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Question: From the phase diagram of water and an aqueous solution containing non volatile solute, identify the...

From the phase diagram of water and an aqueous solution containing non volatile solute, identify the correct options:

A

At temperature T0T_0, vapour pressure of solid solvent and vapour pressure of liquid solvent will be same.

B

Order of vapour pressure (P0,P1,P2P_0, P_1, P_2) are P0>P1>P2P_0 > P_1 > P_2.

C

P0=P2eΔHfusionR[T0T1T0T1]P_0 = P_2e^{\frac{\Delta H_{fusion}}{R}[\frac{T_0 - T_1}{T_0 T_1}]}

D

P1=P2eΔHvapR[T0T1T0T1]P_1 = P_2e^{\frac{\Delta H_{vap}}{R}[\frac{T_0 - T_1}{T_0 T_1}]}

Answer

All options A, B, C, and D are correct.

Explanation

Solution

  1. Option A: For a pure solvent, at its triple point (which occurs at T0T_0), the vapor pressures of the solid and liquid phases are equal. Hence option A is correct.

  2. Option B: In the diagram, at the same temperature T0T_0 the vapor pressure of the solution (P1P_1) is lowered (due to the presence of the nonvolatile solute) compared to that of the pure solvent (P0P_0). Also, at a lower temperature T1 T_1 the vapor pressure on the solution curve is P2P_2 (with P2<P1P_2 < P_1). Thus, the order is P0>P1>P2P_0 > P_1 > P_2. Option B is correct.

  3. Option C: The freezing point depression is derived using the Clausius–Clapeyron relation (applied to the fusion process). It leads to:

    ln(P0P2)=ΔHfusionR(1T11T0)\ln\Big(\frac{P_0}{P_2}\Big) = \frac{\Delta H_{fusion}}{R}\left(\frac{1}{T_1} - \frac{1}{T_0}\right)

    Rewriting 1T11T0=T0T1T0T1\frac{1}{T_1} - \frac{1}{T_0} = \frac{T_0-T_1}{T_0T_1} gives:

    P0=P2exp[ΔHfusionRT0T1T0T1]P_0 = P_2 \exp\left[\frac{\Delta H_{fusion}}{R}\frac{T_0-T_1}{T_0T_1}\right]

    So, option C is correct.

  4. Option D: Similarly, applying the Clausius–Clapeyron equation to the vaporization process for the solution,

    ln(P1P2)=ΔHvapR(1T11T0)\ln\Big(\frac{P_1}{P_2}\Big) = \frac{\Delta H_{vap}}{R}\left(\frac{1}{T_1} - \frac{1}{T_0}\right)

    which rewrites to:

    P1=P2exp[ΔHvapRT0T1T0T1]P_1 = P_2 \exp\left[\frac{\Delta H_{vap}}{R}\frac{T_0-T_1}{T_0T_1}\right]

    Making option D also correct.