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%	5%	-	10%	-	5%	5%
Reference	[5]	[6]	[2,7]	[2,7]	[8]	[8]	[9-11]	[9,11]
75	3.50	44.07	-345.5	579.4	25834	-30427	6.3	4.9
80	3.50	83.65	-300.8	501.8	23762	-33180	6.8	5.3
85	3.50	146.17	-264.7	439.6	21740	-33208	7.3	5.6
90	3.50	238.79	-235.0	389.3	19874	-31936	7.7	6.0
95	3.50	369.17	-210.3	348.2	18195	-30089	8.2	6.3
100	3.50	545.28	-189.4	314.2	16703	-28043	8.7	6.7
110	3.50	1068.16	-156.2	261.8	14222	-24023	9.7	7.4
120	3.50	1879.21	-131.1	223.6	12287	-20501	10.6	8.0
130	3.50	3063.14	-111.5	194.8	10766	-17564	11.5	8.7
140	3.50	-	-95.8	172.5	9555	-15149	12.4	9.3
150	3.50	-	-82.9	154.6	8580	-13167	13.3	9.9
160	3.50	-	-72.2	140.1	7784	-11534	14.2	10.5
170	3.50	-	-63.1	128.2	7127	-10180	15.0	11.1
180	3.50	-	-55.3	118.1	6578	-9049	15.9	11.7
190	3.50	-	-48.6	109.5	6115	-8097	16.7	12.2
200	3.50	-	-42.7	102.1	5721	-7291	17.5	12.8
210	3.50	-	-37.4	95.7	5382	-6602	18.3	13.3
220	3.50	-	-32.8	90.0	5089	-6010	19.1	13.8
230	3.50	-	-28.6	85.0	4833	-5499	19.9	14.4
240	3.50	-	-24.9	80.6	4609	-5054	20.7	14.9
250	3.50	-	-21.5	76.6	4411	-4665	21.4	15.4
260	3.50	-	-18.4	73.0	4234	-4323	22.2	15.9
270	3.50	-	-15.5	69.7	4077	-4021	22.9	16.4
280	3.50	-	-12.9	66.7	3936	-3753	23.7	16.8
290	3.50	-	-10.5	64.0	3808	-3514	24.4	17.3
300	3.50	-	-8.3	61.5	3693	-3301	25.1	17.8
310	3.51	-	-6.3	59.2	3588	-3109	25.8	18.2
320	3.51	-	-4.3	57.1	3492	-2936	26.5	18.7
330	3.51	-	-2.5	55.1	3404	-2781	27.2	19.1
340	3.51	-	-0.9	53.3	3323	-2639	27.9	19.5
350	3.51	-	0.7	51.5	3249	-2511	28.6	20.0
360	3.52	-	2.2	49.9	3179	-2394	29.3	20.4
370	3.52	-	3.6	48.4	3115	-2287	29.9	20.8
380	3.52	-	4.9	47.0	3056	-2189	30.6	21.2
390	3.52	-	6.1	45.7	3000	-2099	31.3	21.6
400	3.53	-	7.3	44.4	2948	-2016	31.9	22.0
410	3.53	-	8.4	43.2	2899	-1939	32.6	22.4
420	3.54	-	9.4	42.1	2853	-1869	33.2	22.8
430	3.54	-	10.4	41.1	2810	-1803	33.8	23.2
440	3.55	-	11.4	40.0	2769	-1743	34.5	23.6
450	3.55	-	12.3	39.1	2731	-1686	35.1	24.0
460	3.56	-	13.2	38.2	2694	-1634	35.7	24.3
470	3.56	-	14.0	37.3	2660	-1585	36.3	24.7
480	3.57	-	14.8	36.5	2627	-1539	37.0	25.1
490	3.58	-	15.5	35.7	2596	-1497	37.6	25.4
500	3.58	-	16.3	34.9	2566	-1457	38.2	25.8
550	3.62	-	19.5	31.6	2435	-1290	41.2	27.6
600	3.66	-	22.1	28.8	2328	-1165	44.0	29.2
650	3.70	-	24.4	26.5	2239	-1069	46.9	30.8
700	3.74	-	25.2	20.8	2163	-994	49.6	32.4
750	3.78	-	26.6	18.8	2096	-934	52.3	33.8
800	3.81	-	27.8	17.0	2038	-885	54.9	35.3
850	3.84	-	28.7	15.5	1985	-844	57.4	36.7
900	3.87	-	29.6	14.1	1938	-809	60.0	38.0
950	3.90	-	30.3	12.9	1895	-780	62.4	39.3
1000	3.91	-	31.0	11.9	1856	-755	64.8	40.6

References:

1. IUPAC; "Atomic Weights of the Elements 1993"; J. Phys. Chem. Ref. Data 1995, 24, 1561.
2. "Selected Values of Properties of Chemical Compounds", Data Project; Thermodynamics Research Center, Texas A&M University, College Station, Texas, 1980-extant. loose-leaf data sheets.
3. B. J. Zwolinski, A. P. Kudchadker, G. H. Alani, "The Critical Constants of Organic Substances", Chem. Rev. 1968, 68, 659.
4. "TRC Thermodynamic Tables-Hydrocarbons", Thermodynamics Research Center, The Texas A&M University System, College Station, TX, 1985.
5. R. D. Goodwin, "Carbon Monoxide Thermophysical Properties from 68 to 1000K at Pressures to 100 MPa", J. Phys. Chem. Ref. Data 1985, 14, 849.
6. D. R. Stull, "Vapor Pressure of Pure Substances", Ind. Eng. Chem. 1947, 39, 517.
7. G. Saville, M. N. DaPointe, J. C. G. Calado, S. F. Barreiros, "Second Virial Coefficients of Carbon Monoxide", J. Chem. Thermo. 1987, 19, 947.
8. Calculated from a Lennard-Jones model fit to Ref [2,7] second virial coefficients.
9. K. Stephan, K. Lucas, "Viscosity of Dense Fluids", New York: Plenum Press, 1979.
10. "Thermal Conductivity 17", Thermophysical Properties Division, Nat. Bur. Stand., Boulder, CO, 1983, 294.
11. "Thermophysical Properties of Matter", IFI/Plenum, New York, 1970.

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