Table 3 should be corrected as shown below to list a reference temperature of 311 K which was used throughout the Zolper et al. [1] manuscript. The fit parameters in the table are unchanged.

Table 3

Parameters for the Tait-Doolittle equation taken from density and viscosity measurements over a range of pressures and temperatures with the reference temperatures set to TR = 311 K for all samples

The authors originally used Blok’s integral to calculate the pressure–viscosity index. On further review, it was found that Bair and Qureshi’s [2] equation below gives better results
α*=[η0αNηN+i=1Nη0αiηiηi1ηiηi1]1,αi=ln(ηi/ηi1)PiPi1
(5)

Table 4 has been revised to include the recalculated the pressure–viscosity indices using Bair and Qureshi’s [2] equation and the measured pressure–viscosity data.

Table 4

Reciprocal asymptotic pressure–viscosity index α* at measurement temperatures for individual samples calculated by the method of Bair and Qureshi [2]

Sample273 K293 K298 K311 K372 K478 K492 K
1-A17.114.212.79.06.7
8-C27.923.821.214.49.2
9-C13.913.19.38.77.2
10-C19.317.015.110.66.4
11-C31.213.87.44.4
12-C26.022.219.413.37.9
13-D28.525.241.54.9
15-D23.211.49.8
17-D32.721.017.913.06.6
18-D27.121.018.210.98.0
19-D18.314.312.99.2
21-D16.914.112.78.55.5
23-D22.617.115.58.94.8
24-E29.321.019.213.17.3
25-E26.620.530.312.39.0
26-E26.622.019.012.45.6
27-E26.320.619.312.15.9
28-F24.422.015.27.6
29-F31.027.716.210.0
30-F24.721.914.6
31-G32.122.921.013.38.6
32-G29.724.422.115.58.7
33-G40.128.426.017.510.3
34-G30.425.022.215.29.0
35-G31.424.721.315.39.9
36-G41.731.127.417.09.3
37-G38.133.219.710.4
38-G65.347.243.623.012.7
39-G39.635.520.210.3
40-G53.038.835.419.510.2
41-G29.624.313.615.29.1
42-G39.229.127.017.38.7
44-G29.224.021.315.19.9
45-G23.314.35.9
46-G46.337.632.719.310.6
47-G50.441.637.222.211.7
48-G52.248.340.824.714.3
49-G22.719.313.39.0
50-G23.520.714.17.8
51-G39.323.620.913.65.9
52-G78.157.450.024.511.5
53-H36.826.321.415.811.7
54-H
55-H17.816.315.814.115.3
56-H24.220.618.811.96.5
Sample273 K293 K298 K311 K372 K478 K492 K
1-A17.114.212.79.06.7
8-C27.923.821.214.49.2
9-C13.913.19.38.77.2
10-C19.317.015.110.66.4
11-C31.213.87.44.4
12-C26.022.219.413.37.9
13-D28.525.241.54.9
15-D23.211.49.8
17-D32.721.017.913.06.6
18-D27.121.018.210.98.0
19-D18.314.312.99.2
21-D16.914.112.78.55.5
23-D22.617.115.58.94.8
24-E29.321.019.213.17.3
25-E26.620.530.312.39.0
26-E26.622.019.012.45.6
27-E26.320.619.312.15.9
28-F24.422.015.27.6
29-F31.027.716.210.0
30-F24.721.914.6
31-G32.122.921.013.38.6
32-G29.724.422.115.58.7
33-G40.128.426.017.510.3
34-G30.425.022.215.29.0
35-G31.424.721.315.39.9
36-G41.731.127.417.09.3
37-G38.133.219.710.4
38-G65.347.243.623.012.7
39-G39.635.520.210.3
40-G53.038.835.419.510.2
41-G29.624.313.615.29.1
42-G39.229.127.017.38.7
44-G29.224.021.315.19.9
45-G23.314.35.9
46-G46.337.632.719.310.6
47-G50.441.637.222.211.7
48-G52.248.340.824.714.3
49-G22.719.313.39.0
50-G23.520.714.17.8
51-G39.323.620.913.65.9
52-G78.157.450.024.511.5
53-H36.826.321.415.811.7
54-H
55-H17.816.315.814.115.3
56-H24.220.618.811.96.5

Table 5 caption and data should be corrected to use the specific volume v0(TR) and viscosity η0(TR) at TR = 311 K.

Table 5

Reference specific volume v0(TR) and viscosity η0(TR) at atmospheric pressure and TR = 311 K and residual ratios for all samples completed

Samplev0 (ml/g)η0 (mPa · s)
1-A1.10711.2
8-C1.17029.2
9-C1.18037.7
10-C1.18213.2
11-C1.3102.3
12-C1.16439.5
13-D1.139315.4
15-D1.15592.6
17-D1.1639.3
18-D1.1638.8
19-D1.10711.8
21-D1.0808.5
23-D1.1794.5
24-E1.116168.1
25-E1.1567.9
26-E1.18829.3
27-E1.15128.2
28-F1.14482.2
29-F1.11689.1
30-F1.031101.2
31-G1.14945.7
32-G1.147145.7
33-G1.122506.0
34-G1.148156.0
35-G1.140136.8
36-G1.10750.0
37-G1.092133.6
38-G1.073446.3
39-G1.083136.6
40-G1.083133.3
41-G1.151135.0
42-G1.13564.8
44-G1.153134.2
45-G1.1471362.0
46-G1.20345.7
47-G1.193127.8
48-G1.181436.2
49-G1.13578.1
50-G1.15546.2
51-G1.08547.8
52-G1.021621.0
53-H0.943115.5
54-H0.518175.3
55-H1.04370.6
56-H1.02929.2
Samplev0 (ml/g)η0 (mPa · s)
1-A1.10711.2
8-C1.17029.2
9-C1.18037.7
10-C1.18213.2
11-C1.3102.3
12-C1.16439.5
13-D1.139315.4
15-D1.15592.6
17-D1.1639.3
18-D1.1638.8
19-D1.10711.8
21-D1.0808.5
23-D1.1794.5
24-E1.116168.1
25-E1.1567.9
26-E1.18829.3
27-E1.15128.2
28-F1.14482.2
29-F1.11689.1
30-F1.031101.2
31-G1.14945.7
32-G1.147145.7
33-G1.122506.0
34-G1.148156.0
35-G1.140136.8
36-G1.10750.0
37-G1.092133.6
38-G1.073446.3
39-G1.083136.6
40-G1.083133.3
41-G1.151135.0
42-G1.13564.8
44-G1.153134.2
45-G1.1471362.0
46-G1.20345.7
47-G1.193127.8
48-G1.181436.2
49-G1.13578.1
50-G1.15546.2
51-G1.08547.8
52-G1.021621.0
53-H0.943115.5
54-H0.518175.3
55-H1.04370.6
56-H1.02929.2

References

1.
Zolper
,
T. J.
,
Bair
,
S.
, and
Horne
,
K.
,
2021
, “
Revisiting the ASME Pressure-Viscosity Report Using the Tait-Doolittle Equation
,”
ASME J. Tribol.
,
143
(
6
), p.
061901
.
2.
Bair
,
S.
, and
Qureshi
,
F.
,
2002
, “
Accurate Measurements of Pressure-Viscosity Behavior in Lubricants
,”
Tribol. Trans.
,
45
(
3
), pp.
390
396
.