3.3(c1) Temperature Dependency Liquid Viscosity for Propane  |POLVER05_ |4
18  6 
TK	mu	logmu=log(mu)	invTKplusC=1 / (TK - 26.18)	invTK=1 / TK	TKton=TK ^ 0.5
100	3.82E-03	-2.417937	0.0135465	0.01	10.
110	2.29E-03	-2.640165	0.0119303	0.0090909	10.48809
120	1.53E-03	-2.815309	0.0106587	0.0083333	10.95445
130	1.08E-03	-2.966576	0.0096321	0.0076923	11.40175
140	8.32E-04	-3.079877	0.0087858	0.0071429	11.83216
150	6.59E-04	-3.181115	0.0080762	0.0066667	12.24745
160	5.46E-04	-3.262807	0.0074727	0.00625	12.64911
170	4.53E-04	-3.343902	0.0069531	0.0058824	13.0384
180	3.82E-04	-3.417937	0.0065011	0.0055556	13.41641
190	3.36E-04	-3.473661	0.0061043	0.0052632	13.78405
200	2.87E-04	-3.542118	0.0057531	0.005	14.14214
220	2.24E-04	-3.649752	0.0051594	0.0045455	14.8324
240	1.80E-04	-3.744727	0.0046768	0.0041667	15.49193
260	1.44E-04	-3.841638	0.0042768	0.0038462	16.12452
270	1.30E-04	-3.886057	0.0041014	0.0037037	16.43168
280	1.17E-04	-3.931814	0.0039398	0.0035714	16.7332
290	1.05E-04	-3.978811	0.0037905	0.0034483	17.02939
300	9.59E-05	-4.018181	0.003652	0.0033333	17.32051
*
logmu=A+B/(TK+C)
A=-4.51	B=159.9	C=-26.18