Drop size in power law non‐newtonian systems
- 1 February 1972
- journal article
- research article
- Published by Wiley in The Canadian Journal of Chemical Engineering
- Vol. 50 (1) , 41-44
- https://doi.org/10.1002/cjce.5450500108
Abstract
Drop volume studies were made by forming non‐Newtonian pseudoplastic drops in a continuous toluene phase and chlorobenzene drops in non‐Newtonian continuous phases. Combination of results for these cases enabled development of a correlation for the prediction of non‐Newtonian drop volume in a non‐Newtonian continuous phase. The development is confined to power law fluids and provides expressions for both long and short nozzles in terms of a two‐stage drop formation process. Variables included nozzle size, formation time, and rheological properties from eight non‐Newtonian systems in a program of 144 runs.Keywords
This publication has 12 references indexed in Scilit:
- Formation of organic drops in waterAIChE Journal, 1971
- Drop formation in liquid—liquid systems—I prediction of drop volumes at moderate speed of formationChemical Engineering Science, 1971
- Drop formation at low velocities in liquid‐liquid systems: Part I. Prediction of drop volumeAIChE Journal, 1968
- Drop formation studies in liquid—liquid systemsChemical Engineering Science, 1966
- Studies of bubble formation and riseThe Canadian Journal of Chemical Engineering, 1960
- Drop formation in liquid‐liquid systems from single nozzlesAIChE Journal, 1958
- Size of drops formed at the end of single nozzlesChemical engineering, 1957
- Zur Entstehung von Tropfendispersionen an Siebböden bei der SolventextraktionChemie Ingenieur Technik - CIT, 1956
- Drop Formation in Two-Liquid-Phase SystemsIndustrial & Engineering Chemistry, 1950
- THE DETERMINATION OF SURFACE TENSION (FREE SURFACE ENERGY), AND THE WEIGHT OF FALLING DROPS: THE SURFACE TENSION OF WATER AND BENZENE BY THE CAPILLARY HEIGHT METHOD.Journal of the American Chemical Society, 1919