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4
3
2
1
0
-1
-2
-3
-4
6
5
4
3
2
1
50
100
150
200
250
300
350
Reservoir Temperature, °F
Lee, Gonzales, and Eakin
Londono et al.
Sutton
Poling et al.
Fig. 2-5. Comparisons of relative errors in gas viscosity correlations using data of table 2-4 sorted
and split by temperature. All calculations used the Piper et al. pseudocritical temperature and
pseudocritical pressure equations. The Dranchuk-Abou-Kassem z-factor equations were used to
obtain gas densities as required.
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