It is possible to envision three-dimensional (3D) graphs showing three thermodynamic quantities. For example, for a single component, a 3D Cartesian coordinate type graph can show temperature (
T) on one axis, pressure (
p) on a second axis, and
specific volume (
v) on a third. Such a 3D graph is sometimes called a
p–
v–
T diagram. The equilibrium conditions are shown as curves on a curved surface in 3D with areas for solid, liquid, and vapor phases and areas where solid and liquid, solid and vapor, or liquid and vapor coexist in equilibrium. A line on the surface called a
triple line is where solid, liquid and vapor can all coexist in equilibrium. The critical point remains a point on the surface even on a 3D phase diagram. An
orthographic projection of the 3D
p–
v–
T graph showing pressure and temperature as the vertical and horizontal axes collapses the 3D plot into the standard 2D pressure–temperature diagram. When this is done, the solid–vapor, solid–liquid, and liquid–vapor surfaces collapse into three corresponding curved lines meeting at the triple point, which is the collapsed orthographic projection of the triple line.
Binary phase diagrams .Other much more complex types of phase diagrams can be constructed, particularly when more than one pure component is present. In that case,
concentration becomes an important variable. Phase diagrams with more than two dimensions can be constructed that show the effect of more than two variables on the phase of a substance. Phase diagrams can use other variables in addition to or in place of temperature, pressure and composition, for example the strength of an applied electrical or magnetic field, and they can also involve substances that take on more than just three states of matter. One type of phase diagram plots temperature against the relative concentrations of two substances in a
binary mixture called a
binary phase diagram, as shown at right. Such a
mixture can be either a
solid solution,
eutectic or
peritectic, among others. These two types of mixtures result in very different graphs. Another type of binary phase diagram is a
boiling-point diagram for a mixture of two components, i. e.
chemical compounds. For two particular
volatile components at a certain pressure such as
atmospheric pressure, a
boiling-point diagram shows what
vapor (gas) compositions are in
equilibrium with given liquid compositions depending on temperature. In a typical binary boiling-point diagram, temperature is plotted on a vertical axis and mixture composition on a horizontal axis. A two component diagram with components A and B in an "ideal" solution is shown. The construction of a liquid vapor phase diagram assumes an
ideal liquid solution obeying
Raoult's law and an ideal gas mixture obeying
Dalton's law of partial pressure. A tie line from the liquid to the gas at constant pressure would indicate the two compositions of the liquid and gas respectively. A simple example diagram with hypothetical components 1 and 2 in a non-
azeotropic mixture is shown at right. The fact that there are two separate curved lines joining the boiling points of the pure components means that the vapor composition is usually not the same as the liquid composition the vapor is in equilibrium with. See
Vapor–liquid equilibrium for more information. In addition to the above-mentioned types of phase diagrams, there are many other possible combinations. Some of the major features of phase diagrams include congruent points, where a solid phase transforms directly into a liquid. There is also the
peritectoid, a point where two solid phases combine into one solid phase during cooling. The inverse of this, when one solid phase transforms into two solid phases during cooling, is called the
eutectoid. A complex phase diagram of great technological importance is that of the
iron–
carbon system for less than 7% carbon (see
steel). The x-axis of such a diagram represents the concentration variable of the mixture. As the mixtures are typically far from dilute and their density as a function of temperature is usually unknown, the preferred concentration measure is
mole fraction. A volume-based measure like
molarity would be inadvisable.
Ternary phase diagrams A system with three components is called a ternary system. At constant pressure the maximum number of independent variables is three – the temperature and two concentration values. For a representation of ternary equilibria a three-dimensional phase diagram is required. Often such a diagram is drawn with the composition as a horizontal plane and the temperature on an axis perpendicular to this plane. To represent composition in a ternary system an equilateral triangle is used, called Gibbs triangle (see also
Ternary plot). File:Gibbs triangle-ternary plot.jpg|Gibbs triangle File:Space diagram of a three-component system.jpg|alt=Space diagram of a three-component system|Space phase diagram of a ternary system The temperature scale is plotted on the axis perpendicular to the composition triangle. Thus, the space model of a ternary phase diagram is a right-triangular prism. The prism sides represent corresponding binary systems A-B, B-C, A-C. However, the most common methods to present phase equilibria in a ternary system are the following: 1) projections on the concentration triangle ABC of the liquidus, solidus, solvus surfaces; 2) isothermal sections; 3) vertical sections.
Crystals Polymorphic and
polyamorphic substances have multiple
crystal or
amorphous phases, which can be graphed in a similar fashion to solid, liquid, and gas phases. pressure–temperature phase diagram of water. The
Roman numerals indicate various
ice phases.
Mesophases Some organic materials pass through intermediate states between solid and liquid; these states are called
mesophases. Attention has been directed to mesophases because they enable
display devices and have become commercially important through the so-called
liquid-crystal technology. Phase diagrams are used to describe the occurrence of mesophases. == See also ==