1 00:00:00 --> 00:00:01 2 00:00:01 --> 00:00:02 The following content is provided under a Creative 3 00:00:02 --> 00:00:03 Commons license. 4 00:00:03 --> 00:00:06 Your support will help MIT OpenCourseWare continue to 5 00:00:06 --> 00:00:10 offer high quality educational resources for free. 6 00:00:10 --> 00:00:13 To make a donation or view additional materials from 7 00:00:13 --> 00:00:16 hundreds of MIT courses, visit MIT OpenCourseWare 8 00:00:16 --> 00:00:20 at ocw.mit.edu. 9 00:00:20 --> 00:00:24 PROFESSOR: Alright, so last time we started talking about 10 00:00:24 --> 00:00:30 more complicated mixtures. 11 00:00:30 --> 00:00:32 To get into colligative properties. 12 00:00:32 --> 00:00:38 And the example we gave was a binary system that 13 00:00:38 --> 00:00:43 has two components. 14 00:00:43 --> 00:00:49 And two phases. 15 00:00:49 --> 00:00:54 So we have a liquid phase on the bottom. 16 00:00:54 --> 00:00:59 A gas phase on top, and two components, A and B, where 17 00:00:59 --> 00:01:05 compositions xA and xB are in the liquid phase. 18 00:01:05 --> 00:01:06 Those are the mole fractions. 19 00:01:06 --> 00:01:14 And yA and yB in the gas phase, the mole fractions 20 00:01:14 --> 00:01:17 in the gas phase. 21 00:01:17 --> 00:01:22 And what we did last time was to begin to say how many 22 00:01:22 --> 00:01:25 degrees of freedom do we have, how many variables do we need 23 00:01:25 --> 00:01:28 to completely describe this mixture. 24 00:01:28 --> 00:01:30 And it turned out that for this mixture, we only 25 00:01:30 --> 00:01:32 needed two variables. 26 00:01:32 --> 00:01:34 Two degrees of freedom. 27 00:01:34 --> 00:01:37 We started out with four variables; the temperature, the 28 00:01:37 --> 00:01:48 pressure, and the components in the composition in the liquid 29 00:01:48 --> 00:01:51 phase and the composition in the gas phase. 30 00:01:51 --> 00:01:54 We need one of these, either xA or xB, and one of these, 31 00:01:54 --> 00:01:57 either yA or yB because they add up to 1. 32 00:01:57 --> 00:02:01 So you start with four, but because you are in a mixture, 33 00:02:01 --> 00:02:03 an equilibrium, you have constraints. 34 00:02:03 --> 00:02:10 You have the chemical potentials that have to 35 00:02:10 --> 00:02:11 be equal to each other. 36 00:02:11 --> 00:02:14 The chemical potential of A in the gas phase has to be equal 37 00:02:14 --> 00:02:16 to the chemical potential of A in the liquid phase. 38 00:02:16 --> 00:02:20 And the chemical potential of B in the gas phase has to B equal 39 00:02:20 --> 00:02:22 to the chemical potential of B in the liquid phase. 40 00:02:22 --> 00:02:25 So you start with four variables. 41 00:02:25 --> 00:02:32 Temperature, pressure, xA, yA, then you have the constraints 42 00:02:32 --> 00:02:38 that mu A, in the liquid phase has to be equal to mu 43 00:02:38 --> 00:02:40 A in the gas phase. 44 00:02:40 --> 00:02:42 Because you're at equilibrium. 45 00:02:42 --> 00:02:46 And mu B in the liquid phase has to be equal to mu 46 00:02:46 --> 00:02:48 B in the gas phase. 47 00:02:48 --> 00:02:52 So four minus two constraints means you have two 48 00:02:52 --> 00:02:54 degrees of freedom. 49 00:02:54 --> 00:02:58 And so if you want to know everything about this mixture, 50 00:02:58 --> 00:03:02 all you need is the temperature and the total pressure. 51 00:03:02 --> 00:03:02 And that's enough. 52 00:03:02 --> 00:03:05 It's kind of amazing. 53 00:03:05 --> 00:03:09 Give me the temperature and pressure and these two 54 00:03:09 --> 00:03:12 components, like water and alcohol, for instance, and 55 00:03:12 --> 00:03:17 I can tell you everything about the compositions. 56 00:03:17 --> 00:03:18 It's very powerful. 57 00:03:18 --> 00:03:20 And then we said that this turned out to be a special 58 00:03:20 --> 00:03:26 case, or sub-case of the more general Gibbs phase rule. where 59 00:03:26 --> 00:03:38 the Gibbs phase rule tells you that if you have C components, 60 00:03:38 --> 00:03:42 in this case here we have two, and the general case of C 61 00:03:42 --> 00:03:46 components with p phases, the number of degrees of freedom 62 00:03:46 --> 00:03:47 is C minus p plus two. 63 00:03:47 --> 00:03:54 This is components. 64 00:03:54 --> 00:03:57 And phases. 65 00:03:57 --> 00:03:59 And where we're going to start today is by proving this. 66 00:03:59 --> 00:04:04 And then we'll do more with this problem here. 67 00:04:04 --> 00:04:08 So the first thing is for us to prove Gibbs' phase rule. 68 00:04:08 --> 00:04:10 So Gibbs phase rule. 69 00:04:10 --> 00:04:13 We start out with all the variables that we have. 70 00:04:13 --> 00:04:16 And then we add the constraints. 71 00:04:16 --> 00:04:20 And for the Gibbs phase rule, then we start with the two 72 00:04:20 --> 00:04:22 knobs that we can turn externally. 73 00:04:22 --> 00:04:24 Which are the temperature and the pressure. 74 00:04:24 --> 00:04:26 So we start with temperature and pressure, as two 75 00:04:26 --> 00:04:28 variables that we have. 76 00:04:28 --> 00:04:29 And then we have a bunch of phases. 77 00:04:29 --> 00:04:30 We have C phases. 78 00:04:30 --> 00:04:34 And in each phase we have to describe the composition 79 00:04:34 --> 00:04:36 in that phase. 80 00:04:36 --> 00:04:42 So, for each phase alpha, we have to describe 81 00:04:42 --> 00:04:44 its mole fraction. 82 00:04:44 --> 00:04:47 So here we needed to describe xA for phase A. 83 00:04:47 --> 00:04:51 And yA for phase A. 84 00:04:51 --> 00:04:53 For component A in the gas phase. 85 00:04:53 --> 00:04:59 So now we have alpha components. 86 00:04:59 --> 00:05:05 And for each component we have to describe its mole fraction 87 00:05:05 --> 00:05:07 in that particular phase. 88 00:05:07 --> 00:05:12 So we have to describe x sub i. 89 00:05:12 --> 00:05:15 But we have a constraint on that. 90 00:05:15 --> 00:05:18 The constraint is that the sum of all the mole factions 91 00:05:18 --> 00:05:19 has to be equal to one. 92 00:05:19 --> 00:05:20 That's what it is, to be a mole fraction. 93 00:05:20 --> 00:05:24 So the constraint is that x sub i, i from one to 94 00:05:24 --> 00:05:30 alpha, is equal to one. 95 00:05:30 --> 00:05:36 So the constraint on the number of the components, instead of 96 00:05:36 --> 00:05:42 having, actually, i goes from one to C, because that's 97 00:05:42 --> 00:05:46 the number components. 98 00:05:46 --> 00:05:51 So instead of having C different compositions that 99 00:05:51 --> 00:05:54 we need to take care of, we only need C minus one. 100 00:05:54 --> 00:05:56 Just like here we only needed one, just xA. 101 00:05:56 --> 00:05:58 We didn't need both xA and xB, because we knew the 102 00:05:58 --> 00:06:00 sum was equal to one. 103 00:06:00 --> 00:06:05 So that means that we really need C minus one variables to 104 00:06:05 --> 00:06:10 describe the composition in one of the phases. 105 00:06:10 --> 00:06:16 But we have p phases, so let me fix this. 106 00:06:16 --> 00:06:19 We had C components. 107 00:06:19 --> 00:06:21 We have p phases. 108 00:06:21 --> 00:06:24 And so for each phase, we have to describe the composition. 109 00:06:24 --> 00:06:27 So that means that we need p times C minus one variables to 110 00:06:27 --> 00:06:31 describe all the components and all the phases, plus 111 00:06:31 --> 00:06:33 these extra two. 112 00:06:33 --> 00:06:38 So the total number variables then that we start out with 113 00:06:38 --> 00:06:41 before putting the fact that we're in equilibrium, is 114 00:06:41 --> 00:06:47 going to be two plus p times C minus one. 115 00:06:47 --> 00:06:49 So that's a basic description of the system. 116 00:06:49 --> 00:06:51 Then we put in the same constraints 117 00:06:51 --> 00:06:52 that we had up here. 118 00:06:52 --> 00:06:58 In terms of the chemical potentials. 119 00:06:58 --> 00:07:00 If I take any of the components, let's take 120 00:07:00 --> 00:07:03 the alpha component, or the i'th component. 121 00:07:03 --> 00:07:07 Because it's in equilibrium, the chemical potential of that 122 00:07:07 --> 00:07:12 particular component has to be the same in all the phases. 123 00:07:12 --> 00:07:14 So let's take the i'th component. 124 00:07:14 --> 00:07:21 So yi in phase one has to be equal to yi in phase two, has 125 00:07:21 --> 00:07:24 to be equal to yi in phase three, has to be equal 126 00:07:24 --> 00:07:33 to yi in phase p. 127 00:07:33 --> 00:07:35 All the chemical potentials have to be the same across all 128 00:07:35 --> 00:07:37 the phases for that component. 129 00:07:37 --> 00:07:42 And if you count the number of equations, the number of equals 130 00:07:42 --> 00:07:47 signs here, that's p minus one. p minus one equals signs, 131 00:07:47 --> 00:07:50 constraints due to the fact that I have an 132 00:07:50 --> 00:07:51 equilibrium here. 133 00:07:51 --> 00:08:03 So this gives me p minus one constraints. 134 00:08:03 --> 00:08:05 And this is true for every single component. 135 00:08:05 --> 00:08:08 Every single component has to have its chemical potential, 136 00:08:08 --> 00:08:12 its chemical potential equal throughout the phases. 137 00:08:12 --> 00:08:14 So p minus one's constraint for one component 138 00:08:14 --> 00:08:16 times C components. 139 00:08:16 --> 00:08:26 So for a total of C times p minus one total constraints. 140 00:08:26 --> 00:08:29 My variables, my constraints. 141 00:08:29 --> 00:08:36 So the number of degrees of freedom then becomes p times 142 00:08:36 --> 00:08:49 C minus one minus C times p minus one and then plus two. 143 00:08:49 --> 00:08:52 And if you multiply this out, p times C gets rid 144 00:08:52 --> 00:08:53 of the p times C here. 145 00:08:53 --> 00:08:58 And you get the plus C minus p plus two. 146 00:08:58 --> 00:09:02 Which is the Gibbs phase rule, right? 147 00:09:02 --> 00:09:05 Which I'm going to bring back up here. 148 00:09:05 --> 00:09:08 C minus p plus two. 149 00:09:08 --> 00:09:12 So just purely in accounting, just accounting for the 150 00:09:12 --> 00:09:16 variables and the constraints. 151 00:09:16 --> 00:09:23 OK, any questions on how we did this? 152 00:09:23 --> 00:09:26 Great. 153 00:09:26 --> 00:09:26 OK. 154 00:09:26 --> 00:09:33 So let's move on, then, to these ideal solutions. 155 00:09:33 --> 00:09:35 Which is this case right here. 156 00:09:35 --> 00:09:41 And the first thing we're going to do is look at the case where 157 00:09:41 --> 00:09:47 we have A is a solvent, and it's volatile. 158 00:09:47 --> 00:09:50 And B is a solute, which is non-volatile. 159 00:09:50 --> 00:09:53 So let's take the first case. 160 00:09:53 --> 00:10:00 We have A volatile, that's a solvent. 161 00:10:00 --> 00:10:01 Could be water. 162 00:10:01 --> 00:10:05 And B is going to be the solute. 163 00:10:05 --> 00:10:09 It's non-volatile. 164 00:10:09 --> 00:10:11 And let's interchange solute or non-volatile 165 00:10:11 --> 00:10:14 to be consistent here. 166 00:10:14 --> 00:10:18 So this could be sugar. 167 00:10:18 --> 00:10:27 A sweet water. 168 00:10:27 --> 00:10:41 So, Mr. Raoult looked at such solutions, and found that they 169 00:10:41 --> 00:10:46 could be well described by the following diagram here. 170 00:10:46 --> 00:10:51 So if I plot on the x-axis here, from zero to one, I'm 171 00:10:51 --> 00:10:57 going to plot the partial molar fraction of the solute. 172 00:10:57 --> 00:11:00 Partial molar fractions of the solute, that's going to be xB. 173 00:11:00 --> 00:11:02 174 00:11:02 --> 00:11:06 So when xB equals to zero, I have a pure water solution. 175 00:11:06 --> 00:11:11 When xB is equal to one, I have pure sugar. 176 00:11:11 --> 00:11:17 Then on the y axis, I'm going to plot the total pressure. 177 00:11:17 --> 00:11:20 So when I have a pure water solution, the total pressure is 178 00:11:20 --> 00:11:25 going to be the same as the vapor pressure of water at 179 00:11:25 --> 00:11:28 a particular temperature. 180 00:11:28 --> 00:11:36 Let's take temperature fixed at some value. 181 00:11:36 --> 00:11:39 Temperature is fixed at some value. 182 00:11:39 --> 00:11:44 I'm going to have the total pressure is going to be the 183 00:11:44 --> 00:11:45 partial pressure of the water. 184 00:11:45 --> 00:11:49 And clearly, when I don't have any water left, all I have is 185 00:11:49 --> 00:11:51 the sugar, there's no pressure. 186 00:11:51 --> 00:11:54 We're going to assume that it's totally non-volatile. 187 00:11:54 --> 00:11:56 Obviously there's going to be a little bit of vapor pressure, 188 00:11:56 --> 00:11:58 even at room temperature. 189 00:11:58 --> 00:12:01 Ten to the minus, I don't know, 13 torr or something. 190 00:12:01 --> 00:12:05 But anyway, it's basically zero here. 191 00:12:05 --> 00:12:07 And what Raoult said is that while these two points are just 192 00:12:07 --> 00:12:13 connected by a straight line. 193 00:12:13 --> 00:12:19 Simplest way to connect two points. 194 00:12:19 --> 00:12:27 Basically, he said that the pressure of, the vapor pressure 195 00:12:27 --> 00:12:38 of the water in this case, is equal to xA times pA star. 196 00:12:38 --> 00:12:42 I could also plot this with xA, going from one to zero, since 197 00:12:42 --> 00:12:49 xA plus xB is equal to one. 198 00:12:49 --> 00:12:56 Or I could write this as one minus xB times pA star. 199 00:12:56 --> 00:12:58 Where a star, the star, means pure water. 200 00:12:58 --> 00:13:01 So pure A. 201 00:13:01 --> 00:13:06 And pA is the vapor pressure of the mixture. 202 00:13:06 --> 00:13:09 Which in this case here is the total pressure, because I don't 203 00:13:09 --> 00:13:12 have anything else that's volatile. 204 00:13:12 --> 00:13:29 And this is Raoult's law. 205 00:13:29 --> 00:13:32 And the first thing that you can use this for is to look 206 00:13:32 --> 00:13:35 at your first colligative property which is vapor 207 00:13:35 --> 00:13:45 pressure lowering. 208 00:13:45 --> 00:13:48 And let me point out another thing first. 209 00:13:48 --> 00:13:51 So if a solution obeys that property here, it's 210 00:13:51 --> 00:13:53 called an ideal solution. 211 00:13:53 --> 00:13:56 So if the water-sugar solution really did behave like a 212 00:13:56 --> 00:13:59 straight line like this, as you increase the amount of sugar, 213 00:13:59 --> 00:14:00 then it would be an ideal solution. 214 00:14:00 --> 00:14:02 Many things are very close to it. 215 00:14:02 --> 00:14:07 It's not such a bad approximation. 216 00:14:07 --> 00:14:09 Especially in that region up here. 217 00:14:09 --> 00:14:12 Around zero, when the amount of sugar is pretty small. 218 00:14:12 --> 00:14:19 You expect to obey an ideal solution behavior. 219 00:14:19 --> 00:14:23 Alright, so let's look now at a glass of water 220 00:14:23 --> 00:14:26 that has sugar in it. 221 00:14:26 --> 00:14:28 We've got my glass of water, H20. 222 00:14:28 --> 00:14:34 With some sugar dissolved in it. 223 00:14:34 --> 00:14:42 And it's got a certain vapor pressure on top. pA, or pH2O. 224 00:14:42 --> 00:14:43 And I'm going to ask the question, what's the difference 225 00:14:43 --> 00:14:49 between the vapor pressure what it would be without 226 00:14:49 --> 00:14:51 the sugar in it. 227 00:14:51 --> 00:14:59 What is pA star minus pA? 228 00:14:59 --> 00:15:07 Obeys Raoult's law. pA star, pA is xA pA star, 229 00:15:07 --> 00:15:09 plug that in here. 230 00:15:09 --> 00:15:15 That's one minus xA pA star, one minus xA is xB. 231 00:15:15 --> 00:15:18 xB pA star. 232 00:15:18 --> 00:15:21 Well, the first thing I know is that this is a positive number. 233 00:15:21 --> 00:15:25 xB is a positive number. pA star is a positive number. 234 00:15:25 --> 00:15:26 This is greater than zero. 235 00:15:26 --> 00:15:34 That means that the act of putting some solute in my water 236 00:15:34 --> 00:15:40 decreases the vapor pressure of the water in the gas phase. 237 00:15:40 --> 00:15:41 Pretty simple. 238 00:15:41 --> 00:15:47 It's called vapor pressure law. 239 00:15:47 --> 00:15:49 And we can actually take this one step further. 240 00:15:49 --> 00:15:57 We can draw a phase diagram. 241 00:15:57 --> 00:16:00 So our usual phase diagram here with temperature on this axis 242 00:16:00 --> 00:16:04 here and pressure on this axis here, and we've got our 243 00:16:04 --> 00:16:09 triple point sitting here. 244 00:16:09 --> 00:16:13 And our gas-liquid line, with a critical point here. 245 00:16:13 --> 00:16:16 So this is gas here, there's a liquid here. 246 00:16:16 --> 00:16:21 And we've got our, this is going to be water. 247 00:16:21 --> 00:16:23 So it's got a negative slope. 248 00:16:23 --> 00:16:26 I think I've got it right this time. 249 00:16:26 --> 00:16:29 And there's the solid phase here. 250 00:16:29 --> 00:16:31 OK, this is for the pure stuff. 251 00:16:31 --> 00:16:40 So now I can draw a similar diagram for sugared water. 252 00:16:40 --> 00:16:44 And I just looked at this, assuming it obeys Raoult's law. 253 00:16:44 --> 00:16:50 What we looked at here was the gas-liquid coexistence. 254 00:16:50 --> 00:16:55 And we found that the gas-liquid coexistence point, 255 00:16:55 --> 00:16:58 the vapor pressure of the water, was less than 256 00:16:58 --> 00:16:59 if it were pure. 257 00:16:59 --> 00:17:02 So that means that if I looked at the gas-liquid coexistence, 258 00:17:02 --> 00:17:05 which is this line right here. 259 00:17:05 --> 00:17:08 In the presence of sugar, that whole line is 260 00:17:08 --> 00:17:11 going to get lowered. 261 00:17:11 --> 00:17:14 The pressure, the vapor pressure, of the water is 262 00:17:14 --> 00:17:17 going to be lower when the sugar is there. 263 00:17:17 --> 00:17:26 So the whole thing is going to get lower. 264 00:17:26 --> 00:17:32 Now, if I have a solid, if the water is a solid, it's going 265 00:17:32 --> 00:17:34 to crystallize the water, the sugar is going to be 266 00:17:34 --> 00:17:36 separated from the water. 267 00:17:36 --> 00:17:37 The sugar and the water are not going to really 268 00:17:37 --> 00:17:40 know about each other. 269 00:17:40 --> 00:17:44 They're just going to have big chunks of pure water, with 270 00:17:44 --> 00:17:49 every now and then a molecule of sugar that's in there. 271 00:17:49 --> 00:17:53 So you don't really expect to see any difference between the 272 00:17:53 --> 00:17:58 pure solid water, in terms of the gas-solid interface, 273 00:17:58 --> 00:18:02 and the pure liquid water. 274 00:18:02 --> 00:18:06 There's no sugar in the gas phase. 275 00:18:06 --> 00:18:10 And as far as the gas phase is concerned, that solid 276 00:18:10 --> 00:18:11 phase is pure water. 277 00:18:11 --> 00:18:14 It's just seeing pure ice crystals on the surface. 278 00:18:14 --> 00:18:17 Every now and then there's a molecule of sugar. 279 00:18:17 --> 00:18:22 So you expect this to be pretty close here. 280 00:18:22 --> 00:18:24 So you expect the triple point to go down. 281 00:18:24 --> 00:18:29 And if I now, I go up to the solid-liquid coexistence, 282 00:18:29 --> 00:18:33 and go up like this, I can make a prediction about 283 00:18:33 --> 00:18:36 solid-liquid coexistence. 284 00:18:36 --> 00:18:41 I can predict that if I'm looking at, let's put 285 00:18:41 --> 00:18:49 one bar here somewhere. 286 00:18:49 --> 00:18:52 One bar. 287 00:18:52 --> 00:18:53 Room temperature, sitting here somewhere. 288 00:18:53 --> 00:18:57 One bar, room temperature, water is all liquid. 289 00:18:57 --> 00:19:03 This is what it would usually, solid, liquid, that would 290 00:19:03 --> 00:19:06 be 273 degrees Kelvin. 291 00:19:06 --> 00:19:10 That's the melting point of water. 292 00:19:10 --> 00:19:14 So now if I put sugar in the water, and I follow my diagram 293 00:19:14 --> 00:19:21 here, what I find is that the new melting point of water is 294 00:19:21 --> 00:19:29 some new temperature T, T1, where T1 is less than 295 00:19:29 --> 00:19:30 273 degrees Kelvin. 296 00:19:30 --> 00:19:31 You all know this. 297 00:19:31 --> 00:19:34 When you put something, like an impurity, a salt or sugar in 298 00:19:34 --> 00:19:37 the water, the melting point gets depressed. 299 00:19:37 --> 00:19:43 It goes down. 300 00:19:43 --> 00:19:44 Straight from here. 301 00:19:44 --> 00:19:46 You can build it up straight from here. 302 00:19:46 --> 00:19:51 When we get to the colligative properties, we'll attack 303 00:19:51 --> 00:19:55 it from the point of chemical potentials. 304 00:19:55 --> 00:19:57 We'll equate chemical potentials and we'll look at 305 00:19:57 --> 00:19:59 the change in the chemical potential in the water, and 306 00:19:59 --> 00:20:02 the presence of the sugar and we'll do it rigorously. 307 00:20:02 --> 00:20:05 But this is sort of the first indication that these 308 00:20:05 --> 00:20:08 colligative properties are all connected to each other. 309 00:20:08 --> 00:20:13 They're connected to this diagram here. 310 00:20:13 --> 00:20:14 OK. 311 00:20:14 --> 00:20:19 So when I was a kid, and I knew that this was the case. 312 00:20:19 --> 00:20:21 Everybody knows this is the case, right? 313 00:20:21 --> 00:20:24 You put salt in the water and you expect all sorts 314 00:20:24 --> 00:20:25 of things to happen. 315 00:20:25 --> 00:20:27 You expect the vapor pressure to go down. 316 00:20:27 --> 00:20:31 And certainly you know that you add salt to the roads and 317 00:20:31 --> 00:20:33 the water melts, et cetera. 318 00:20:33 --> 00:20:36 And my mother always told me that the reason why you added 319 00:20:36 --> 00:20:42 salt to the water was so that the temperature of the water 320 00:20:42 --> 00:20:46 would get higher when you try to boil pasta. 321 00:20:46 --> 00:20:50 And for, I don't know, fifteen years I believed her. 322 00:20:50 --> 00:20:53 Until I taught thermodynamics. 323 00:20:53 --> 00:20:57 And I actually calculated the change in the temperature 324 00:20:57 --> 00:21:01 by adding a few pinches of salt to the water. 325 00:21:01 --> 00:21:04 And you know how small that temperature change is? 326 00:21:04 --> 00:21:05 You should calculate it. 327 00:21:05 --> 00:21:07 It's really tiny. 328 00:21:07 --> 00:21:09 It won't make any difference for the water. 329 00:21:09 --> 00:21:12 Probably the difference in the temperature of the water will 330 00:21:12 --> 00:21:16 be the same as if I cooked here versus halfway up Mount 331 00:21:16 --> 00:21:18 Washington in New Hampshire or something. 332 00:21:18 --> 00:21:19 Probably even less. 333 00:21:19 --> 00:21:20 There's no difference. 334 00:21:20 --> 00:21:23 The reason why you add salt is so that it tastes better. 335 00:21:23 --> 00:21:24 That's the only reason. 336 00:21:24 --> 00:21:28 It has nothing to do with thermodynamics. 337 00:21:28 --> 00:21:35 Alright, any questions on this? 338 00:21:35 --> 00:21:37 So we going to make it a little bit more complicated now, 339 00:21:37 --> 00:21:38 if there's no questions. 340 00:21:38 --> 00:21:43 We're going to now have, instead of having one 341 00:21:43 --> 00:21:47 non-volatile solute, use we're going to have two, we're going 342 00:21:47 --> 00:21:47 to have this mixture. 343 00:21:47 --> 00:21:58 Where both components are volatile. 344 00:21:58 --> 00:22:03 Can we erase this? 345 00:22:03 --> 00:22:03 Actually, I may not erase this. 346 00:22:03 --> 00:22:12 Because I want to keep Raoult's law here. 347 00:22:12 --> 00:22:13 OK, we're going to have a mixture of two 348 00:22:13 --> 00:22:16 volatile components. 349 00:22:16 --> 00:22:19 For instance, water and alcohol. 350 00:22:19 --> 00:22:25 Your your typical martini type situation. 351 00:22:25 --> 00:22:26 Or margarita. 352 00:22:26 --> 00:22:40 Whatever's your favorite drink. 353 00:22:40 --> 00:22:47 So now we have xA, we have xB, we have yA, we have yB. 354 00:22:47 --> 00:23:00 And we're going to assume that both obey Raoult's law with 355 00:23:00 --> 00:23:02 respect to each other. 356 00:23:02 --> 00:23:08 So now if I draw a diagram, and I just focus on, so there's the 357 00:23:08 --> 00:23:12 total pressure sitting here. 358 00:23:12 --> 00:23:15 And I just focus on one component and ignore the other. 359 00:23:15 --> 00:23:18 Suppose I focus on A. 360 00:23:18 --> 00:23:22 And I know that A in the presence of B, the partial 361 00:23:22 --> 00:23:25 pressure of A is going to obey Raoult's law. 362 00:23:25 --> 00:23:28 And let's take A to be the more volatile component 363 00:23:28 --> 00:23:30 in this case here. 364 00:23:30 --> 00:23:35 So pA star is bigger than pB star. 365 00:23:35 --> 00:23:39 The partial pressure, pure A, had a particular temperature, 366 00:23:39 --> 00:23:45 T fixed is bigger than pB star, it's the more 367 00:23:45 --> 00:23:48 volatile of the two. 368 00:23:48 --> 00:23:57 So if I were to plot pA as a function of xB, going from zero 369 00:23:57 --> 00:23:59 to one, so it'll be Raoult's law, I'm going to 370 00:23:59 --> 00:24:04 start at pA star. 371 00:24:04 --> 00:24:09 And I'm going to go down linearly to xB equals one. 372 00:24:09 --> 00:24:12 Now I can do the same thing for the partial pressure of B. 373 00:24:12 --> 00:24:19 And assume that in the presence of A, just looking at this 374 00:24:19 --> 00:24:21 component B, now, and I'm looking at the partial pressure 375 00:24:21 --> 00:24:24 of B, and it's got its impurity in it, A. 376 00:24:24 --> 00:24:27 B obeys Raoult's law with A in there. 377 00:24:27 --> 00:24:34 But now if I want to keep the same x axis here, I can look 378 00:24:34 --> 00:24:36 at xA here, going from zero to one. 379 00:24:36 --> 00:24:40 So I just basically flip the thing over. 380 00:24:40 --> 00:24:44 So at xA equals zero that's pure B. pB star 381 00:24:44 --> 00:24:45 is less than pA star. 382 00:24:45 --> 00:24:50 I'm starting here, on that side here. pB star, and I'm going 383 00:24:50 --> 00:25:00 down in a straight line to zero. pB is equal to xB pB 384 00:25:00 --> 00:25:02 star, straight line all the way to zero when xB is 385 00:25:02 --> 00:25:05 equal to zero. 386 00:25:05 --> 00:25:08 So that's pB. 387 00:25:08 --> 00:25:10 And that's pA. 388 00:25:10 --> 00:25:17 Now, the total pressure is the sum of the two. pA plus pB. 389 00:25:17 --> 00:25:21 So the total pressure in this system here, that I measure 390 00:25:21 --> 00:25:23 here, is just the sum of these two straight lines. 391 00:25:23 --> 00:25:25 Let me do it in blue. 392 00:25:25 --> 00:25:30 The total pressure, if you add up these two straight 393 00:25:30 --> 00:25:32 lines together, you got another straight line. 394 00:25:32 --> 00:25:37 Two straight lines make a straight line. p is pA 395 00:25:37 --> 00:25:48 plus pB is equal to xA pA star plus xB pB star. 396 00:25:48 --> 00:25:54 Now, xA and xB are related. xB is one minus xA. 397 00:25:54 --> 00:25:57 And so really, this is only a function of one variable here. 398 00:25:57 --> 00:26:02 Linearly, with respect to one variable. 399 00:26:02 --> 00:26:04 OK, what does this diagram tell me? 400 00:26:04 --> 00:26:13 So now, let's ignore how we built it. 401 00:26:13 --> 00:26:19 And let's take a look at it. 402 00:26:19 --> 00:26:23 So I have, going to take xB on the bottom here. 403 00:26:23 --> 00:26:25 From zero to one. 404 00:26:25 --> 00:26:29 We could choose either one, and I've got the straight line for 405 00:26:29 --> 00:26:36 the total pressure going from pA star to pB star. 406 00:26:36 --> 00:26:38 T is fixed. 407 00:26:38 --> 00:26:42 I need to tell you that T is fixed because I have two 408 00:26:42 --> 00:26:43 degrees of freedom, right? 409 00:26:43 --> 00:26:45 I have two degrees of freedom. 410 00:26:45 --> 00:26:48 My degrees of freedom are the temperature, which I'm fixing. 411 00:26:48 --> 00:26:52 And the composition in the liquid phase, which I'm fixing. 412 00:26:52 --> 00:26:59 So my two variables are xB and T. 413 00:26:59 --> 00:27:00 Those are my two degrees of freedom. 414 00:27:00 --> 00:27:03 And I'm telling you what the total pressure is. 415 00:27:03 --> 00:27:08 I'm giving you total pressure as a function of xB and T. 416 00:27:08 --> 00:27:11 By fixing T, I'm really telling you what the pressure is 417 00:27:11 --> 00:27:13 of the function of xB. 418 00:27:13 --> 00:27:16 So the Gibbs phase rule then tells me that the pressure 419 00:27:16 --> 00:27:20 should be only a function of xB if T is fixed. 420 00:27:20 --> 00:27:21 Should be a line. 421 00:27:21 --> 00:27:22 Not necessarily straight, but it should be a 422 00:27:22 --> 00:27:26 line in this diagram. 423 00:27:26 --> 00:27:28 To have coexistence. 424 00:27:28 --> 00:27:34 So what this line is, then, this line is the line of points 425 00:27:34 --> 00:27:37 that tells me when I have coexistence between the gas 426 00:27:37 --> 00:27:41 phase and the liquid phase. 427 00:27:41 --> 00:27:41 The coexistence line. 428 00:27:41 --> 00:27:45 This is the gas-liquids coexistence line 429 00:27:45 --> 00:27:47 for the mixture. 430 00:27:47 --> 00:27:55 It's not so different than this coexistence line up here. 431 00:27:55 --> 00:27:59 So you can think of this as a phase diagram, kind of 432 00:27:59 --> 00:28:02 like you thought, you know this as a phase diagram. 433 00:28:02 --> 00:28:05 It's got a coexistence line. 434 00:28:05 --> 00:28:08 And then if I'm above this line, if I'm at a certain 435 00:28:08 --> 00:28:14 pressure here, I'm at this point here, this pressure well, 436 00:28:14 --> 00:28:18 let's go to a slightly higher different pressure here. 437 00:28:18 --> 00:28:22 And this composition here. 438 00:28:22 --> 00:28:24 I'm not on the line. 439 00:28:24 --> 00:28:27 That means that I don't have coexistence 440 00:28:27 --> 00:28:29 between liquid and gas. 441 00:28:29 --> 00:28:30 I'm above the line. 442 00:28:30 --> 00:28:35 I'm at a pressure higher then where I would get coexistence. 443 00:28:35 --> 00:28:38 The pressure is higher, means I probably don't 444 00:28:38 --> 00:28:42 have a gas any more. 445 00:28:42 --> 00:28:44 Probably means that the total pressure pushing down on 446 00:28:44 --> 00:28:48 my mixture is too high to have a gas phase around. 447 00:28:48 --> 00:28:55 It means that the top part here is a liquid phase. 448 00:28:55 --> 00:29:00 So I'm in the liquid phase if I'm above this line and I have 449 00:29:00 --> 00:29:03 a coexistence between the gas and the liquid if 450 00:29:03 --> 00:29:06 I'm on the line. 451 00:29:06 --> 00:29:13 Now, if I'm below this line here, well, I get in trouble. 452 00:29:13 --> 00:29:17 I get in trouble because my first instinct would be, 453 00:29:17 --> 00:29:19 well this is just gas. 454 00:29:19 --> 00:29:22 I go from liquid, and then I have coexistence. 455 00:29:22 --> 00:29:24 Then I go into the gas phase. 456 00:29:24 --> 00:29:27 But my x-axis here is the composition in 457 00:29:27 --> 00:29:28 the liquid phase. 458 00:29:28 --> 00:29:31 There's no liquid around. 459 00:29:31 --> 00:29:35 So I really can't say anything here. 460 00:29:35 --> 00:29:37 This diagram is a little bit meaningless down here. 461 00:29:37 --> 00:29:40 Because my x-axis is describing a phase which doesn't 462 00:29:40 --> 00:29:45 exist on the diagram. 463 00:29:45 --> 00:29:48 On this diagram, here. 464 00:29:48 --> 00:29:51 So when you see it, this diagram here with Raoult's law 465 00:29:51 --> 00:29:54 on it, you've got to remember that the part that's really 466 00:29:54 --> 00:30:00 interesting is above the line and at the line itself. 467 00:30:00 --> 00:30:14 So you could do an experiment, then, on this line here. 468 00:30:14 --> 00:30:14 T fixed. 469 00:30:14 --> 00:30:20 This is the liquid phase. 470 00:30:20 --> 00:30:22 So suppose I start with some high pressure 471 00:30:22 --> 00:30:23 up here somewhere. 472 00:30:23 --> 00:30:29 At this point, let's call this point one. 473 00:30:29 --> 00:30:36 We've got my container, my piston here. p is equal to p1. 474 00:30:36 --> 00:30:38 Again, I put the point in an awkward place. 475 00:30:38 --> 00:30:49 Let's put it right there. p1, and composition 476 00:30:49 --> 00:30:56 xB. p1 and xB here. 477 00:30:56 --> 00:31:02 And I'm going to slowly decrease the pressure. 478 00:31:02 --> 00:31:03 I start in this composition. 479 00:31:03 --> 00:31:05 The composition doesn't change. 480 00:31:05 --> 00:31:07 I'm just decreasing the pressure. 481 00:31:07 --> 00:31:08 Decrease the pressure, decrease the pressure, decrease 482 00:31:08 --> 00:31:09 the pressure. 483 00:31:09 --> 00:31:14 And at some point, I get to that line. 484 00:31:14 --> 00:31:18 Get to that line, what happens when I get to that line? 485 00:31:18 --> 00:31:21 I start to see bubbles coming out of the liquid. 486 00:31:21 --> 00:31:22 Vapor starts to form, because it wants to be in the 487 00:31:22 --> 00:31:24 coexistence line. 488 00:31:24 --> 00:31:25 So I get to that line. 489 00:31:25 --> 00:31:29 And I get a little bit of bubbles forming. 490 00:31:29 --> 00:31:32 And a little bit of vapor. 491 00:31:32 --> 00:31:33 That's the liquid here. 492 00:31:33 --> 00:31:36 Little bit of gas. 493 00:31:36 --> 00:31:44 And that's why this line here is called the bubble line. 494 00:31:44 --> 00:31:48 So I've gone down, decreased the pressure. 495 00:31:48 --> 00:31:50 So p has gone down now. 496 00:31:50 --> 00:31:52 Decreased the pressure. 497 00:31:52 --> 00:31:58 And if I keep on decreasing pressure, well, I'm not 498 00:31:58 --> 00:32:00 going to jump into this area of the diagram. 499 00:32:00 --> 00:32:02 Because this area of the diagram means there's 500 00:32:02 --> 00:32:05 no liquid, it's a meaningless area. 501 00:32:05 --> 00:32:08 If I keep decreasing the pressure, I'm still going 502 00:32:08 --> 00:32:09 to be in coexistence. 503 00:32:09 --> 00:32:12 I'm just going to make more gas. 504 00:32:12 --> 00:32:13 More vapor. 505 00:32:13 --> 00:32:15 I'm going to transfer more of the liquid 506 00:32:15 --> 00:32:17 into the vapor phase. 507 00:32:17 --> 00:32:21 I'm going to ride down that line. 508 00:32:21 --> 00:32:22 I'm going to ride down the line. 509 00:32:22 --> 00:32:23 I'm decreasing the pressure. 510 00:32:23 --> 00:32:24 I'm not going to skip into here. 511 00:32:24 --> 00:32:29 I'm going to ride down the line here. 512 00:32:29 --> 00:32:33 We're going to keep decreasing the pressure even more. 513 00:32:33 --> 00:32:34 p goes down even more. 514 00:32:34 --> 00:32:37 Now, I make even more vapor. 515 00:32:37 --> 00:32:41 There's my piston right there. 516 00:32:41 --> 00:32:43 There's the gas phase. 517 00:32:43 --> 00:32:46 There's the liquid phase. 518 00:32:46 --> 00:32:51 Now I've transferred material from the liquid phase 519 00:32:51 --> 00:32:53 to the gas phase. 520 00:32:53 --> 00:32:57 But I also changed the composition of my liquid phase. 521 00:32:57 --> 00:33:02 And if I read my new composition, this is what 522 00:33:02 --> 00:33:05 I started out with. xB. 523 00:33:05 --> 00:33:09 My new composition in the liquid phase is going to be, 524 00:33:09 --> 00:33:15 let's call it xB prime. 525 00:33:15 --> 00:33:17 There's going to be more solute in there. 526 00:33:17 --> 00:33:24 Or more B in there, than what I started out with. 527 00:33:24 --> 00:33:25 Now which one was the more volatile one? 528 00:33:25 --> 00:33:27 A or B? 529 00:33:27 --> 00:33:29 A was more volatile, right? 530 00:33:29 --> 00:33:34 So as I decreased the pressure and I started bubbling off the 531 00:33:34 --> 00:33:38 material, which one's going to bubble off preferentially? 532 00:33:38 --> 00:33:39 A is going to. 533 00:33:39 --> 00:33:47 So it makes sense that I would concentrate B in there. 534 00:33:47 --> 00:33:49 Decrease the pressure. 535 00:33:49 --> 00:33:51 Bubbles that are rich in A come out. 536 00:33:51 --> 00:33:52 Both A and 537 00:33:52 --> 00:33:52 B come out. 538 00:33:52 --> 00:33:55 But more A comes out than B. 539 00:33:55 --> 00:33:58 And what's left over is rich and then more than the less 540 00:33:58 --> 00:34:01 volatile material which is B. 541 00:34:01 --> 00:34:05 So we're beginning to see how distillation comes about. 542 00:34:05 --> 00:34:07 This is the first step in it. 543 00:34:07 --> 00:34:18 In a distillation process. 544 00:34:18 --> 00:34:21 So let's make this a little bit more complicated now. 545 00:34:21 --> 00:34:30 Any questions, first? 546 00:34:30 --> 00:34:32 Alright, now, suppose I wanted to know. 547 00:34:32 --> 00:34:35 So I found out where the composition in the 548 00:34:35 --> 00:34:38 liquid phase is here. 549 00:34:38 --> 00:34:41 And I know that should tell me immediately whether the 550 00:34:41 --> 00:34:43 composition in the gas phase is here. 551 00:34:43 --> 00:34:47 So I have all, I have everything I need to know to 552 00:34:47 --> 00:34:52 calculate what the composition in the gas phase is. 553 00:34:52 --> 00:34:55 So I have everything I need, then, to calculate and draw a 554 00:34:55 --> 00:34:58 diagram that looks just like this. 555 00:34:58 --> 00:35:04 Except where my x-axis is the y's instead of the x's. 556 00:35:04 --> 00:35:08 Going to make the same diagram, except now I'm going to use 557 00:35:08 --> 00:35:10 the gas phase as my reference point. 558 00:35:10 --> 00:35:15 The composition in the gas phase. 559 00:35:15 --> 00:35:22 So I need to get, so here I got p as a function of xB. 560 00:35:22 --> 00:35:30 I want p, total pressure, as a function of yB. 561 00:35:30 --> 00:35:33 So I can draw a diagram that looks just like this except 562 00:35:33 --> 00:35:41 now with the x-axis being the gas phase composition. 563 00:35:41 --> 00:35:41 Let's turn the crank. 564 00:35:41 --> 00:35:45 What do I know? 565 00:35:45 --> 00:35:55 I know Dalton's law. pA is yA times total pressure. 566 00:35:55 --> 00:35:59 I'm trying mix up the partial pressures and the total 567 00:35:59 --> 00:36:02 pressure in all ways that I know how to write it. 568 00:36:02 --> 00:36:05 And then hope that something's going to come out that's 569 00:36:05 --> 00:36:06 going to be helpful. 570 00:36:06 --> 00:36:10 So that's Dalton's law. 571 00:36:10 --> 00:36:17 I know Raoult's law. pA is xA star times pA star. 572 00:36:17 --> 00:36:22 And that's Raoult. 573 00:36:22 --> 00:36:25 And I can write Raoult's law in a different way. 574 00:36:25 --> 00:36:30 I can write as pB is equal to xB pB star, that's 575 00:36:30 --> 00:36:35 just Raoult's law for B. 576 00:36:35 --> 00:36:41 One minus xA pB star. 577 00:36:41 --> 00:36:45 And I'm looking for this. 578 00:36:45 --> 00:36:48 I'm looking for the composition in the gas phase. 579 00:36:48 --> 00:36:50 Or the total pressure as a function of the composition 580 00:36:50 --> 00:36:51 in the gas phase. 581 00:36:51 --> 00:36:54 Let's start by finding the composition in the gas phase as 582 00:36:54 --> 00:36:58 a function of the composition in the liquid phase. 583 00:36:58 --> 00:37:01 And the total pressure. 584 00:37:01 --> 00:37:08 Rewrite yA is equal to pA over P. 585 00:37:08 --> 00:37:11 Total pressure is pA plus pB. 586 00:37:11 --> 00:37:16 Sum of the two partial pressures. pA over pA plus pB. 587 00:37:16 --> 00:37:19 And I'm trying to get yA in terms of the xA's. 588 00:37:19 --> 00:37:21 Or xB's, in terms of composition in 589 00:37:21 --> 00:37:22 the liquid phase. 590 00:37:22 --> 00:37:25 And I know how to relate that to a constant. 591 00:37:25 --> 00:37:29 Which is the vapor pressure of the pure material times the, 592 00:37:29 --> 00:37:33 and the composition of the liquid phase, Raoult's law. 593 00:37:33 --> 00:37:44 This is xA pA star divided by xA pA star plus xB pB star. 594 00:37:44 --> 00:37:46 And I know that xB is one minus xA. 595 00:37:46 --> 00:37:58 So this is xA pA star times pB star plus pA star 596 00:37:58 --> 00:38:02 minus pB star times xA. 597 00:38:02 --> 00:38:07 Where all I did was replace xB with one minus xA. 598 00:38:07 --> 00:38:10 And rearrange my equation on the bottom. 599 00:38:10 --> 00:38:15 So I've gotten the composition in the gas phase in terms of 600 00:38:15 --> 00:38:17 the composition in the liquid phase. 601 00:38:17 --> 00:38:18 They're not independent. 602 00:38:18 --> 00:38:20 I knew they weren't independent. 603 00:38:20 --> 00:38:24 And this just shows me that math works. 604 00:38:24 --> 00:38:24 OK. 605 00:38:24 --> 00:38:25 So I've got that. 606 00:38:25 --> 00:38:28 And I can invert this to get the composition in the liquid 607 00:38:28 --> 00:38:31 phase in terms of the composition in the gas phase. 608 00:38:31 --> 00:38:35 It's not so straightforward, but you can get xA as a 609 00:38:35 --> 00:38:37 function of yA, as well. 610 00:38:37 --> 00:38:40 You've got xA, if you reverse this you get xA 611 00:38:40 --> 00:38:44 is equal to yA pB star. 612 00:38:44 --> 00:38:54 It looks kind of the same. pB star plus pA star plus pB star 613 00:38:54 --> 00:39:01 minus pA star times yA. xA as a function of yA. 614 00:39:01 --> 00:39:05 615 00:39:05 --> 00:39:05 Alright. 616 00:39:05 --> 00:39:11 So now you can actually put everything together, 617 00:39:11 --> 00:39:13 starting from Dalton's law. 618 00:39:13 --> 00:39:15 Because really what we want is the total pressure as a 619 00:39:15 --> 00:39:19 function of the composition in the gas phase. 620 00:39:19 --> 00:39:20 So there's our total pressure here. 621 00:39:20 --> 00:39:22 There's the composition in the gas phase. 622 00:39:22 --> 00:39:24 There's pA. 623 00:39:24 --> 00:39:26 We've found composition in the gas phase in terms 624 00:39:26 --> 00:39:30 of composition in the liquid phase. 625 00:39:30 --> 00:39:38 P is equal to yA over pA. 626 00:39:38 --> 00:39:45 Which is equal to yA over xA pA star. 627 00:39:45 --> 00:39:48 So if we could get rid of this here, in terms of 628 00:39:48 --> 00:39:49 yA, we'd be all set. 629 00:39:49 --> 00:39:52 We'd get the total pressure as a function of the composition 630 00:39:52 --> 00:39:54 in the gas phase. 631 00:39:54 --> 00:39:57 And there's what we need. 632 00:39:57 --> 00:40:00 So we plug that in here. 633 00:40:00 --> 00:40:06 And now we have the total pressure in terms of constants 634 00:40:06 --> 00:40:12 like these pure vapor pressures and the composition of 635 00:40:12 --> 00:40:18 A in the gas phase. 636 00:40:18 --> 00:40:21 So let me find a way to write that somewhere. 637 00:40:21 --> 00:40:24 Let me write it right here in this little box here. 638 00:40:24 --> 00:40:29 Plug it in, you get something that's not a straight line. 639 00:40:29 --> 00:40:31 Unfortunately. 640 00:40:31 --> 00:40:38 Doesn't look like Raoult's law. pA star pB star. pA star plus 641 00:40:38 --> 00:40:48 pB star minus pA star times yA. 642 00:40:48 --> 00:40:49 It's not a straight line. 643 00:40:49 --> 00:40:57 It's a more complicated function. 644 00:40:57 --> 00:41:16 What does it look like? 645 00:41:16 --> 00:41:17 Looks like this. 646 00:41:17 --> 00:41:23 I'm going to use the same sort of plot. 647 00:41:23 --> 00:41:24 I going to plot the total pressure on this axis 648 00:41:24 --> 00:41:25 here, on the y axis. 649 00:41:25 --> 00:41:28 I'm going to keep the T fixed. 650 00:41:28 --> 00:41:31 Temperature is fixed. 651 00:41:31 --> 00:41:34 So I'm going to find the total pressure as a function of 652 00:41:34 --> 00:41:35 the composition in the gas 653 00:41:35 --> 00:41:35 phase. 654 00:41:35 --> 00:41:42 I'm going to put yB here. yB going from zero to one. 655 00:41:42 --> 00:41:50 So it's kind of looking like what I had before. 656 00:41:50 --> 00:41:51 Total pressure is going to look the same. 657 00:41:51 --> 00:41:54 If you want to do it in terms of B, you just have everywhere 658 00:41:54 --> 00:41:55 you see B replace it with A. 659 00:41:55 --> 00:41:57 And everywhere you see A replace it with B. 660 00:41:57 --> 00:42:02 You just need to change the two. 661 00:42:02 --> 00:42:06 You know that if yB is equal to zero, that you have pure A. 662 00:42:06 --> 00:42:12 So you know that this is going to be pA star here. 663 00:42:12 --> 00:42:14 You know if you have yB equals to one in the gas phase, you 664 00:42:14 --> 00:42:16 have pure B in the gas phase. 665 00:42:16 --> 00:42:20 You know that what you have is the vapor pressure of the pure 666 00:42:20 --> 00:42:26 B, in this case the pure water. pB star, OK? 667 00:42:26 --> 00:42:31 Where A is more volatile then B. 668 00:42:31 --> 00:42:35 A would be the ethanol and B would be the water. 669 00:42:35 --> 00:42:37 And it's not a straight line. 670 00:42:37 --> 00:42:39 If it were Raoult, he would say just connect these 671 00:42:39 --> 00:42:40 two with a straight line. 672 00:42:40 --> 00:42:41 But it's not. 673 00:42:41 --> 00:42:44 It's not, we just figured out with an equation here. 674 00:42:44 --> 00:42:49 And it turns out to be a line that looks like this. 675 00:42:49 --> 00:42:55 It's a curved line that looks a bit like this. 676 00:42:55 --> 00:42:57 OK, what does this line mean? 677 00:42:57 --> 00:43:01 This line is also a coexistence line. 678 00:43:01 --> 00:43:02 That's what we started out with. 679 00:43:02 --> 00:43:05 We started out with Raoult. 680 00:43:05 --> 00:43:07 That was part of our derivation. 681 00:43:07 --> 00:43:15 Raoult's law tells you the composition at coexistence. 682 00:43:15 --> 00:43:18 Tells you the pressure of, the total pressure, or partial 683 00:43:18 --> 00:43:21 pressure at coexistence and the composition. 684 00:43:21 --> 00:43:26 So this is a coexistence line between the liquid and the gas. 685 00:43:26 --> 00:43:28 Coexistence between liquid and gas. 686 00:43:28 --> 00:43:30 But now, it's not as a function of the composition 687 00:43:30 --> 00:43:30 at the liquid phase. 688 00:43:30 --> 00:43:34 It's a function of the composition in the gas phase. 689 00:43:34 --> 00:43:38 Which was missing before. 690 00:43:38 --> 00:43:44 So now if I do my experiment, and I'm, so what 691 00:43:44 --> 00:43:44 does this mean? 692 00:43:44 --> 00:43:48 So if I have a point, if I have a pressure which is lower than 693 00:43:48 --> 00:43:51 the line here, then I have pure gas. 694 00:43:51 --> 00:43:52 Pressure, low pressure, I have pure gas. 695 00:43:52 --> 00:43:53 Don't have any liquids. 696 00:43:53 --> 00:43:57 And that's fine, because I can, I know what that point is. 697 00:43:57 --> 00:44:02 If I'm sitting below the line here somewhere, 698 00:44:02 --> 00:44:06 so I'm sitting here. 699 00:44:06 --> 00:44:09 Some composition in the gas phase, a certain pressure. 700 00:44:09 --> 00:44:11 That's fine. 701 00:44:11 --> 00:44:15 It's a meaningful point. 702 00:44:15 --> 00:44:18 So my container here has a piston on it. 703 00:44:18 --> 00:44:26 And I'm starting out with this pressure, p1 here. 704 00:44:26 --> 00:44:27 p1 pressing down. 705 00:44:27 --> 00:44:30 And I got yB in this here. 706 00:44:30 --> 00:44:33 And I increase the pressure, pressure goes up. 707 00:44:33 --> 00:44:35 Composition doesn't change. 708 00:44:35 --> 00:44:38 I'm just increasing the pressure. 709 00:44:38 --> 00:44:39 Increasing the pressure, increasing the pressure. 710 00:44:39 --> 00:44:42 Now, at some point the pressure becomes big enough that I 711 00:44:42 --> 00:44:44 start to see liquid forming. 712 00:44:44 --> 00:44:54 Little drops of liquid forming in my container. 713 00:44:54 --> 00:44:58 So now I have little drops of liquid that are forming in my 714 00:44:58 --> 00:45:01 container, that are going to start to rain down and form a 715 00:45:01 --> 00:45:05 little bit of liquid pooling at the bottom of the container. 716 00:45:05 --> 00:45:10 And that's called the dew line. 717 00:45:10 --> 00:45:12 The other one was called the bubble line, this 718 00:45:12 --> 00:45:15 is called the dew line. 719 00:45:15 --> 00:45:19 So when I reach the dew line, I start forming liquid. 720 00:45:19 --> 00:45:21 And again, just like in the previous case, if I keep 721 00:45:21 --> 00:45:24 increasing the pressure, I don't go into this area here. 722 00:45:24 --> 00:45:25 First of all, this area's meaningless for 723 00:45:25 --> 00:45:27 this diagram here. 724 00:45:27 --> 00:45:31 Because this area's pure liquid. 725 00:45:31 --> 00:45:33 But the x-axis here doesn't tell me about the 726 00:45:33 --> 00:45:34 composition of pure liquid. 727 00:45:34 --> 00:45:35 It's all yB. 728 00:45:35 --> 00:45:38 It's all about the composition in the gas -- yes. 729 00:45:38 --> 00:45:40 STUDENT: [INAUDIBLE] 730 00:45:40 --> 00:45:43 PROFESSOR: Between the dew line and the bubble line? 731 00:45:43 --> 00:45:43 STUDENT: Yeah. 732 00:45:43 --> 00:45:44 PROFESSOR: This never, never world. 733 00:45:44 --> 00:45:47 Where you're not allowed to inhabit. 734 00:45:47 --> 00:45:54 We're going to go into that next time. 735 00:45:54 --> 00:45:57 On how to use those two curves together. 736 00:45:57 --> 00:45:59 OK, but the same thing happens here. 737 00:45:59 --> 00:46:01 If I increase the pressure, I'm going to ride the 738 00:46:01 --> 00:46:01 coexistence line up. 739 00:46:01 --> 00:46:12 I ride it up, and keep riding it up. 740 00:46:12 --> 00:46:14 And I get liquid forming in here. 741 00:46:14 --> 00:46:16 And I can find out the composition in the 742 00:46:16 --> 00:46:17 gas phase now. 743 00:46:17 --> 00:46:20 The composition in the gas phase, as I increase the 744 00:46:20 --> 00:46:25 pressure, I get yB prime, there's yB that I 745 00:46:25 --> 00:46:26 started out with with. 746 00:46:26 --> 00:46:30 With yB prime is less than yB. 747 00:46:30 --> 00:46:37 And remember, B was the less volatile of the two. 748 00:46:37 --> 00:46:42 As I increase the pressure, I am forming liquid. 749 00:46:42 --> 00:46:46 The composition in the gas phase changes. 750 00:46:46 --> 00:46:50 You decrease the mole fraction of the less volatile 751 00:46:50 --> 00:46:51 material in the gas phase. 752 00:46:51 --> 00:46:55 The more volatile A becomes more prevalent 753 00:46:55 --> 00:46:57 in the gas phase. 754 00:46:57 --> 00:47:00 And what's coming down is mostly, then, 755 00:47:00 --> 00:47:02 it's enriched in B. 756 00:47:02 --> 00:47:06 You've done an enrichment of the less volatile 757 00:47:06 --> 00:47:10 material down in here. 758 00:47:10 --> 00:47:12 And now you can put the two together, as the 759 00:47:12 --> 00:47:19 question was asked. 760 00:47:19 --> 00:47:21 Now we can have, we mix the two together. 761 00:47:21 --> 00:47:27 We mix our Raoult diagram with our dew line diagram. 762 00:47:27 --> 00:47:31 We mix the bubble line and the dew line together. 763 00:47:31 --> 00:47:32 In one diagram, which is going to be a powerful 764 00:47:32 --> 00:47:48 diagram to use. 765 00:47:48 --> 00:47:51 Total pressure. 766 00:47:51 --> 00:47:54 Temperature fixed. 767 00:47:54 --> 00:48:02 You've got two materials, pA star is bigger than pB star. 768 00:48:02 --> 00:48:08 So I'm going to have pA star here, pB star down here. 769 00:48:08 --> 00:48:13 And if I choose, as my x-axis, to have xB going from zero to 770 00:48:13 --> 00:48:18 one, I can draw a coexistence line on this axis. 771 00:48:18 --> 00:48:20 On this diagram. 772 00:48:20 --> 00:48:24 That's the coexistence line in terms of xB. 773 00:48:24 --> 00:48:29 And any point up here is well-described by this xB 774 00:48:29 --> 00:48:32 value, and the p value. 775 00:48:32 --> 00:48:36 And as long as I have xB here, I'm not allowed to touch the 776 00:48:36 --> 00:48:38 bottom part of this diagram. 777 00:48:38 --> 00:48:43 But now if I add another x-axis, I'm going to add yB. 778 00:48:43 --> 00:48:46 779 00:48:46 --> 00:48:50 From zero to one. 780 00:48:50 --> 00:48:53 I draw a coexistence line in terms of yB. 781 00:48:53 --> 00:48:55 782 00:48:55 --> 00:48:56 Like this. 783 00:48:56 --> 00:49:01 So this line is p as a function of yB coexistence line. 784 00:49:01 --> 00:49:08 This line is total pressure of function of xB. 785 00:49:08 --> 00:49:10 And as long as I'm on this line or below this line, 786 00:49:10 --> 00:49:15 then this axis makes sense. 787 00:49:15 --> 00:49:17 That's how we build this diagram here. 788 00:49:17 --> 00:49:21 It's got a bubble line on top, and the dew line on the bottom. 789 00:49:21 --> 00:49:26 So I'm up here going down, I'm going to hit the bubble line. 790 00:49:26 --> 00:49:28 If I'm down here and go up in pressure, I'm going 791 00:49:28 --> 00:49:29 to hit the dew line. 792 00:49:29 --> 00:49:32 And next time -- well, next time we have an exam. 793 00:49:32 --> 00:49:38 But on Friday, we'll figure out how to use this diagram. 794 00:49:38 --> 00:49:39