 112J
B. 294J
C. 588J
D. 813J

Explanation

Solution

For an adiabatic process there is no heat exchange and to calculate heat from isobaric and isochoric(isovolumetric) process use molar heat capacity at constant pressure and molar heat capacity at constant volume and from the equation of adiabatic expansion you can find the ratio of molar heat capacity at constant pressure and molar heat capacity at constant volume.

Complete step by step answer:
Let look at the adiabatic equation, we have P3V5=constant{P^3}{V^5} = {\rm{constant}} which can be also written as PV53=constantP{V^{\dfrac{5}{3}}} = {\rm{constant}} therefore, γ=53\gamma = \dfrac{5}{3} from the value of γ\gamma we can find molar heat capacity at constant pressure and molar heat capacity at constant volume i.e; Cp&CV{C_p} \& {C_V}.
So, γ=CPCV=53\gamma = \dfrac{{{C_P}}}{{{C_V}}} = \dfrac{5}{3}
CP=52R&CV=32R\Rightarrow {C_P} = \dfrac{5}{2}R \& {C_V} = \dfrac{3}{2}R
Now will find heat supplied in both cases
For case(i) isobaric process
Heat supplied H1=nCPΔT{H_1} = n{C_P}\Delta T
H1=n52R(TfTi) H1=52(nRTfnRTi) H1=52(PiVfPiVi)\Rightarrow {H_1} = n\dfrac{5}{2}R({T_f} - {T_i})\\\ \Rightarrow {H_1} = \dfrac{5}{2}(nR{T_f} - nR{T_i})\\\ \Rightarrow {H_1} = \dfrac{5}{2}({P_i}{V_f} - {P_i}{V_i})
Putting value of pressure and volume we have value of heat supplied as
H1=52×105(81)103 H1=1750joule{H_1} = \dfrac{5}{2} \times {10^5}(8 - 1){10^{ - 3}}\\\ \Rightarrow{H_1}= 1750\,joule
For case(ii) isochoric(isovolumetric)
Heat supplied H2=nCVΔT{H_2} = n{C_V}\Delta T
H2=n32R(TfTi) H2=52(nRTfnRTi) H2=52(PfVfPiVf)\Rightarrow {H_2} = n\dfrac{3}{2}R({T_f} - {T_i})\\\ \Rightarrow {H_2} = \dfrac{5}{2}(nR{T_f} - nR{T_i})\\\ \Rightarrow {H_2} = \dfrac{5}{2}({P_f}{V_f} - {P_i}{V_f})
Putting values of pressure and temperature we have,
H2=32×8×103×(1321)105 H2=1162joule{H_2} = \dfrac{3}{2} \times 8 \times {10^{ - 3}} \times (\dfrac{1}{{32}} - 1){10^5}\\\ \Rightarrow{H_2}= - 1162 joule
Total heat supplied will be sum of these two hearts
H=H1+H2 H=1750+(1162) H=588jouleH = {H_1} + {H_2} \\\ \Rightarrow H= 1750 + ( - 1162) \\\ \therefore H= 588\,joule

Hence, the correct answer is Option C.

Note: Here expression of adiabatic expansion is given to help you find molar heat capacity at constant pressure and molar heat capacity at constant volume because you don’t know the which type of gas is it although you know it once you found the molar heat capacity at constant pressure and molar heat capacity at constant volume. Once you know these two heat capacities simply put the formula to get the final answer.