Lab Report
by My Name
Student ID #
Binary Liquid-Vapor Phase Diagrams
Teaching Assistant: TA Name
Chem 374-005
Group #6
11/7/96
Performed: 11/17/96, 11/24/96
Lab Partner: Their Name
Abstract
This experiment attempted to determine the relationship between vapor pressure and composition of solutions of cyclohexanone and tetrachloroethane at various concentrations. This was achieved through distillation and analysis of (condensed) vapor and liquid vapor samples by measuring their indices of refraction. This mixture has a strong negative deviation from Raoult's law, resulting in a maximum boiling point and an azeotrope.
Introduction & Theory
Raoult's law states that, in an ideal mixture, the partial pressure of a component is proportional to its molar percentage-where an ideal mixture is a mixture that obeys Raoult's law throughout its ranges of composition(1). While some mixtures do obey Raoult's law (especially those similar in nature), many do not. Mixtures that have temperatures where the vapor pressure of a component is higher than that predicted by Raoult's law are said to show a positive deviation, while mixtures with components with lower vapor pressures are said to show negative deviations. Often, these deviations are large enough to cause maxima or minima in vapor-pressure and boiling-point curves.
At a maximum or minimum, the plot of the temperature or pressure of L, the liquid phase, and V, the vapor phase become tangent. The mixtures defined by these tangent points are called azeotropes. As a result, azeotropes are mixtures that cannot be separated by simple distillation, as the liquid and vapor phases are of the same composition.
Experimental
The procedure from Experiments in Physical Chemistry(2) pages 212-214 was followed, with the only change of procedure being an interruption of the experiment after step 6, and the experiment being restarted at step 7 one week later.
Ambient temperature for steps 1-6 was 26C, and 23C for steps 7-10. Ambient pressure was 738 mm Hg for steps 1-6 and 746 mm Hg for steps 7-10 (corrected for temperature).
Results
|
Table 1 - Raw Data | |||||
| Sample # |
|
Liquid | |||
| Starting Temperature (C) | Ending Temperature (C) | Index of Refraction (nD20) | Temperature (C) | Index of Refraction (nD20) | |
| 1 | 144.5 | 144.5 | 1.4938 | 144.5 | 1.4944 |
| 2 | 149.0 | 149.5 | 1.489 | 149.5 | 1.4835 |
| 3 | 151.0 | 151.0 | 1.488 | 151.5 | 1.4826 |
| 4 | 154.0 | 154.0 | 1.4835 | 154.0 | 1.4795 |
| 5 | 157.0 | 157.2 | 1.4749 | 157.5 | 1.4736 |
| 6 | 157.0 | 157.0 | 1.4694 | 157.0 | 1.4693 |
| 7 | 153.5 | 153.5 | 1.450 | 153.5 | 1.450 |
| 8 | 154.0 | 155.0 | 1.4563 | 155.0 | 1.4598 |
| 9 | 155.5 | 156.0 | 1.4575 | 156.0 | 1.4675 |
| 10 | 157.0 | 157.0 | 1.4635 | 157.0 | 1.4615 |
In order to improve the accuracy of the temperature readings, a stem temperature correction
should be applied to all of the temperature data. Using the following formula:
After applying stem corrections to all of the temperature readings, the starting and ending
temperature readings for the vapor phase must be averaged, giving the actual temperature at which
the vapor was condensed and collected. The next step is to use the refractive indices to find the
weight percent of cyclohexanone in each sample, and finally determine the molar percentage.
By interpolation from table 2, the weight percentage of cyclohexanone can be determined for
each sample. For example, the vapor from sample 1 has a refractive index of 1.4938. The logarithm
of this number is 0.17429. This is between the numbers for 0% and 10%. By subtracting the lower
logarithm of refraction number and dividing by the difference between the two numbers, a percentage
is obtained, in this case 72.1%. This percentage is then multiplied by the difference in weight
percentages and the result is subtracted from the higher weight percentage. This final result is the
extrapolated weight percentage. For some of the data points, the results are out of the range of the
table. Extrapolation is not necessary for these points however, as they are known pure solutions and
can be set to 0% or 100% exactly.
These weight percentages can be converted to molar percentages with the following formula:
Table 3 - Calculated Results Sample The graph of this data (see appendix) clearly shows an azeotrope at about 45%
cyclohexanone, boiling at about 156C at about 742 mm Hg (averaged).
Discussion
The fact that three of the samples had indices of refraction outside of the range of the given
table is a clear indication of error. As values were found that were both too high and too low, a
simple calibration problem with the refractometer does not explain this. The refractometer was
checked against a known value of 1.5133 and measured 1.5124; giving an error of only 0.059%.
Impure starting materials, dirty glassware, or other contamination are the most likely causes for this;
of course improper reading of the instrument could cause the errors as well.
Another cause of error is the way the data was handled. The data in the table did not show
a relationship between composition and index of refraction that was exactly linear. In this case,
interpolation was probably more accurate than linear regression, as linear regression forces the entire
data series to a straight line, where interpolation is based only on the two closest points.
The sharp drop in boiling point when the composition was near 45% cyclohexanone is a fairly
clear indication of an azeotrope. Unfortunately, only two data points support the decrease, making
it impossible to ascertain that the drop was not merely experimental error or to determine exactly the
shape of the curve.
References
1. P. Atkins, Physical Chemistry, 5th ed., p. 217, W. H. Freeman and Company (1994).
2. D. P. Shoemaker, C. W. Garland, J. W. Nibler, Experiments in Physical Chemistry, 6th
ed., chap. 8, experiment 14, The McGraw-Hill Companies (1996).


Table 2 - Logarithm of refractive index for cyclohexanone-tetrachloroethane mixtures(4)
Log nD20
W% C6H10O
Log nD20
W% C6H10O
Log nD20
W% C6H10O
0.17441
0
0.16864
40
0.16360
80
0.17298
10
0.16719
50
0.16256
90
0.17155
20
0.16582
60
0.16158
100
0.17010
30
0.16473
70

Vapor Phase
Liquid Phase
Temperature
(C)
Molar %
Cyclohexanone
Temperature
(C)
Molar %
Cyclohexanone
1
145.3
0.489%
144.5
0.000%
2
150.2
6.576%
149.5
14.175%
3
152.0
7.899%
151.5
15.496%
4
155.1
14.157%
154.0
20.179%
5
158.3
27.600%
157.5
29.822%
6
158.2
37.521%
157.0
37.726%
7
154.6
100.000%
153.5
100%
8
155.6
74.786%
155.0
62.619%
9
156.9
70.187%
156.0
41.436%
10
158.2
51.211%
157.0
57.257%