T K		Vapor Pressure kPa	B(T) cm3·mol-1	dB/dT · T cm3·mol-1	C(T) cm6·mol-2	dC/dT · T cm6·mol-2	mW/(m·K)	µPa·s
Estimated Uncertainty	1%	1%	3%	-	5%	-	3%	3%
Reference	[4]	[3,4]	[5]	[5]	[5]	[5]	[6,7]	[6-9]
77	3.50	97.19	-267.6	524.2	-7811	102120	7.4	5.4
80	3.50	136.90	-248.3	482.6	-4451	74995	7.7	5.6
85	3.50	228.82	-220.9	425.0	-877	45186	8.2	5.9
90	3.50	360.29	-197.9	378.6	1154	27157	8.7	6.3
95	3.50	540.22	-178.5	340.6	2299	15969	9.2	6.6
100	3.50	777.99	-161.9	309.0	2925	8892	9.7	7.0
110	3.50	1467.16	-134.9	259.7	3371	1425	10.6	7.6
120	3.50	2515.42	-113.9	223.2	3342	-1681	11.5	8.3
130	3.50	-	-97.2	195.2	3151	-2900	12.4	8.9
140	3.50	-	-83.6	173.0	2919	-3272	13.3	9.5
150	3.50	-	-72.3	155.2	2692	-3259	14.1	10.1
160	3.50	-	-62.7	140.5	2487	-3077	14.9	10.7
170	3.50	-	-54.6	128.2	2308	-2829	15.8	11.3
180	3.50	-	-47.6	117.8	2154	-2565	16.6	11.8
190	3.50	-	-41.4	108.8	2022	-2309	17.4	12.4
200	3.50	-	-36.1	101.1	1910	-2071	18.2	12.9
210	3.50	-	-31.3	94.3	1814	-1855	19.0	13.4
220	3.50	-	-27.0	88.3	1732	-1661	19.7	14.0
230	3.50	-	-23.2	83.0	1662	-1490	20.5	14.5
240	3.50	-	-19.8	78.2	1602	-1337	21.2	15.0
250	3.50	-	-16.7	74.0	1550	-1203	22.0	15.5
260	3.50	-	-13.9	70.1	1505	-1084	22.7	15.9
270	3.50	-	-11.3	66.6	1466	-979	23.5	16.4
280	3.50	-	-8.9	63.4	1433	-886	24.2	16.9
290	3.50	-	-6.8	60.4	1403	-804	24.9	17.3
300	3.50	-	-4.8	57.7	1377	-731	25.6	17.8
310	3.50	-	-2.9	55.2	1354	-666	26.3	18.2
320	3.50	-	-1.2	52.9	1334	-609	27.0	18.7
330	3.51	-	0.4	50.8	1316	-557	27.7	19.1
340	3.51	-	1.9	48.8	1300	-512	28.4	19.6
350	3.51	-	3.3	46.9	1286	-471	29.1	20.0
360	3.51	-	4.6	45.2	1273	-435	29.8	20.4
370	3.51	-	5.8	43.6	1262	-402	30.5	20.8
380	3.51	-	6.9	42.1	1251	-373	31.1	21.2
390	3.52	-	8.0	40.6	1242	-347	31.8	21.7
400	3.52	-	9.0	39.3	1233	-324	32.5	22.1
410	3.52	-	10.0	38.0	1226	-303	33.1	22.5
420	3.52	-	10.9	36.8	1219	-284	33.8	22.8
430	3.53	-	11.7	35.6	1212	-267	34.4	23.2
440	3.53	-	12.5	34.5	1206	-252	35.1	23.6
450	3.53	-	13.3	33.5	1201	-238	35.7	24.0
460	3.54	-	14.0	32.5	1195	-226	36.4	24.4
470	3.54	-	14.7	31.6	1191	-215	37.0	24.8
480	3.55	-	15.4	30.7	1186	-205	37.6	25.1
490	3.55	-	16.0	29.8	1182	-196	38.3	25.5
500	3.56	-	16.6	29.0	1178	-188	38.9	25.9
550	3.59	-	19.2	25.5	1162	-159	42.0	27.7
600	3.62	-	21.3	22.5	1149	-144	45.0	29.4
650	3.66	-	23.0	20.1	1138	-136	48.0	31.1
700	3.70	-	24.4	18.0	1128	-133	50.9	32.7
750	3.74	-	25.6	16.2	1118	-134	53.8	34.2
800	3.78	-	26.6	14.7	1110	-137	56.6	35.8
850	3.82	-	27.4	13.4	1101	-141	59.4	37.3
900	3.86	-	28.1	12.2	1093	-146	62.2	38.7
950	3.90	-	28.8	11.1	1085	-151	64.9	40.1
1000	3.93	-	29.3	10.2	1077	-156	67.6	41.5

References:

1. IUPAC; "Atomic Weights of the Elements 1993"; J. Phys. Chem. Ref. Data 1995, 24, 1561.
2. "Standard Tables of Physical Constants of Paraffin Hydrocarbons and Other Components of Natural Gas", Publication No. 2145-84; Gas Processors Association, Tulsa, Oklahoma, 1984.
3. "IUPAC; International Thermodynamic Tables of the Fluid State-Nitrogen", Pergammon Press, Oxford, 1979.
4. "TRC Thermodynamic Tables-Hydrocarbons", Thermodynamics Research Center, The Texas A&M University System, College Station, TX, 1985.
5. J. F. Estela-Uribe and J. P. M. Trusler, "Acoustic and volumetric virial coefficients of nitrogen", Inter. J. Thermophys., In Press.
6. H. J. M. Hanley, J. F. Ely, "The Viscosity and Thermal Conductivity Coefficients of Dilute Nitrogen and Oxygen", J. Phys. Chem. Ref. Data 1973, 2, 735.
7. R. D. McCarty, W. M. Haynes, H. J. M. Hanley, "The Viscosity and Thermal Conductivity Coefficients for Dense Gaseous and Liquid Argon, Krypton, Xenon, Nitrogen, and Oxygen", J. Phys. Chem. Ref. Data 1974, 3, 979.
8. W. A. Wakeham, W. A. Cole, "The Viscosity of Nitrogen, Oxygen and their Binary Mixtures in the Limit of Zero Density", J. Phys. Chem. Ref. Data 1985, 14, 209.
9. B. A. Younglove, "Thermophysical Properties of Fluids.1. Argon, Ethylene, Parahydrogen, Nitrogen, Nitrogen trifluoride, and Oxygen", J. Phys. Chem. Ref. Data 1982, 11. Suppl. No. 1.

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