Correction for “Mixing of Newtonian and Non-Newtonian Fluids in a

Dec 12, 2012 - Table 1. Parameters for the Hershel−Bulkley Model conc (w/w%) τ0 (Pa) k (Pa sn) n. Re. N = 327 rpm. N = 416 rpm. N = 565 rpm. N = 68...
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Correction for “Mixing of Newtonian and Non-Newtonian Fluids in a Cylindrical Mixer Equipped with a Side-Entry Impeller” J. Sossa-Echeverria and F. Taghipour Ind. Eng. Chem. Res. 2012, 51 (46), 15258-15267, DOI: 10.1021/ie300979y Because of a production error, the version of this paper that was published online November 8, 2012 and in print in a subsequent print issue of Industrial & Engineering Chemistry Research (Volume 51, Issue 46) was missing Table 1. This table should appear as shown below: The Journal Production staff regret this error and apologize for any confusion that this omission may have caused. Table 1. Parameters for the Hershel−Bulkley Model Re conc (w/w%)

τ0 (Pa)

k (Pa s )

n

0.075 0.09 0.1

4.9 ± 0.4 10.8 ± 0.8 16 ± 0.9

1.32 1.99 3.94

0.4 0.4 0.4

n

N = 327 rpm

N = 416 rpm

N = 565 rpm

N = 684 rpm

16581 10913 5463

24370 16039 8030

39773 26176 13104

54003 35542 17793

Published: December 12, 2012 © 2012 American Chemical Society

16763

dx.doi.org/10.1021/ie3032845 | Ind. Eng. Chem. Res. 2012, 51, 16763−16763