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The Clausius-Clapeyron relation, named after Rudolf Clausius and Émile Clapeyron, is a way of characterizing the phase transition between two phases of matter, such as solid and liquid. On a pressure-temperature (P-T) diagram, the line separating the two phases is known as the coexistence curve. The Clausius-Clapeyron relation gives the slope of this curve. Mathematically,

$\frac{\mathrm{d}P}{\mathrm{d}T} = \frac{L}{T\,\Delta V}$

where $d P / d T$ is the slope of the coexistence curve, $L$ is the latent heat, $T$ is the temperature, and $Δ V$ is the volume change of the phase transition.

1 Disambiguation
2 Derivation
3 Other derivation
4 Applications
- 4.1 Chemistry and Chemical Engineering
5 Example
6 See also
7 References
8 Bibliography

Disambiguation

The generalized equation given in the opening of this article is sometimes called the Clapeyron equation, while a less general form is sometimes called the Clausius-Clapeyron equation. The less general form neglects the magnitude of the specific volume of the liquid (or solid) state relative to that of the gas state and also approximates the specific volume of the gas state via the ideal gas law.¹^:509

Derivation

A typical phase diagram. The dotted line gives the anomalous behavior of water. The Clausius-Clapeyron relation can be used to (numerically) find the relationships between pressure and temperature for the phase change boundaries. Entropy and volume changes (due to phase change) are orthogonal to the plane of this drawing

Using the state postulate, take the specific entropy, $s$ , for a homogeneous substance to be a function of specific volume, $v$ , and temperature, $T$ .¹^:508

$d s = \frac{\partial s}{\partial v} d v + \frac {\partial s}{\partial T} d T$

During a phase change, the temperature is constant, so¹^:508

$d s = \frac{\partial s}{\partial v} d v$ .

Using the appropriate Maxwell relation gives¹^:508

$d s = \frac{\partial P}{\partial T} d v$ .

Since temperature and pressure are constant during a phase change, the derivative of pressure with respect to temperature is not a function of the specific volume.²³^{:57, 62 & 671} Thus the partial derivative may be changed into a total derivative and be factored out when taking an integral from one phase to another,¹^:508

$s_2 - s_1 = \frac{d P}{d T} (v_2 - v_1)$ ,

$\frac{d P}{d T} = \frac {s_2 - s_1}{v_2 - v_1} = \frac {\Delta s}{\Delta v}$ .

Δ

is used as an operator to represent the change in the variable that follows it—final (2) minus initial (1)

For a closed system undergoing an internally reversible process, the first law is

$d u = \delta q + \delta w = T d s - P d v\,$ .

Using the definition of specific enthalpy, $h$ , and the fact that the temperature and pressure are constant, we have¹^:508

$d u + P d v = d h = T ds \Rightarrow ds = \frac {d h}{T} \Rightarrow \Delta s = \frac {\Delta h}{T}$ .

After substitution of this result into the derivative of the pressure, one finds⁴¹^:508

$\frac{d P}{d T} = \frac {\Delta h}{T \Delta v} = \frac {\Delta H}{T \Delta V} = \frac {L}{T \Delta V}$ ,

where the shift to capital letters indicates a shift to extensive variables. This last equation is called the Clausius-Clapeyron equation, though some thermodynamics texts just call it the Clapeyron equation, possibly to distinguish it from the approximation below.

When the transition is to a gas phase, the final specific volume can be many times the size of the initial specific volume. A natural approximation would be to replace $Δ v$ with $v 2$ . Furthermore, at low pressures, the gas phase may be approximated by the ideal gas law, so that $v 2 = v g a s = R T / P$ , where R is the mass specific gas constant (forcing $h$ and $v$ to be mass specific). Thus,¹^:509

$\frac{d P}{d T} = \frac {P \Delta h}{T^2 R}$ .

This leads to a version of the Clausius-Clapeyron equation that is simpler to integrate:¹^:509

$\frac {d P}{P} = \frac {\Delta h}{R} \frac {dT}{T^2}$ ,

$\ln P = - \frac {\Delta h}{R} \frac {1}{T} + C$ , or³^:672

$\ln \frac {P_2}{P_1} = \frac {\Delta h}{R} \left ( \frac {1}{T_1} - \frac {1}{T_2} \right )$ .

C

is a constant of integration

These last equations are useful because they relate saturation pressure and saturation temperature to the enthalpy of phase change, without requiring specific volume data. Note that in this last equation, the subscripts 1 and 2 correspond to different locations on the pressure versus temperature phase lines. In earlier equations, they corresponded to different specific volumes and entropies at the same saturation pressure and temperature.

Other derivation

Suppose two phases, I and II, are in contact and at equilibrium with each other. Then the chemical potentials are related by $μ I = μ I I$ . Along the coexistence curve, we also have $dμ I = dμ I I$ . We now use the Gibbs-Duhem relation $dμ = - s d T + v d P$ , where $s$ and $v$ are, respectively, the entropy and volume per particle, to obtain

$-(s_I-s_{II}) \mathrm{d}T + (v_I-v_{II}) \mathrm{d}P = 0. \,$

Hence, rearranging, we have

$\frac{\mathrm{d}P}{\mathrm{d}T} = \frac{s_I-s_{II}}{v_I-v_{II}}.$

From the relation between heat and change of entropy in a reversible process δQ = T dS, we have that the quantity of heat added in the transformation is

$L= T (s_I-s_{II}). \,$

Combining the last two equations we obtain the standard relation.

Applications

Chemistry and Chemical Engineering

The Clausius-Clapeyron equation for the liquid-vapor boundary may be used in either of two equivalent forms.

$\ln \left(\frac{P_1}{P_2} \right) = \frac{\Delta H_\mathrm{vap}}{R}\left(\frac{1}{T_2} - \frac{1}{T_1} \right)$

where

$T 1$ and $P 1$ are a corresponding temperature (in kelvin or other absolute temperature units) and vapor pressure
$T 2$ and $P 2$ are the corresponding temperature and pressure at another point
$Δ H vap$ is the molar enthalpy of vaporization
$R$ is the gas constant (8.314 J mol^-1K^-1)

This can be used to predict the temperature at a certain pressure, given the temperature at another pressure, or vice versa. Alternatively, if the corresponding temperature and pressure is known at two points, the enthalpy of vaporization can be determined.

The equivalent formulation, in which the values associated with one P,T point are combined into a constant (the constant of integration as above), is

$\ln P = -\frac{\Delta H_\mathrm{vap}}{RT}+C$

For instance, if the p,T values are known for a series of data points along the phase boundary, then the enthalpy of vaporization may be determined from a plot of $ln P$ against $1 / T$ .

Notes:

As in the derivation above, the enthalpy of vaporization is assumed to be constant over the pressure/temperature range considered
Equivalent expressions for the solid-vapor boundary are found by replacing the molar enthalpy of vaporization by the molar enthalpy of sublimation, $Δ H sub$

Clausius-Clapeyron equations is given for typical atmospheric conditions as

$\frac{\mathrm{d}e_s}{\mathrm{d}T} = \frac{L_v e_s}{R_v T^2}$

where:

$e s$ is saturation water vapor pressure
$T$ is a temperature
$L v$ is latent heat of evaporation
$R v$ is water vapor gas constant.

One can solve this equation to give⁵

Example

One of the uses of this equation is to determine if a phase transition will occur in a given situation. Consider the question of how much pressure is needed to melt ice at a temperature $Δ T$ below 0 °C. We can assume

${\Delta P} = \frac{L}{T\,\Delta V} {\Delta T}$

and substituting in

L

= 3.34×10⁵ J/kg (latent heat of water),

T

= 273 K (absolute temperature), and

Δ V

= -9.05×10^-5 m³/kg (change in volume from solid to liquid),

we obtain

$\frac{\Delta P}{\Delta T}$ = -13.1 MPa/°C.

To provide a rough example of how much pressure this is, to melt ice at -7 °C (the temperature many ice skating rinks are set at) would require balancing a small car (mass = 1000 kg⁶) on a thimble (area = 1 cm²).

References

^ ^a ^b ^c ^d ^e ^f ^g ^h ⁱ Wark, Kenneth (1988) [1966]. "Generalized Thermodynamic Relationships" (in English). Thermodynamics (5th ed.). New York, NY: McGraw-Hill, Inc.. ISBN 0-07-068286-0.
^ Carl Rod Nave (2006). "PvT Surface for a Substance which Contracts Upon Freezing" (in English). HyperPhysics. Georgia State University. Retrieved on 2007-10-16.
^ ^a ^b Çengel, Yunus A.; Boles, Michael A. (1998) [1989] (in English). Thermodynamics - An Engineering Approach. McGraw-Hill Series in Mechanical Engineering (3rd ed.). Boston, MA.: McGraw-Hill. ISBN 0-07-011927-9.
^ Salzman, William R. (2001-08-21). "Clapeyron and Clausius-Clapeyron Equations" (in English). Chemical Thermodynamics. University of Arizona. Archived from the original on 2007-07-07. Retrieved on 2007-10-11.
^ American Meteorological Society - The Computation of Equivalent Potential Temperature
^ Zorina, Yana (2000). "Mass of a Car". The Physics Factbook.

Bibliography

M.K. Yau and R.R. Rogers, Short Course in Cloud Physics, Third Edition, published by Butterworth-Heinemann, January 1, 1989, 304 pages. EAN 9780750632157 ISBN 0-7506-3215-1

J.V. Iribarne and W.L. Godson, Atmospheric Thermodynamics, published by D. Reidel Publishing Company, Dordrecht, Holland, 1973, 222 pages

H.B. Callen, Thermodynamics and an Introduction to Thermostatistics, published by Wiley, 1985. ISBN 0-471-86256-8

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