Boiling incipience in a reboiler tube [Erratum to document cited in

Cussler, E. L.Diffusion: Mass Transfer in Fluid Systems; Cam- bridge: New York ... McHugh, A.J.; Spevacek, A. J. A Technique for Monitoring the. Kinet...
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452 Ind. Eng. Chem. Res., Vol. 31, No. 1, 1992 Bearman, R.J. On the Molecular Basis of Some Current Theories of Diffusion. J. Phys. Chem. 1961,65,1961-1968. Born, M.; Wolf, E. Principles of Optics; Pergamon: New York, 1989; pp 424-428. Cussler, E. L. Diffusion: Mass Transfer in Fluid Systems; Cambridge: New York, 1984;pp 133-137. Gaides, G. E. Measurement and Analysis of Bath-Side Interfacial Concentration Gradienta During Membrane Quenching by Phase Inversion. Ph.D. Dissertation, University of Illinois at Urbana, 1992. Johnston, R. C.; Lobdell, C. 0.;Janauer, G. E. Cation Exchange in Mixed Solvent Media. 2. Alkali Ion and Solvent Self-Diffusion in Dowex 50W-Dimethyl Sulfoxide-Water. J. Phys. Chem. 1979, 83,1816-1820. Klein, M. V.; Furtak, T. E. Optics; Wiley: New York, 1986;p 485. McHugh, A. J.; Spevacek, A. J. A Technique for Monitoring the Kinetics of Flow-Induced Crystallization. J. Polym. Sci., Polym. Lett. Ed. 1987,2.5,105-110.

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Chorng-Shyuan Teay, Anthony J. McHugh* Department of Chemical Engineering University of Illinois Urbana, Illinois 61801 Received for review July 23, 1991 Revised manuscript received October 30, 1991 Accepted November 12, 1991

ADDITIONS AND CORRECTIONS Boiling Incipience in a Reboiler Tube [Volume 30, Number 3, Page 5621. Hamid Mi* and S. S. Alam Page 567. In eq 9, the value of the constant should be 0.0405 and not 0.405 as printed. The correct equation is therefore

9)

0.216

X 100 = 0 . 0 4 0 5 ( ~ ~ B ~ 0 . 3 0 8 ~ ~ " ~ 0 . 3 6 6 ~ .(9) 6g2( L zOB