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. 2022 Oct 10;36(20):12563–12579. doi: 10.1021/acs.energyfuels.2c02625

Figure 2.

Figure 2

Relative difference between the kinematic viscosity measured at −40 °C and estimated from viscosity data above −20 °C using eq 1 as a function of the initial boiling point of the petroleum-based kerosene cuts and the synthetic distillate cuts. The final boiling point was 5 °C above the initial boiling point. Positive differences indicate an overestimation of the viscosity by eq 1, whereas negative values indicate an underestimation. The full data set is presented in Tables S9 and S10 in the Supporting Information.