(ProQuest Information and Learning: ... denotes formulae omitted.)
Calculating Pipeline Pressure Drop
To the Editor:
The article "Pipeline Pressure Drop: A New Design Correlation," written by Roger Gilmont in the June 2006 issue of CEP (pp. 34-41) and the response by Kevin Farrell
...
The iterative solution of this expression for a specified value of Re converges rapidly, even with a handheld programmable calculator. The unfamiliar second and third terms on the right-hand side are a necessary consequence of the viscous boundary layer near the wall. They become significant in magnitude only near the lower limit of fully developed turbulent flow, namely Re = 4,000.
Stuart Churchill
Univ. of Pennsylvania
Clarification on Pharmaceutical Compound Solubilities
In the article "Predicting Solubilities of Pharmaceutical Compounds" (Aug. 2006, pp. 20-21), the fourth parameter in Eq. 3, d, was not defined. Due to page constraints, the equation that defined d was not included in article. It was, however, defined in the original paper:
...
where m is the number of components in the system. Note that A is also a function of the bulk properties:
...
where: d is a constant; d^sub solute^ and ... the solute and average dielectric constants. All of these parameters are at 25?C.
For more detailed information, please read the authors' original manuscript: Mirmehrabi, M., Rohani, S. and L. Perry, "Thermodynamic Modeling of Activity Coefficient and Prediction of Solubility: Part 1. Predictive Models," J. Pharm. Sci. 95 (4), pp. 790-797 (2006).
Readers who are interested in receiving the original manuscript may contact the authors and request copies. Mahmoud Mirmehrabi can be reached at (514) 748-4730 or mirmehma@wyeth.com. Please he sure to give your complete mailing address information (P.O. box numbers will not be accepted ). -Editors
We Look forward to receiving your letters. Please, send them to cepedit@aiche.org