Drop Breakup in Stirred-Tank Contactors. Part III: Correlations for Mean Size and Drop Size Distribution.
| dc.contributor.author | Calabrese, Richard V. | en_US |
| dc.contributor.author | Wang, C.Y. | en_US |
| dc.contributor.author | Bryner, Nelson P. | en_US |
| dc.contributor.department | ISR | en_US |
| dc.date.accessioned | 2007-05-23T09:37:43Z | |
| dc.date.available | 2007-05-23T09:37:43Z | |
| dc.date.issued | 1987 | en_US |
| dc.description.abstract | In Part II, the extent to which dispersed-phase viscosity and interfacial tension influence equilibrium mean drop size and drop size distribution was determined for dilute suspensions produced in baffled cylindrical tanks of standard geometry equipped with six-blade Rushton turbines. Low to moderate viscosity dispersed- phase systems behaved similarly in that Sauter mean diameter could be correlated using the mechanistic arguments of Part I, and drop sizes, normalized with respect to D_32, could be correlated by a normal distribution in volume. Limited moderate viscosity data were reported in Part I but were not used to develop the correlations of Part II. The objective of this study is to combine the low to moderate viscosity data of Parts I and II with those obtained by other investigators to obtain correlations of broader utility, and to extend these via mechanistic arguments so that they apply to nondilute systems. | en_US |
| dc.format.extent | 177063 bytes | |
| dc.format.mimetype | application/pdf | |
| dc.identifier.uri | http://hdl.handle.net/1903/4595 | |
| dc.language.iso | en_US | en_US |
| dc.relation.ispartofseries | ISR; TR 1987-87 | en_US |
| dc.title | Drop Breakup in Stirred-Tank Contactors. Part III: Correlations for Mean Size and Drop Size Distribution. | en_US |
| dc.type | Technical Report | en_US |
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