Physical Chemistry Lab Course

Vapor pressure

German version

Theory

The aim of this lab course is to obtain information regarding the behavior of a boiling pure substance.

Phase equilibrium of one-component systems

We consider the thermodynamic equilibrium of a system that consists of one component only (a pure substance). We say that the system is boiling if both a liquid and a gaseous phase exist simultaneously. In thermal equilibrium, the pressure, temperature and chemical potential of this pure substance is equal in each phase. We call the temperature boiling temperature  T_\text b.

The chemical potential of the pure substance \mu^\text l and \mu^\text g in the liquid and the gaseous phase of the system is the molar free enthalpy G_\text m^\text l and G_\text m^\text g.

\begin{aligned} && \mu^\text{l} &= \mu^\text{g}\qquad\qquad\\ &\Leftrightarrow& G_\text m^\text{l} &= G_\text m^\text{g}\\ &\Leftrightarrow& \mathrm dG_\text m^\text{l} &= \mathrm dG_\text m^\text{g} \end{aligned}

The total differential of the molar free enthalpy is

\mathrm dG_\text m^\text{l} = V_\text m^\text l \mathrm dp - S_\text m^\text l \mathrm dT_\text b
\mathrm dG_\text m^\text{g} = V_\text m^\text g \mathrm dp - S_\text m^\text g \mathrm dT_\text b

Here V_\text{m}^\text l and V_\text{m}^\text g are the molar volume and S_{\text m}^\text l as well as S_{\text m}^\text g are the molar entropy of the liquid and gaseous phase.

From equation , and follows that in thermal equilibrium

\mathrm dp=\frac{S_\text m^\text g-S_\text m^\text l}{V_\text{m}^\text g-V_\text{m}^\text l} \mathrm dT_\text b.

The difference between the molar entropy of the liquid and the gaseous phase is called molar evaporation entropy \Delta_\text{vap}S_\text{m}. The difference between the molar volume of the liquid and gaseous phase is called molar evaporation volume \Delta_\text{vap}V_\text{m}.

Vapor pressure curve

From the definition of the molar free enthalpy G_\text m = H_\text m-S_\text mT follows that

G_{\text{m}}^\text g = H_{\text{m}}^\text g -S_{\text{m}}^\text gT_\text b
\text{and}\qquad G_{\text{m}}^\text l = H_{\text{m}}^\text l -S_{\text{m}}^\text lT_\text b.

Since in thermal equilibrium the molar free enthalpy of each phase is equal, the difference between equations  and  yields

G_{\text{m}}^\text g-G_{\text{m}}^\text l = \underbrace{\left(H_{\text{m}}^\text g-H_{\text{m}}^\text l\right)}_{=\Delta_\text{vap}H_\text{m}} -\underbrace{\left(S_{\text{m}}^\text g-S_{\text{m}}^\text l\right)}_{=\Delta_\text{vap}S_\text{m}}T_\text b \stackrel{!}{=} 0

The difference between the molar enthalpy of the liquid and gaseous phase is called molar evaporation enthalpy \Delta_\text{vap}H_\text{m}.

This allows to express the molar evaporation entropy using the molar evaporation enthalpy:

\Delta_\text{vap}S_\text{m}=\frac{\Delta_\text{vap}H_\text{m}}{T_\text b}

The molar volume of the gaseous phase is typically significantly larger than the molar volume of the liquid phase:

\Delta_\text{vap}V \approx V_\text{m}^\text g

The molar volume of the gaseous phase can then be expressed by using the ideal gas equation

V_\text{m}^\text g = \frac{RT_\text b}{p}

The universal gas constant is R=8.314 \text J / (\text{mol} \text K) . Using equation , and in equation , we obtain the expression

\frac{1}{p}\mathrm dp = \frac{\Delta_\text{vap}H_\text{m}}{RT_\text b^2}\mathrm dT_\text b.

This differential equation can be solved by integration, if we approximate that the molar evaporation enthalpy does not depend on temperature. The lower integration bounds are set to a pressure p^\text{ref} at which the pure substance boils at a temperature of T_\text b^\text{ref}.

Interactive visualization of the August vapor pressure equation
\begin{aligned} \int_{p^\text{ref}}^{p}\frac{1}{p'}\mathrm dp' &= \int_{T^\text{ref}_\text b}^{T_\text b}\frac{\Delta_\text{vap}H_\text{m}}{RT_{\text b}'^2}\mathrm dT'_\text b\\ \Leftrightarrow\quad \ln{\left(\frac{p}{p^\text{ref}}\right)} &= \frac{\Delta_\text{vap}H_\text{m}}{R}\left(\frac{1}{T^\text{ref}_\text b}-\frac{1}{T^\text{\vphantom{ref}}_{\text b}}\right) \end{aligned}

Equation  is called August vapor pressure equation. The equation describes the dependency of the vapor pressure p of a pure substance as a function of temperature T_\text b. A plot of the vapor pressure p versus the boiling temperature T_\text b is called vapor pressure curve.

Pictet-Trouton rule

The Pictet-Trouton rule states that the evaporation entropy of most liquids is approximately equal. . This was discovered around the year 1900 from the physicist Trouton, who noticed that the quotient of evaporation enthalpy and boiling temperature (equation ) approximates roughly 88 J / (mol K). Here, the boiling temperature refers to a pressure of 1013 hPa. Thus, it follows that

\Delta_\text{vap}S_\text{m}=88 \text J / (\text{mol} \text K).

The Pictet-Trouton rule states that the molecular order for a phase transition from liquid to gas changes by a similar amount. Large deviations of the Pictet-Trouton rule are typically observed for liquids consisting of polar molecules (that form, for example, hydrogen bonds).

Experimental setup

Experimental setup
Experimental setup consisting of a three-jacket vessel (Dreimantelgefäß) connected with a cryostat (right) and diaphragm pump (left). The vessel can be opened using an air valve (Lufthahn) and a vapor valve (Dampfhahn).

The experimental setup consists of a three-jacket vessel with a temperature sensor and a pressure sensor. The inner vessel contains the liquid pure substance and is surrounded by a tempering jacket. A constant temperature is achieved using a thermostat. A further vacuum jacket surrounds the temperature jacket to reduce condensation of water from air. A diaphragm pump is used to remove air from the gaseous phase within the setup and to reduce the pressure within the setup to the vapor pressure of the substance.

Instructions

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Lab course instructions

Preparation

Measurement

Vapor pressure of acetone

Vapor pressure of ethanol

Clean up

Switch off the lower and upper unit of the cryostat, the magnet stirrer, the thermometer and the manometer. Leave the vessel open to allow residual liquid to evaporate. Do not clean the vessel with water.

Analysis

Analyse your data for acetone and ethanol using the following steps:

The literature values are

\begin{aligned} \Delta_\text{vap} H_\text{m,acetone}^\text{lit.}&= 29{.}10\,\text{kJ}\,/\,\text{mol}\\ \Delta_\text{vap} H_\text{m,ethanol}^\text{lit.} &= 38{.}56\,\text{kJ}\,/\,\text{mol}\\ T_\text{b,acetone}^\text{lit.} &=329{.}20\,\text K\\ T_\text{b,ethanol}^\text{lit.} &=351{.}44\,\text K \end{aligned}

Bibliography