An azeotrope or azeotropic mixture ( Greek a- “not”, zeo- “boiling”, tropos “turning”, here in the sense of “change”) is a liquid consisting of two or more chemical compounds whose vapor phase has the same composition as the liquid phase. The mixture has a constant boiling point and cannot be separated by simple distillation ; so it behaves like a pure substance . Azeotropy is the opposite of zeotropy .
In azeotropic mixtures touch the p - x - phase diagram the boiling and condensation curves of the components in azeotropic mixture ratio. In the x - y diagram, the x = y line is intersected (see illustration).
Azeotropes form when the partial vapor pressures of the components of a mixed liquid deviate greatly from the vapor pressures resulting from Raoult's law for an ideal mixture . Two components (e.g. HCl / H 2 O), which interact more strongly with one another than in the pure substance, form an azeotrope with a vapor pressure minimum / boiling point maximum; the cohesion between HCl and H 2 O is greater than that between H 2 O molecules or HCl molecules. Two components, such as ethanol and water, which have weaker interactions with one another than in the pure substances, form an azeotrope with a vapor pressure maximum or boiling point minimum. This typically occurs when the components differ significantly in polarity .
Substances that are very similar to each other, such as the different alkanes , do not form azeotropes and can be separated cleanly by distillation. Mixtures of heavy and light water can also be separated by distillation via a column with a corresponding number of trays, despite the small distance between the boiling points.
Pressure minimum or pressure maximum
There are two different types of azeotropes:
- The positive azeotrope in the p, x diagram corresponds to the mixture of substances at the maximum of the vapor pressure . The boiling point of this mixture has a minimum in the T, x diagram and is below that of the pure substances involved. Examples of this are the ethanol / water and water / 1,4-dioxane systems .
- The negative azeotrope in the p, x diagram corresponds to the mixture of substances at the minimum of the vapor pressure. The boiling point of this mixture has a maximum in the T, x diagram and is higher than that of the pure substances involved. An example of this is the water / nitric acid system .
Heteroazeotrope or homogeneous azeotrope
In the case of components that do not completely dissolve in one another, there may be an azeotrope in the miscibility gap. In this case it is called a heteroazeotrope. In the event that the azeotropic composition is in the miscible range or the components can be mixed as required, this is referred to as a homogeneous azeotrope.
water / 1-pentanol
In the case of a heteroazeotrope, the liquid and the vapor do not have the same composition, since in the case of the azeotropic composition the liquid phase is unstable and breaks down into two phases. This property is used, for example, in azeotropic rectification , in order to separate an azeotropic mixture by means of a liquid-liquid phase separator.
A saddle azeotrope occurs only in ternary and higher mixtures. It is characterized by the fact that the ternary (or higher) azeotrope lies between the boiling points of the pure substances and thus forms neither a pressure maximum nor a pressure minimum azeotrope.
|T [K]||P [kPa]||x acetone [mol / mol]||x chloroform [mol / mol]||x methanol [mol / mol]||source|
In this system, all binary subsystems also form azeotropes, acetone / chloroform a pressure minimum, acetone / methanol and methanol / chloroform a pressure maximum azeotrope.
The term “saddle azeotrope” is derived directly from the shape of the three-dimensionally drawn vapor-liquid equilibrium.
Physical separation processes for azeotropes
Since azeotropic mixtures consist of components with very different properties (see above), they can usually be easily separated using other common separation methods besides distillation. Examples would be chromatography , addition of suitable molecular sieves or drying agents such as magnesium sulfate , crystallization of a component at low temperatures. The composition of the azeotrope can be changed in the desired direction by changing the pressure.
When an ethanol-water mixture is distilled several times, an azeotrope of approx. 96% ethanol and 4% water is obtained, which cannot be further separated by distillation and which boils at 78.17 ° C.
However, this azeotrope can be separated by adding a third component. When benzene is added, the water-ethanol mixture forms an azeotrope with three components (a ternary azeotrope ) that boils at 64.9 ° C. This water-benzene-ethanol mixture can now be distilled off and the water can thus be gradually dragged out of the liquid phase. What remains is a mixture of benzene and ethanol, from which the benzene can be separated off by normal distillation, so that anhydrous ethanol is obtained.
Vapor permeation and pervaporation
Another way to separate an azeotropic ethanol-water mixture is vapor permeation. The mixture is evaporated and passed through a membrane unit. The membrane works like a filter, i. In other words, their pores only allow one component to pass through - here the water. The driving force for the separation of the mixture is a pressure difference between the interior and the exterior and the selectivity of the membrane. Thus the water passes through the membrane (permeate) and the anhydrous ethanol remains on the other side of the membrane (retentate). So you can get ethanol with a purity of up to 99.97%.
In contrast to vapor permeation, in pervaporation the liquid mixture is led past the membrane.
The formation of azeotropes can be used to “drag out” a substance from a mixture. For example, in chemical reaction engineering, toluene is often used as an entrainer to separate water from a reaction mixture . Toluene forms a minimum azeotrope with water. The two liquids separate again in the condensate and form two phases. The toluene, the upper phase, is fed back into the reaction through a water separator . The water is separated off and the course of the reaction can be observed on the basis of the amount of water formed.
- Dortmund database - database for azeotropic and zeotropic systems
- Azeotropes, Non-Ideal Mixtures . (PDF; 139 kB) Paderborn University, on Heidelberg University's server
- Chemgapedia (animation)
- H. Lang: About the boiling equilibrium of the system methanol-acetone-chloroform. In: Z.Phys.Chem. (Leipzig). 196, 1950, pp. 278-297.