Temperature range (°C) Volume of fraction (mL) Composition Fraction 1 72.0 – 77.0 0.61 Fraction 2 77.0 – 82.0 3.95 Fraction 3 82.0 – 87.0 4.55 v Choose... mostly cyclohexane Fraction 4 87.0 – 92.0 2.71 mostly toluene Fraction 5 92.0 – 97.0 2.17 mixture Fraction 6 97.0 – 100.5 1.80 Fraction 7 100.5 – 105.5 2.70 Fraction 8 105.5 – 110.5 5.20 Fraction 9 110.5 – 115.5 4.26 Fraction 10 115.5 – 120.5 1.50

Chemistry
10th Edition
ISBN:9781305957404
Author:Steven S. Zumdahl, Susan A. Zumdahl, Donald J. DeCoste
Publisher:Steven S. Zumdahl, Susan A. Zumdahl, Donald J. DeCoste
Chapter1: Chemical Foundations
Section: Chapter Questions
Problem 1RQ: Define and explain the differences between the following terms. a. law and theory b. theory and...
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distialltion on 30 mL of a mixture of cyclohexane and toluene was perfromed. Their literature values ar given. You need to designate all distillation fractions and pot residue as mostly cyclohexane, mostly toluene, or a mixture 

Literature boiling point of cyclohexane (°C)
80.7
Literature boiling point of toluene (°C)
110.6
Transcribed Image Text:Literature boiling point of cyclohexane (°C) 80.7 Literature boiling point of toluene (°C) 110.6
Temperature range (°C)
Volume of fraction (mL)
Composition
Fraction 1
72.0 – 77.0
0.61
Fraction 2
77.0 – 82.0
3.95
Fraction 3
82.0 – 87.0
4.55
v Choose...
mostly cyclohexane
Fraction 4
87.0 – 92.0
2.71
mostly toluene
Fraction 5
92.0 – 97.0
2.17
mixture
Fraction 6
97.0 – 100.5
1.80
Fraction 7
100.5 – 105.5
2.70
Fraction 8
105.5 – 110.5
5.20
Fraction 9
110.5 – 115.5
4.26
Fraction 10
115.5 – 120.5
1.50
Pot Residue
N/A
0.95
Transcribed Image Text:Temperature range (°C) Volume of fraction (mL) Composition Fraction 1 72.0 – 77.0 0.61 Fraction 2 77.0 – 82.0 3.95 Fraction 3 82.0 – 87.0 4.55 v Choose... mostly cyclohexane Fraction 4 87.0 – 92.0 2.71 mostly toluene Fraction 5 92.0 – 97.0 2.17 mixture Fraction 6 97.0 – 100.5 1.80 Fraction 7 100.5 – 105.5 2.70 Fraction 8 105.5 – 110.5 5.20 Fraction 9 110.5 – 115.5 4.26 Fraction 10 115.5 – 120.5 1.50 Pot Residue N/A 0.95
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