Critical point (thermodynamics)
In physical chemistry, thermodynamics, chemistry and condensed matter physics, a critical point, also known as a critical state, occurs under conditions (such as specific values of temperature, pressure or composition) at which no phase boundaries exist. There are multiple types of critical points, including vapor–liquid critical points and liquid–liquid critical points.
- 1 Pure substances: vapor–liquid critical point
- 2 Mixtures: liquid–liquid critical point
- 3 In renormalization group theory
- 4 See also
- 5 Footnotes
- 6 References
- 7 External links
Pure substances: vapor–liquid critical point
The term critical point is sometimes used to specifically denote the vapor–liquid critical point of a material, above which distinct liquid and gas phases do not exist. As shown in the phase diagram to the right, this is the point at which the phase boundary between liquid and gas terminates. In water, the critical point occurs at around 647 K (374 °C; 705 °F) and 22.064 MPa (3200 PSIA or 218 atm).
As the substance approaches critical temperature, the properties of its gas and liquid phases converge, resulting in only one phase at the critical point: a homogeneous supercritical fluid. The heat of vaporization is zero at and beyond this critical point, and so no distinction exists between the two phases. On the PT diagram, the point at which critical temperature and critical pressure meet is called the critical point of the substance. Above the critical temperature, a liquid cannot be formed by an increase in pressure, even though a solid may be formed under sufficient pressure. The critical pressure is the vapor pressure at the critical temperature. The critical molar volume is the volume of one mole of material at the critical temperature and pressure.
Critical properties vary from material to material, and for many pure substances are readily available in the literature. Nonetheless, obtaining critical properties for mixtures is more challenging.
That is, the first and second partial derivatives of the pressure p with respect to the volume V are both zero, with the partial derivatives evaluated at constant temperature T. This relation can be used to evaluate two parameters for an equation of state in terms of the critical properties, such as the parameters a and b in the van der Waals equation, for which
where is the reduced temperature, is the reduced pressure, is the reduced volume, and is the universal gas constant.
Principle of corresponding states
Critical variables are useful for writing a varied equation of state that applies to all materials, similar to normalization. The principle of corresponding states indicates that substances at equal reduced pressures and temperatures have equal reduced volumes. This relationship is approximately true for many substances, but becomes increasingly inaccurate for large values of pr.
Table of liquid–vapor critical temperature and pressure for selected substances
|Substance||Critical temperature||Critical pressure (absolute)|
|Argon||−122.4 °C (150.8 K)||48.1 atm (4,870 kPa)|
|Ammonia||132.4 °C (405.5 K)||111.3 atm (11,280 kPa)|
|Bromine||310.8 °C (584.0 K)||102 atm (10,300 kPa)|
|Caesium||1,664.85 °C (1,938.00 K)||94 atm (9,500 kPa)|
|Chlorine||143.8 °C (416.9 K)||76.0 atm (7,700 kPa)|
|Ethanol||241 °C (514 K)||62.18 atm (6,300 kPa)|
|Fluorine||−128.85 °C (144.30 K)||51.5 atm (5,220 kPa)|
|Helium||−267.96 °C (5.19 K)||2.24 atm (227 kPa)|
|Hydrogen||−239.95 °C (33.20 K)||12.8 atm (1,300 kPa)|
|Krypton||−63.8 °C (209.3 K)||54.3 atm (5,500 kPa)|
|CH4 (methane)||−82.3 °C (190.8 K)||45.79 atm (4,640 kPa)|
|Neon||−228.75 °C (44.40 K)||27.2 atm (2,760 kPa)|
|Nitrogen||−146.9 °C (126.2 K)||33.5 atm (3,390 kPa)|
|Oxygen||−118.6 °C (154.6 K)||49.8 atm (5,050 kPa)|
|CO2||31.04 °C (304.19 K)||72.8 atm (7,380 kPa)|
|N2O||36.4 °C (309.5 K)||71.5 atm (7,240 kPa)|
|H2SO4||654 °C (927 K)||45.4 atm (4,600 kPa)|
|Xenon||16.6 °C (289.8 K)||57.6 atm (5,840 kPa)|
|Lithium||2,950 °C (3,220 K)||652 atm (66,100 kPa)|
|Mercury||1,476.9 °C (1,750.1 K)||1,720 atm (174,000 kPa)|
|Sulfur||1,040.85 °C (1,314.00 K)||207 atm (21,000 kPa)|
|Iron||8,227 °C (8,500 K)|
|Gold||6,977 °C (7,250 K)||5,000 atm (510,000 kPa)|
|Aluminium||7,577 °C (7,850 K)|
|Water||373.946 °C (647.096 K)||217.7 atm (22.06 MPa)|
The existence of a critical point was first discovered by Charles Cagniard de la Tour in 1822  and named by Thomas Andrews in 1869. He showed that CO2 could be liquefied at 31 °C at a pressure of 73 atm, but not at a slightly higher temperature, even under pressures as high as 3,000 atm.
Mixtures: liquid–liquid critical point
The liquid–liquid critical point of a solution, which occurs at the critical solution temperature, occurs at the limit of the two-phase region of the phase diagram. In other words, it is the point at which an infinitesimal change in some thermodynamic variable (such as temperature or pressure) will lead to separation of the mixture into two distinct liquid phases, as shown in the polymer–solvent phase diagram to the right. Two types of liquid–liquid critical points are the upper critical solution temperature (UCST), which is the hottest point at which cooling will induce phase separation, and the lower critical solution temperature(LCST), which is the coldest point at which heating will induce phase separation.
From a theoretical standpoint, the liquid–liquid critical point represents the temperature-concentration extremum of the spinodal curve (as can be seen in the figure to the right). Thus, the liquid–liquid critical point in a two-component system must satisfy two conditions: the condition of the spinodal curve (the second derivative of the free energy with respect to concentration must equal zero), and the extremum condition (the third derivative of the free energy with respect to concentration must also equal zero or the derivative of the spinodal temperature with respect to concentration must equal zero).
In renormalization group theory
The critical point is described by a conformal field theory. According to the renormalization group theory, the defining property of criticality is that the characteristic length scale of the structure of the physical system, also known as the correlation length ξ, becomes infinite. This can happen along critical lines in phase space. This effect is the cause of the critical opalescence that can be observed as binary fluid mixture approaches its liquid–liquid critical point.
In systems in equilibrium, the critical point is reached only by precisely tuning a control parameter. However, in some non-equilibrium systems, the critical point is an attractor of the dynamics in a manner that is robust with respect to system parameters, a phenomenon referred to as self-organized criticality.
- Conformal field theory
- Critical exponents
- Critical phenomena
- Critical points of the elements (data page)
- Joback method, Klincewicz method, Lydersen method (Estimation of critical temperature, pressure, and volume from molecular structure)
- Lower critical solution temperature
- Percolation thresholds
- Phase transition
- Rushbrooke inequality
- Scale invariance
- Self-organized criticality
- Supercritical fluid, Supercritical drying, Supercritical water oxidation, Supercritical fluid extraction
- Tricritical point
- Triple point
- Upper critical solution temperature
- Widom scaling
- Sven Horstmann, "Theoretische und experimentelle Untersuchungen zum Hochdruckphasengleichgewichtsverhalten fluider Stoffgemische für die Erweiterung der PSRK-Gruppenbeitragszustandsgleichung", Doktorarbeit, C.-v.-O. Universität Oldenburg, 2000
- International Association for the Properties of Water and Steam, 2007.
- P. Atkins and J. de Paula, Physical Chemistry, 8th ed. (W.H. Freeman 2006), p.21
- K.J. Laidler and J.H. Meiser, Physical Chemistry (Benjamin/Cummings 1982), p.27
- P.A. Rock, Chemical Thermodynamics (MacMillan 1969), p.123
- Cengel, Yunus A.; Boles, Michael A. (2002). Thermodynamics: an engineering approach. Boston: McGraw-Hill. pp. 91–93. ISBN 0-07-121688-X.
- Emsley, John (1991). The Elements ((Second Edition) ed.). Oxford University Press. ISBN 0-19-855818-X.
- Cengel, Yunus A.; Boles, Michael A. (2002). Thermodynamics: An Engineering Approach ((Fourth Edition) ed.). McGraw-Hill. p. 824. ISBN 0-07-238332-1.
- "Critical Temperature and Pressure". Purdue University. Retrieved 2006-12-19.
- Charles Cagniard de la Tour (1822) "Exposé de quelques résultats obtenu par l'action combinée de la chaleur et de la compression sur certains liquides, tels que l'eau, l'alcool, l'éther sulfurique et l'essence de pétrole rectifiée" (Presentation of some results obtained by the combined action of heat and compression on certain liquids, such as water, alcohol, sulfuric ether [i.e., diethyl ether], and distilled petroleum spirit), Annales de chimie et de physique, 21 : 127-132.
- Berche, B., Henkel, M., Kenna, R (2009) Critical phenomena: 150 years since Cagniard de la Tour. Journal of Physical Studies 13 (3) , pp. 3001-1-3001-4.
- Andrews, Thomas (1869) "The Bakerian lecture: On the continuity of the gaseous and liquid states of matter" Philosophical Transactions of the Royal Society (London), 159, 575-590; the term "critical point" appears on page 588.
- "Revised Release on the IAPWS Industrial Formulation 1997 for the Thermodynamic Properties of Water and Steam" (PDF). International Association for the Properties of Water and Steam. August 2007. Retrieved 2009-06-09.
- "Critical points for some common solvents". ProSciTech. Archived from the original on 2008-01-31.
- "Critical Temperature and Pressure". Department of Chemistry. Purdue University. Retrieved 2006-12-03.
- Hagen Kleinert and Verena Schulte-Frohlinde, Critical Properties of φ4-Theories, World Scientific (Singapur, 2001); Paperback ISBN 981-02-4658-7 (readable online here)