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CHM-06

Clausius–Clapeyron

ln(P2/P1) = −(ΔHvap/R)(1/T2 − 1/T1). Vapour pressure vs T.

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Phase changeClausius–Clapeyron

Governing equation

ln⁡P2P1=−ΔHvapR(1T2−1T1)\ln\dfrac{P_2}{P_1}=-\dfrac{\Delta H_{\mathrm{vap}}}{R}\left(\dfrac1{T_2}-\dfrac1{T_1}\right)

T2∈[200,500]T_2 \in \left[200, 500\right]

where

P_1
P at T1 (kPa)
T_1
T1 (K)
T_2
T2 (K)
\Delta H_{vap}
Enthalpy of vaporisation (kJ/mol)
P_2
P at T2 (kPa)

The figure, part by part

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CHM-06 · phase
00:0 / 00:08
①

Governing law — red

ln⁡P2P1=−ΔHvapR(1T2−1T1)\ln\dfrac{P_2}{P_1}=-\dfrac{\Delta H_{\mathrm{vap}}}{R}\left(\dfrac1{T_2}-\dfrac1{T_1}\right)

T2∈[200,500]T_2 \in \left[200, 500\right]

T2=200T_2 = 200P2=0.001P_2 = 0.001

②

Domain of the variable — blue

T_2_{\min} = 200,\quad T_2_{\max} = 500

T2∈[200,500]T_2 \in \left[200, 500\right]

T2=200T_2 = 200T2=200T_2 = 200

③

Response curve — green

ln⁡P2P1=−ΔHvapR(1T2−1T1)\ln\dfrac{P_2}{P_1}=-\dfrac{\Delta H_{\mathrm{vap}}}{R}\left(\dfrac1{T_2}-\dfrac1{T_1}\right)

T2∈[200,500]T_2 \in \left[200, 500\right]

T2=200T_2 = 200P2=0.001P_2 = 0.001

④

Rate of change — amber

dP2dT2\frac{\mathrm{d}P_2}{\mathrm{d}T_2}

T2∈[200,500]T_2 \in \left[200, 500\right]

T2=201.9T_2 = 201.9P2′=1.81×10−4P_2^{\prime} = 1.81\times 10^{-4}

Lecture brief

Historical brief

Ideal-gas law, van ’t Hoff, Nernst, Michaelis–Menten and Clausius–Clapeyron are physical chemistry’s working equations of equilibrium and rate. The lab is pressure, potential and kinetics. This sheet (CHM-06 — Clausius–Clapeyron) is the form associated with Clausius–Clapeyron. Working symbols: P1P_1, T1T_1, T2T_2, ΔHvap\Delta H_{vap} →\rightarrow P2P_2. Ideal vapour, neglected liquid volume, constant ΔHvap. The slope of ln P vs 1/T is −ΔHvap/R.

Purpose

Purpose: compute P2P_2 from P1P_1, T1T_1, T2T_2, ΔHvap\Delta H_{vap} in Physical chemistry via ln⁡P2P1=−ΔHvapR(1T2−1T1)\ln\dfrac{P_2}{P_1}=-\dfrac{\Delta H_{\mathrm{vap}}}{R}\left(\dfrac1{T_2}-\dfrac1{T_1}\right) ln(P2/P1) = −(ΔHvap/R)(1/T2 − 1/T1). Vapour pressure vs T. Use it when a real physical chemistry question must be answered in SI before a code check.

Live realistic example

In symbols

Live case. Given P1=101.300 kPaP_1 = 101.300\,\mathrm{kPa}, T1=373.000 KT_1 = 373.000\,\mathrm{K}, T2=353.000 KT_2 = 353.000\,\mathrm{K}, ΔHvap=40.700 kJ/mol\Delta H_{vap} = 40.700\,\mathrm{kJ/mol}, the governing relation ln⁡P2P1=−ΔHvapR(1T2−1T1)\ln\dfrac{P_2}{P_1}=-\dfrac{\Delta H_{\mathrm{vap}}}{R}\left(\dfrac1{T_2}-\dfrac1{T_1}\right) yields P2=48.161 kPaP_2 = 48.161\,\mathrm{kPa}. Two temperatures on the coexistence curve. Move a slider: the numbers are this situation, not a canned story.

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Inputs

Outputs

  • P at T2 P_248.161 kPa
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CHM-06 · phase
00:0 / 00:08

Narration of this film

Two temperatures on the coexistence curve.

Ideal vapour, neglected liquid volume, constant ΔHvap. The slope of ln P vs 1/T is −ΔHvap/R.

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