1212 A Tables of Numerical Data
Table A.6 Molar Heat Capacities
Gases
CP,ma+bT+cT−^2
(Applicable between 298 K and 2000 K)
Substance a/JK−^1 mol−^1 b× 103 /JK−^2 mol−^1 c× 10 −^5 /J K mol−^1
H 2 27. 33. 30. 50
O 2 30. 04. 18 − 1. 67
N 2 28. 63. 8 − 0. 50
CO 28. 44. 1 − 0. 46
CO 2 44. 28. 79 − 8. 62
H 2 O30. 510. 30
CH 4 23. 647. 86 − 1. 8
Liquids
Substance T/K CP,m/JK−^1 mol−^1
H 2 O 273 − 373 75. 48
CO 80 60. 7
C 2 H 6 100 68. 6
Hg 234 28. 286
Solids
Substance T/K CP,m/JK−^1 mol−^1
H 2 O 273 37. 15
Hg 234 28. 274
Cu 1357 31. 0
Zn 693 29. 7
Sn 505 30. 5
From K. S. Pitzer and L. Brewer,Thermodynamics, McGraw-Hill, New York, 1961, pp. 63, 66.
Table A.7 Specific Enthalpy Changes of Fusion and Vaporization
Substance M.P./◦C ∆fusHm/Jg−^1 B.P./◦C ∆vapHm/Jg−^1
Ammonia 66. 7 − 33. 35 1372
Benzene 5. 5 127 80. 1 394
Carbon dioxide −56.6a 180. 7 −78.5b 526. 6
Carbon monoxide − 199 29. 8 − 191. 5 240. 98
Carbon tetrachloride − 22. 99 17. 576. 54 207. 5
Ethane − 183. 395. 10 − 88. 6 520. 32
Ethanol − 117. 3 109. 078. 5 878. 58
Methane − 182 58. 41 − 164 555. 19
Water 0. 0 333. 5 100. 0 2257. 5
From R. C. Weast,Handbook of Chemistry and Physics, 64th ed., CRC Press, Boca Raton, FL, 1983,
pp. B227ff, C691ff.
aAt 5.2 atm pressure.
bSublimation temperature at 1.000 atm pressure.