Question 9

MCQHARD

Ten moles of an ideal monoatomic gas, initially in state aa at atmospheric pressure and temperature Ta=27∘CT_a = 27^\circ\text{C}, is enclosed in a metal cylinder of volume V0V_0 fitted with a frictionless piston. The gas is suddenly compressed to state bb with volume V0/3V_0/3. Now, keeping the piston stationary, the cylinder is submerged in a water bath of temperature 11∘C11^\circ\text{C} until the gas reaches the temperature of the water bath, which is denoted as state cc. Finally, while still in the water bath, the piston is brought slowly to its initial position, which is denoted as state ff. If RR is universal gas constant, then the correct option(s) is/are:

[Given: 91/3=2.089^{1/3} = 2.08]

(A)

The schematic P-V diagram of the processes described above is:

Option A
(B)

The change in internal energy in going from state aa to bb is 4860R4860R.

(C)

The net change in the internal energy in the whole process is −240R-240R.

(D)

The pressure and temperature of the state bb are 2.082.08 times the atmospheric pressure and 624 K624\text{ K}, respectively.

Detailed Solution

1. Process a→ba \to b (Sudden Compression): This is an adiabatic process. Given: n=10n = 10, Ta=27∘C=300 KT_a = 27^\circ\text{C} = 300\text{ K}, Va=V0V_a = V_0, Vb=V0/3V_b = V_0/3. For a monoatomic gas, γ=5/3\gamma = 5/3 and Cv=32RC_v = \frac{3}{2}R. Temperature at bb: Tb=Ta(VaVb)γ−1=300(3)5/3−1=300(3)2/3=300(9)1/3T_b = T_a \left(\frac{V_a}{V_b}\right)^{\gamma-1} = 300 (3)^{5/3 - 1} = 300 (3)^{2/3} = 300 (9)^{1/3} Given 91/3=2.089^{1/3} = 2.08, so Tb=300×2.08=624 KT_b = 300 \times 2.08 = 624\text{ K}. Pressure at bb: Pb=Pa(VaVb)γ=Pa(3)5/3=Pa×3×32/3=Pa×3×2.08=6.24PaP_b = P_a \left(\frac{V_a}{V_b}\right)^\gamma = P_a (3)^{5/3} = P_a \times 3 \times 3^{2/3} = P_a \times 3 \times 2.08 = 6.24 P_a. Since the pressure is 6.246.24 times the atmospheric pressure (not 2.082.08), Option (D) is incorrect.

Change in internal energy: ΔUab=nCv(Tb−Ta)=10×32R(624−300)=15R×324=4860R\Delta U_{ab} = n C_v (T_b - T_a) = 10 \times \frac{3}{2} R (624 - 300) = 15R \times 324 = 4860R. Option (B) is correct.

2. Process b→cb \to c (Isochoric Cooling): The piston is kept stationary, so the volume is constant at V0/3V_0/3. The temperature reaches the bath temperature, Tc=11∘C=284 KT_c = 11^\circ\text{C} = 284\text{ K}.

3. Process c→fc \to f (Isothermal Expansion): The piston is brought slowly to its initial volume while submerged in the water bath. Therefore, the temperature remains constant at Tf=Tc=284 KT_f = T_c = 284\text{ K} until the volume reaches Vf=V0V_f = V_0.

4. Net Internal Energy Change: The net change in internal energy depends only on the initial and final states of the entire process. ΔUnet=nCv(Tf−Ta)=10×32R(284−300)=15R(−16)=−240R\Delta U_{net} = n C_v (T_f - T_a) = 10 \times \frac{3}{2} R (284 - 300) = 15R (-16) = -240R. Option (C) is correct.

5. P-V Diagram Analysis:

  • a→ba \to b: Adiabatic compression (steep curve to the left, volume decreases).
  • b→cb \to c: Isochoric cooling (vertical line downwards, pressure drops at constant volume).
  • c→fc \to f: Isothermal expansion (flatter curve to the right, ending at V0V_0). Additionally, at the final state ff, Vf=VaV_f = V_a but Tf(284 K)<Ta(300 K)T_f (284\text{ K}) < T_a (300\text{ K}). Thus, Pf<PaP_f < P_a. The schematic correctly shows point ff lying below point aa on the same vertical volume line. Option (A) is correct.

**Correct Options: (A), (B), (C)**1. Process a→ba \to b (Sudden Compression): This is an adiabatic process. Given: n=10n = 10, Ta=27∘C=300 KT_a = 27^\circ\text{C} = 300\text{ K}, Va=V0V_a = V_0, Vb=V0/3V_b = V_0/3. For a monoatomic gas, γ=5/3\gamma = 5/3 and Cv=32RC_v = \frac{3}{2}R. Temperature at bb: Tb=Ta(VaVb)γ−1=300(3)5/3−1=300(3)2/3=300(9)1/3T_b = T_a \left(\frac{V_a}{V_b}\right)^{\gamma-1} = 300 (3)^{5/3 - 1} = 300 (3)^{2/3} = 300 (9)^{1/3} Given 91/3=2.089^{1/3} = 2.08, so Tb=300×2.08=624 KT_b = 300 \times 2.08 = 624\text{ K}. Pressure at bb: Pb=Pa(VaVb)γ=Pa(3)5/3=Pa×3×32/3=Pa×3×2.08=6.24PaP_b = P_a \left(\frac{V_a}{V_b}\right)^\gamma = P_a (3)^{5/3} = P_a \times 3 \times 3^{2/3} = P_a \times 3 \times 2.08 = 6.24 P_a. Since the pressure is 6.246.24 times the atmospheric pressure (not 2.082.08), Option (D) is incorrect.

Change in internal energy: ΔUab=nCv(Tb−Ta)=10×32R(624−300)=15R×324=4860R\Delta U_{ab} = n C_v (T_b - T_a) = 10 \times \frac{3}{2} R (624 - 300) = 15R \times 324 = 4860R. Option (B) is correct.

2. Process b→cb \to c (Isochoric Cooling): The piston is kept stationary, so the volume is constant at V0/3V_0/3. The temperature reaches the bath temperature, Tc=11∘C=284 KT_c = 11^\circ\text{C} = 284\text{ K}.

3. Process c→fc \to f (Isothermal Expansion): The piston is brought slowly to its initial volume while submerged in the water bath. Therefore, the temperature remains constant at Tf=Tc=284 KT_f = T_c = 284\text{ K} until the volume reaches Vf=V0V_f = V_0.

4. Net Internal Energy Change: The net change in internal energy depends only on the initial and final states of the entire process. ΔUnet=nCv(Tf−Ta)=10×32R(284−300)=15R(−16)=−240R\Delta U_{net} = n C_v (T_f - T_a) = 10 \times \frac{3}{2} R (284 - 300) = 15R (-16) = -240R. Option (C) is correct.

5. P-V Diagram Analysis:

  • a→ba \to b: Adiabatic compression (steep curve to the left, volume decreases).
  • b→cb \to c: Isochoric cooling (vertical line downwards, pressure drops at constant volume).
  • c→fc \to f: Isothermal expansion (flatter curve to the right, ending at V0V_0). Additionally, at the final state ff, Vf=VaV_f = V_a but Tf(284 K)<Ta(300 K)T_f (284\text{ K}) < T_a (300\text{ K}). Thus, Pf<PaP_f < P_a. The schematic correctly shows point ff lying below point aa on the same vertical volume line. Option (A) is correct.

Correct Options: (A), (B), (C)

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