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Gas-bubble hold-up and axial dispersion coefficient of emulsion phases in fluidized beds

✍ Scribed by Y. Kawase; M. Moo-Young

Book ID
112055229
Publisher
John Wiley and Sons
Year
1987
Tongue
English
Weight
276 KB
Volume
65
Category
Article
ISSN
0008-4034

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πŸ“œ SIMILAR VOLUMES

Gas exchange between the bubble and emul
Gas exchange between the bubble and emulsion phases in gas-solid fluidized beds
✍ T. Chiba; H. Kobayashi πŸ“‚ Article πŸ“… 1970 πŸ› Elsevier Science 🌐 English βš– 967 KB

Experimental studies for measuring the extent of gas exchange between the bubble and emulsion phases in gas-solid fluidized beds were conducted using ozone as a tracer. Measurements were made on the changes of ozone concentration immediately inside the bubbles which were injected successively into t

Gas hold-up and axial mixing in the flui
Gas hold-up and axial mixing in the fluid phase of bubble columns
✍ T. Reith; S. Renken; B.A. IsraΓ«l πŸ“‚ Article πŸ“… 1968 πŸ› Elsevier Science 🌐 English βš– 722 KB

Gas hold-up and liquid phase axial dispersion coefficient have been measured in water filled bubble columns of 5.08, 14.0 and 29sOcm dia. as a function of the superficial gas velocity. From the gas hold-up measurements the following relationship between the relative velocity between gas and liquid,

Effect of dispersing bubbles into liquid
Effect of dispersing bubbles into liquid fluidized beds on heat transfer and hold-up at constant bed expansion
✍ S. Viswanathan; A.S. Kakar; P.S. Murti πŸ“‚ Article πŸ“… 1965 πŸ› Elsevier Science 🌐 English βš– 647 KB

Results on heat transfer coefficients and gas-holdup were reported when small quantities of air were dispersed in a liquid (water) fluidized bed of quartz particles (928 and 649 TV mean dia.), the weight of which was varied from 250 to 1250 g. In the case of holdup studies, glass beads of 4 mm were