An Ellingham diagram is a graph showing the temperature dependence of the stability for compounds. This analysis is usually used to evaluate the ease of reduction of metal oxides and sulfides. These diagrams were first constructed by Harold Ellingham in 1944. In metallurgy, the Ellingham diagram is used to predict the equilibrium temperature between a metal, its oxide, and oxygen -- and by extension, reactions of a metal with sulfur, nitrogen, and other non-metals. The diagrams are useful in predicting the conditions under which an ore will be reduced to its metal. The analysis is thermodynamic in nature and ignores reaction kinetics. Thus, processes that are predicted to be favourable by the Ellingham diagram can still be slow.
Ellingham diagrams are a particular graphical form of the principle that the thermodynamic feasibility of a reaction depends on the sign of ?G, the Gibbs free energy change, which is equal to ?H - T?S, where ?H is the enthalpy change and ?S is the entropy change.
The Ellingham diagram plots the Gibbs free energy change (?G) for each oxidation reaction as a function of temperature. For comparison of different reactions, all values of ?G refer to the reaction of the same quantity of oxygen, chosen as one mole O ( mol ) by some authors and one mole by others. The diagram shown refers to 1 mole , so that for example the line for the oxidation of chromium shows ?G for the reaction Cr(s) + (g) -> (s), which is of the molar Gibbs energy of formation ?Gf°(, s).
In the temperature ranges commonly used, the metal and the oxide are in a condensed state (solid or liquid), and oxygen is a gas with a much larger molar entropy. For the oxidation of each metal, the dominant contribution to the entropy change (?S) is the removal of mol , so that ?S is negative and roughly equal for all metals. The slope of the plots  is therefore positive for all metals, with ?G always becoming more negative with lower temperature, and the lines for all the metal oxides are approximately parallel. Since these reactions are exothermic, they always become feasible at lower temperatures. At a sufficiently high temperature, the sign of ?G may invert (becoming positive) and the oxide can spontaneously reduce to the metal, as shown for Ag and Cu.
For oxidation of carbon, the red line is for the formation of CO: C(s) + (g) -> CO(g) with an increase in the number of moles of gas, leading to a positive ?S and a negative slope. The blue line for the formation of CO2 is approximately horizontal, since the reaction C(s) + (g) -> CO2(g) leaves the number of moles of gas unchanged so that ?S is small.
As with any chemical reaction prediction based on purely thermodynamic grounds, a spontaneous reaction may be very slow if one or more stages in the reaction pathway have very high activation energies EA.
If two metals are present, two equilibria have to be considered. The oxide with the more negative ?G will be formed and the other oxide will be reduced.
In industrial processes, the reduction of metal oxides is often effected by a carbothermic reaction, using carbon as a reducing agent. Carbon is available cheaply as coal, which can be rendered to coke. When carbon reacts with oxygen it forms the gaseous oxides carbon monoxide and carbon dioxide, so the thermodynamics of its oxidation is different from that for metals: its oxidation has a more negative ?G with higher temperatures (above 700 °C). Carbon can thus serve as reducing agent. Using this property, reduction of metals may be performed as a double redox reaction at relatively low temperature.
The main application of Ellingham diagrams is in the extractive metallurgy industry, where it helps to select the best reducing agent for various ores in the extraction process, purification and grade setting for steel manufacturing. It also helps to guide the purification of metals, especially the removal of trace elements. The direct reduction process for making iron rests firmly on the guidance of Ellingham diagrams, which show that hydrogen can alone reduce iron oxides to the metal.
In iron ore smelting, haematite gets reduced at the top of the furnace, where temperature is in the range 600 - 700 °C. The Ellingham diagram indicates that in this range carbon monoxide acts as a stronger reducing agent than carbon since the process
has a more-negative free energy change than the process:
In the upper part of the blast furnace, haematite is reduced by CO (produced by oxidation of coke lower down, at higher temperatures) even in the presence of carbon - though this is mainly because the kinetics for gaseous CO reacting with the ore are better.
The Ellingham curve for the reaction 2C(s) + (g) -> 2CO(g) slopes down and falls below the curves for all the metals. Hence, carbon can normally act as a reducing agent for all metal oxides at very high temperatures. But chromium formed at these temperatures reacts with carbon to form its carbide, which gives undesirable properties to the chromium metal obtained. Hence, for high temperature reduction of chromic oxide, carbon cannot be used.
The Ellingham curve for aluminium lies below the curves of most metals such chromium, iron, etc. This fact indicates that aluminium can be used as the reducing agent for oxides of all these metals. This result is illustrated as follows:
The second equation minus the first equation gives:
So aluminium oxide is more stable than chromium oxide (at least at normal temperatures, and in fact all the way up to the decomposition temperatures of the oxides). Since the Gibbs free energy change is negative, aluminium can reduce chromium oxide.