U2 M2 phase separations page 1 of 12 PHASE SEPARATIONS The evaporation of a liquid in a closed container Particles will gain kinetic energy and break away from the surface of the liquid. As the gaseous particles bounce around, some of them will hit the surface of the liquid again, and be trapped there. There will rapidly be an equilibrium set up in which the number of particles leaving the surface is exactly balanced by the number rejoining it. In this equilibrium, there will be a fixed number of the gaseous particles in the space above the liquid. When these particles hit the walls of the container, they exert a pressure. This pressure is called the saturated vapour pressure of the liquid. Saturated vapour pressure and boiling point A liquid boils when its saturated vapour pressure becomes equal to the external pressure on the liquid. If the liquid is in an open container and exposed to normal atmospheric pressure, the liquid boils when its saturated vapour pressure becomes equal to 1 atmosphere (or 101325 Pa or 101.325 kPa or 760 mmHg). This happens with water when the temperature reaches 100°C. But at different pressures, water will boil at different temperatures. For example, at the top of Mount Everest the pressure is so low that water will boil at about 70°C. Depressions from the Atlantic can easily lower the atmospheric pressure so that water will boil at 99°C - even lower with very deep depressions. Raoult's Law The vapour pressure of a solution with a non-volatile solute e.g. water with salt in it is equal to the vapour pressure of the pure solvent at that temperature multiplied by its mole fraction In equation form, this reads: p = xsolv x P0solv In this equation, Po is the vapour pressure of the pure solvent at a particular temperature. xsolv is the mole fraction of the solvent. You calculate this using: xsolv = moles of solvent / total number of moles Suppose you had a solution containing 10 moles of water and 0.1 moles of sugar. The total number of moles is therefore 10.1 The mole fraction of the water is: xwater = 10 / 10.1 = 0.99 U2 M2 phase separations page 2 of 12 Explanation of why Raoult's Law works Remember that saturated vapour pressure is what you get when a liquid is in a sealed container. An equilibrium is set up where the number of particles breaking away from the surface is exactly the same as the number sticking on to the surface again. Now suppose you added enough solute so that the solvent molecules only occupied 50% of the surface of the solution. If you reduce the number of solvent molecules on the surface, you are going to reduce the number which can escape in any given time. The net effect of this is that when equilibrium is established, there will be fewer solvent molecules in the vapour phase – which means that the saturated vapour pressure would be lower. Limitations of Raoult's Law Raoult's Law only works for ideal solutions. An ideal solution is defined as one which obeys Raoult's Law. Examples of ideal mixtures There is no such thing as an ideal mixture. However, some liquid mixtures get fairly close to being ideal. These are mixtures of two very closely similar substances. Common examples include: hexane and heptane benzene and methylbenzene propan-1-ol and propan-2-ol Ideal mixtures and enthalpy change of mixing If the temperature rises or falls when you mix the two liquids, then the mixture isn't ideal. Vapour pressure / composition diagrams Suppose you have an ideal mixture of two liquids A and B. Each of A and B is making its own contribution to the overall vapour pressure of the mixture. The greater the mole fraction, the greater the vapour pressure exerted. U2 M2 phase separations page 3 of 12 Using a boiling point / composition diagram B has the higher vapour pressure. That means that it will have the lower boiling point. Remember this inverse relationship!!!! If you boil a liquid mixture, you can find out the temperature it boils at, and the composition of the vapour over the boiling liquid. For example, in the next diagram, if you boil a liquid mixture C1, it will boil at a temperature T1 and the vapour over the top of the boiling liquid will have the composition C2. All you have to do is to use the liquid composition curve to find the boiling point of the liquid, and then look at what the vapour composition would be at that temperature. Notice again that the vapour is much richer in the more volatile component B than the original liquid mixture was. The beginnings of fractional distillation Suppose that you collected and condensed the vapour over the top of the boiling liquid and reboiled it. You would now be boiling a new liquid which had a composition C2. That would boil at a new temperature T2, and the vapour over the top of it would have a composition C3. If you keep on doing this (condensing the vapour, and then reboiling the liquid produced) you will eventually get pure B U2 M2 phase separations page 4 of 12 Please note Raoult's Law only works for ideal mixtures. In these, the forces between the particles in the mixture are exactly the same as those in the pure liquids. The tendency for the particles to escape is the same in the mixture and in the pure liquids. That is NOT TRUE in non-ideal mixtures. Positive deviations from Raoult's Law In mixtures showing a positive deviation from Raoult's Law, the vapour pressure of the mixture is always higher than you would expect from an ideal mixture. The deviation can be small or it may be large. Large deviations shown a very distorted curve as shown below. REMEMBER HIGHER VAPOUR PRESSURE MEANS LOWER BOILING POINT! Notice that mixtures over a range of compositions have higher vapour pressures than either pure liquid. The maximum vapour pressure is no longer that of one of the pure liquids. Explanation The fact that the vapour pressure is higher than ideal in these mixtures means that molecules are breaking away more easily than they do in the pure liquids. That is because the intermolecular forces between molecules of A and B are less than they are in the pure liquids. The classic example of a mixture of this kind is ethanol and water. This produces a highly distorted curve with a maximum vapour pressure for a mixture containing 95.6% of ethanol by mass. U2 M2 phase separations page 5 of 12 Negative deviations from Raoult's Law In exactly the same way, you can have mixtures with vapour pressures which are less than would be expected by Raoult's Law. In some cases, the deviations are small, but in others they are much greater giving a minimum value for vapour pressure lower than that of either pure component. Explanation These are cases where the molecules break away from the mixture less easily than they do from the pure liquids. New stronger forces must exist in the mixture than in the original liquids. The example of a major negative deviation is a mixture of nitric acid and water. A large positive deviation from Raoult's Law: ethanol and water mixtures If a mixture has a high vapour pressure it means that it will have a low boiling point. The molecules are escaping easily and you won't have to heat the mixture much to overcome the intermolecular attractions completely. The implication of this is that the boiling point / composition curve will have a minimum value lower than the boiling points of either A or B. U2 M2 phase separations page 6 of 12 Suppose you are going to distil a mixture of ethanol and water with composition C 1 as shown on the next diagram. It will boil at a temperature given by the liquid curve and produce a vapour with composition C2. . If you reboil that, it will produce a new vapour with composition C3. You can see that if you carried on with this boiling-condensing-reboiling sequence, you would eventually end up with a vapour with a composition of 95.6% ethanol. If you condense that you obviously get a liquid with 95.6% ethanol. This particular mixture of ethanol and water boils as if it were a pure liquid. It has a constant boiling point, and the vapour composition is exactly the same as the liquid. It is known as a constant boiling mixture or an azeotropic mixture or an azeotrope. A large negative deviation from Raoult's Law: nitric acid and water mixtures Nitric acid and water form mixtures in which particles break away to form the vapour with much more difficulty than in either of the pure liquids. In the case of mixtures of nitric acid and water, there is a maximum boiling point of 120.5°C when the mixture contains 68% by mass of nitric acid. That compares with the boiling point of pure nitric acid at 86°C, and water at 100°C. U2 M2 phase separations page 7 of 12 Start with a dilute solution of nitric acid with a composition of C1 and trace through what happens. The vapour produced is richer in water than the original acid. If you condense the vapour and reboil it, the new vapour is even richer in water. Fractional distillation of dilute nitric acid will enable you to collect pure water from the top of the fractionating column. As the acid loses water, it becomes more concentrated. Its concentration gradually increases until it gets to 68% by mass of nitric acid. At that point, the vapour produced has exactly the same concentration as the liquid, because the two curves meet. You produce a constant boiling mixture (or azeotropic mixture or azeotrope). If you distil dilute nitric acid, that's what you will eventually be left with in the distillation flask. You can't produce pure nitric acid from the dilute acid by distilling it. Distilling nitric acid more concentrated than 68% by mass This time you are starting with a concentration C2 to the right of the azeotropic mixture. U2 M2 phase separations page 8 of 12 The vapour formed is richer in nitric acid. If you condense and reboil this, you will get a still richer vapour. If you continue to do this all the way up the fractionating column, you can get pure nitric acid out of the top. As far as the liquid in the distillation flask is concerned, it is gradually losing nitric acid. Its concentration drifts down towards the azeotropic composition. Once it reaches that, there can't be any further change, because it then boils to give a vapour with the same composition as the liquid. Distilling a nitric acid / water mixture containing more than 68% by mass of nitric acid gives you pure nitric acid from the top of the fractionating column and the azeotropic mixture left in the distillation flask. Immiscible liquids If you have two immiscible liquids in a closed flask and keep everything still, the vapour pressure you measure will simply be the vapour pressure of the one which is floating on top. There is no way that the bottom liquid can turn to vapour. The top one is sealing it in. For the purposes of the rest of this topic, we always assume that the mixture is being stirred or agitated in some way so that the two liquids are broken up into drops. At any one time there will be drops of both liquids on the surface. That means that both of them contribute to the overall vapour pressure of the mixture. Total vapour pressure of the mixture Assuming that the mixture is being agitated, then both of the liquids will be in equilibrium with their vapours. The total vapour pressure is then simply the sum of the individual vapour pressures: . . . where po refers to the saturated vapour pressure of the pure liquid. Notice that this is independent of the amount of each sort of liquid present. All you need is enough of each so that both can exist in equilibrium with their vapour. For example, phenylamine and water can be treated as if they were completely immiscible. At 98°C, the saturated vapour pressures of the two pure liquids are: phenylamine 7.07 kPa water 94.30 kPa The total vapour pressure of an agitated mixture would just be the sum of these - in other words, 101.37 kPa U2 M2 phase separations page 9 of 12 Boiling point of the mixture Liquids boil when their vapour pressure becomes equal to the external pressure. Normal atmospheric pressure is 101.325 kPa. Compare that with the figure we have just got for the total vapour pressure of a mixture of water and phenylamine at 98°C. Its total vapour pressure is fractionally higher than the normal external pressure. This means that such a mixture would boil at a temperature just a shade less than 98°C - in other words lower than the boiling point of pure water (100°C) and much lower than the phenylamine (184°C). Exactly the same sort of argument could be applied to any other mixture of immiscible liquids. Important conclusion Agitated mixtures of immiscible liquids will boil at a temperature lower than the boiling point of either of the pure liquids. Their combined vapour pressures are bound to reach the external pressure before the vapour pressure of either of the individual components get there. Steam distillation This exploits the concept shown above and allows for organic compounds which would normally decompose at high temperatures, to be separated at lower temperatures minimising decomposition. Steam is blown through the mixture and the water and phenylamine turn to vapour. This vapour can be condensed and collected. The steam can be generated by heating water in another flask (or something similar). As the hot steam passes through the mixture it condenses, releasing heat. This will be enough to boil the mixture of water and phenylamine at 98°C provided the volume of the mixture isn't too great. For large volumes, it is better to heat the flask as well to avoid having to condense too much steam and increase the volume of liquid in the flask too much. Steam distillation allows separation of components which would decompose at high temperatures usually organic compounds. Vacuum distillation operates via the use of low pressures allowing components to be separated which would otherwise decompose at high temperatures. Some other applications of steam distillation Steam distillation can be used to extract some natural products - for example, to extract eucalyptus oil from eucalyptus, citrus oils from lemon or orange peel, and to extract oils used in perfumes from various plant materials. U2 M2 phase separations page 10 of 12 Calculations involving steam distillation The ratio of the moles of two liquids in the distillate is equal to the ratio of their vapour pressures e.g. phenylamine and water. NB A means phenylamine and W means water nA nW = If pA = 3.99 x 103 Pa and pW = 9.70 x 104 Pa, then ratio of the amounts = 4.11 x 10-2 pA pW If the amount of water produced is 1 g and the amount of phenylamine is 0.212 g, and the molar mass of water is 18g, what is the molar mass of phenylamine? Note nW = mass of water (mW) AND molar mass of water (MW) mA / (MA) mW / MW 0.212 x M 18 1 = 4.11 x 10-2 nA = mass of phenylamine (mA) molar mass of phenylamine (M A) 0.212 / M 1/ 18 = 4.11 x 10-2 = 4.11 x 10-2 Therefore M = 0.212 x 18 4.11 x 10-2 = 92.8 g = 93 g Solvent extraction One solvent can be used to extract a solute from another solvent. This process is called solvent extraction and this technique is very useful for extracting organic or even inorganic solutes. For example, if iodine crystals are placed in water and then a solvent like ether is added to the mixture and shaken in a separating funnel and left for a few hours for equilibrium to be established, the majority of the iodine crystals would be found in the non-aqueous layer. The ratio of the amounts of solute found in each layer is a constant and this is called the partition coefficient. partition coefficient (k) = CU CU = concentration of solute in upper layer CL CL = concentration of solute in lower layer Using the separating funnel, the lower layer is run off and collected and the solute then separated from the solvent. Sample calculation The mass of iodine used in 0.9656 g and 50 cm3 each of water and ether was used in the solvent extraction. After equilibrium was established, it was found that the upper layer contained 0.0112 g and the lower layer contained 0.9544 g. What is the partition coefficient for this system? CU / CL = 0.0112 / 0.9544 = 1.17 x 10-2 Examples of the application of distillation methods used in various industries such as petroleum, rum and fragrance industries. U2 M2 phase separations Questions page 11 of 12 U2 M2 phase separations page 12 of 12