3.3(c2) Temperature Dependency Liquid Viscosity for Propane  |POLVER05_ |4
18  6 
TK	mu	logmu=log(mu)	invTK=1 / TK	logT=log(TK)	T2=TK ^ 2
100	3.82E-03	-2.417937	0.01	2.	10000.
110	2.29E-03	-2.640165	0.0090909	2.041393	1.21E+04
120	1.53E-03	-2.815309	0.0083333	2.079181	1.44E+04
130	1.08E-03	-2.966576	0.0076923	2.113943	1.69E+04
140	8.32E-04	-3.079877	0.0071429	2.146128	1.96E+04
150	6.59E-04	-3.181115	0.0066667	2.176091	2.25E+04
160	5.46E-04	-3.262807	0.00625	2.20412	2.56E+04
170	4.53E-04	-3.343902	0.0058824	2.230449	2.89E+04
180	3.82E-04	-3.417937	0.0055556	2.255273	3.24E+04
190	3.36E-04	-3.473661	0.0052632	2.278754	3.61E+04
200	2.87E-04	-3.542118	0.005	2.30103	4.0E+04
220	2.24E-04	-3.649752	0.0045455	2.342423	4.84E+04
240	1.80E-04	-3.744727	0.0041667	2.380211	5.76E+04
260	1.44E-04	-3.841638	0.0038462	2.414973	6.76E+04
270	1.30E-04	-3.886057	0.0037037	2.431364	7.29E+04
280	1.17E-04	-3.931814	0.0035714	2.447158	7.84E+04
290	1.05E-04	-3.978811	0.0034483	2.462398	8.41E+04
300	9.59E-05	-4.018181	0.0033333	2.477121	9.0E+04
*