Chlorine
Solubility of chlorine in water Reprinted from Chlorine Manual, the Chlorine Institute, 3rd ed. Data for graph from L. Winkler, Math. es. Term.; Ertesito 25 (1907).		Chlorine gas density Data for graph from A.S. Ross and O. Maas, Canadian Journal of Research 18, Section B, 55-65 (1940).
Vapor pressure of liquid chlorine Reprinted from Chlorine Manual, the Chlorine Institute, 3rd ed. 1959. Data for graph from R. Kapoor and J.J. Martin, Thermodynamic Properties of Chlorine, Eng. Res. Inst. Univ. of Michigan, 1957.		Temperature-density relation for liquid chlorine Reprinted from Chlorine Manual, the Chlorine Institute, 3rd ed. 1959. Data for graph from R. Kapoor and J.J. Martin, Thermodynamic Properties of Chlorine, Eng. Res. Inst. Univ. of Michigan, 1957.
Latent heat of vaporization of liquid chlorine Reprinted from J.S. Sconce, Chlorine: Its Manufacture, Properties and Uses, N.Y., Reinhold Publishing Corp., 1962, p. 32. Data for graph from M.J. Pellaton, J. Chem Phys. 13, 454 (1915).		Heat capacity of chlorine gas H.M. Spencer and G.N. Flannagan, J. Am. Chem. Soc., 64, 2511 (1942).
Viscosity of chlorine Reprinted from J.S. Sconce, Chlorine: Its Manufacture, Properties and Uses, N.Y., Reinhold Publishing Corp., 1962, p. 35. Data for graph from E.W.R. Steacie and F.M.G. Johnson, J. Am. Chem. Soc. 47, 756 (1925); R. Wobser and F. Muller, Kolloid-Beihefte 52, 162 (1941).

Technical data for chlorine
Molecular Weight
	Carbon-12 scale		70.9061
Melting Point			-100.98&degC2 (-149.8&degF)
Boiling Point, 760 mm Hg			-34.05&degC2 (-29.3&degF)
Density of Dry Gas, 0&degC (32&degF) and 760 mm Hg
	lb/cu.ft		0.20033
Density of Saturated Gas, 0&degC (32&degF) and 53.155 psia
	lb/cu.ft		0.75373
Density of Liquid, 0&degC (32&degF) and 53.155 psia
	lb/cu.ft		91.673
Viscosity of Gas, 20&degC (68&degF)
	lb/sec./ft.		0.00000944
	poises (gm/sec./cm)		0.0001404
Viscosity of Liquid, 20&degC (68&degF)
	lb/sec./ft.		0.000234
	poises (gm/sec./cm)		0.0035
Critical Density
	lb/cu. ft.		35.775
Critical Pressure
	psia		1118.365
Critical Temperature			144&degC5 (291.2&degF)
Critical Volume
	Cu ft./lb		0.027965
Heat Fusion
	Btu/lb		38.862
Latent Heat of Vaporization
	Btu/lb		123.673
Specific Heat of Gas
	Constant Pressure, Cp
		Btu/lb/&degF, 50&degF - 100&degF	0.1153
	Constant Volume, Cv
		Btu/lb/&degF, 50&degF - 100&degF	0.08483
	Ratio, Cp/Cv		1.355
Specific Heat of Liquid
	Btu/lb/&degF, 50&degF - 75&degF		0.2266
Thermal Conductive of Gas
	Btu/hr./sq.ft./&degF/ft., 32&degF		0.00427
	132&degF		0.0049
Enthalpy, Btu/lb
	Dry Gas, 0&degC (32&degF) and 14.696 psia		232.743
	Saturated Gas, 0&degC (32&degF) and 53.155 psia		231.44
	Liquid, 0&degC (32&degF) and 53.155 psia		116.39
Enthropy, Btu/lb/&degF
	Dry Gas, 0&degC (32&degF) and 14.696 psia		0.739853
	Saturated Gas, 0&degC (32&degF) and 53.155 psia		0.70222
	Liquid, 0&degC (32&degF) and 53.155 psia		0.46823
Compressibility Coefficient of Liquid at 20&degC (68&degF)
	%/atm. (0.0-98.7 atm.)		0.01188
		(98.7-197.4 atm.)	0.0110
		(197.4-296.0 atm)	0.0102
1E. Wickers, J. Am. Chem. Soc. 74 (1952) 2W.F. Giauque and T.M. Powell, J. Am. Chem. Soc. 61, 1970 (1939) 3R. Kapoor and J.J. Martin, "Thermodynamic Properties of Chlorine". Eng. Res. Inst. Univ. of Michigan 1957 4National Research Council International Critical Tables, N.Y., McGraw Hill Book Company, Volume 5 (1929) 5M. Pellaton, J. Chim. Phys. 13, 426 (1915), F.B. Rossini et all., U.S. Circular 500, National Bureau of Standards, 1952 6International Critical Tables, Volume 1 (1926) 7A. Eucken and G. Hoffman, Z. Physik. Chem. B5, 422 (1929). L. Ziegler, Chem. Ing. Tech. 22, 229 (1950) 8T.W. Richards and W.N. Stull, J. Am. Chem. Soc. 26, 408 (1904)

Properties of saturated chlorine (Base: Solid at 0° R or -459.58&degF)

Temperature &degF t	Pressure (Psi)		Enthalpy (Btu per lb)
	Absolute P	Gage P	Sat. Liq. Hf	Vaporization hfg	Sat. Vapor hg
-50	8.603		98.28	126.26	224.54
-40	11.286		100.63	125.08	225.71
-30	14.442		102.98	123.91	226.89
-29.29	14.696	0.00	103.15	123.82	226.97
-20	18.338	3.64	105.33	122.60	227.93
-15	20.574	5.88	106.51	121.96	228.47
-10	23.015	8.42	107.68	121.30	228.98
-5	25.674	10.98	108.86	120.63	229.49
0	28.567	13.87	110.03	119.96	229.99
+5	31.703	17.01	111.21	119.26	230.47
10	35.098	20.40	112.38	118.57	230.95
15	38.766	24.07	113.56	117.86	231.42
20	42.719	28.02	114.73	117.15	231.88
25	46.713	32.02	115.91	116.43	232.34
30	51.193	36.50	117.08	115.69	232.77
35	55.999	41.30	118.26	114.95	233.21
40	61.146	46.45	119.43	114.19	233.63
45	66.649	51.95	120.61	113.43	234.04
50	72.523	57.83	121.78	112.65	234.43
55	78.786	64.09	122.96	111.85	234.81
60	85.452	70.76	124.13	111.06	235.19
65	92.540	77.84	125.31	110.26	235.57
70	100.07	85.37	126.48	109.44	235.92
75	108.04	93.34	127.66	108.63	236.29
80	116.49	101.79	128.83	107.78	236.61
85	125.42	110.72	129.99	106.88	236.87
90	134.85	120.15	131.15	105.88	237.03
95	144.80	130.10	132.31	104.98	237.29
100	157.09	142.39	133.47	104.04	237.51
110	177.95	163.25	135.79	101.95	237.74
120	202.95	188.25	138.11	99.82	237.93
130	230.43	215.73	140.43	97.52	237.95
140	260.51	245.81	142.75	95.38	238.13
150	293.34	278.64	145.11	92.94	238.05
160	329.03	314.33	147.55	90.23	237.78
170	363.73	353.03	150.11	87.76	237.87
180	409.52	394.82	152.83	84.77	237.60
190	454.55	439.85	155.74	81.72	237.46
200	502.93	488.23	158.88	78.31	237.19
210	554.79	540.09	162.29	74.83	237.12
220	610.21	595.51	166.01	70.90	236.91
230	669.31	654.61	170.11	66.73	236.84
240	732.17	717.47	174.70	62.10	236.80
250	798.93	784.23	179.93	56.83	236.76
260	869.62	854.92	185.99	50.71	236.70
270	944.38	929.68	193.09	43.53	236.62
280	1023.3	1008.6	201.48	33.64	235.64
290	1106.3	1091.6	211.45	12.44	223.89
291.2	1153.93	1139.24	218.34	0.00	218.34

From R.E. Hulme and A.B. Tillman, Chem. Eng. 56. 101 (Jan, 1949).