𝔖 Bobbio Scriptorium
✦   LIBER   ✦

Mass transfer in a pulsating bubble

✍ Scribed by V.S. Berman; A.D. Polyanin


Publisher
Elsevier Science
Year
1988
Tongue
English
Weight
632 KB
Volume
52
Category
Article
ISSN
0021-8928

No coin nor oath required. For personal study only.


πŸ“œ SIMILAR VOLUMES


Mass transfer in a recirculating bubble
✍ D.A. Lewis; J.F. Davidson πŸ“‚ Article πŸ“… 1985 πŸ› Elsevier Science 🌐 English βš– 470 KB

The mass transfer of oxygen between air and water in a recirculating bubble column has been studied, at gas and water superficial velocities of up to 0.23 m SK' and 0.68 m s-l respectively. Experiments show that the assumption of plug flow for the gas phase is reasonable, eliminating a possible sour

Heat transfer characteristics in a pulsa
✍ Akira Nishimura; Seiichi Deguchi; Hitoki Matsuda; Masanobu Hasatani; Arun S. Muj πŸ“‚ Article πŸ“… 2002 πŸ› John Wiley and Sons 🌐 English βš– 231 KB πŸ‘ 1 views

## Abstract A pulsating fluidized bed is operated with two sequential durations designated as an on‐period with injecting fluidization gas and an off‐period without it. The heat transfer coefficient between a vertically immersed heater and bed in a pulsating fluidized bed is measured under various

Oxygen mass transfer in bubble columns
✍ M. Alvarez-Cuenca; C.G.J. Baker; M.A. Bergougnou πŸ“‚ Article πŸ“… 1980 πŸ› Elsevier Science 🌐 English βš– 755 KB

The mass transfer of oxygen between an and water has been studled m a bubble column over wide ranges of hquld and gas velocity An oxygen probe was used to map the steady-state hqmd phase concentration of oxygen throughout the column At any given pomt m the column, the oxygen concentration mcreased w

Mass transfer to bubbles
✍ J. Bridgwater; G.S. McNab πŸ“‚ Article πŸ“… 1972 πŸ› Elsevier Science 🌐 English βš– 298 KB
Mass transfer in continuous bubble colum
✍ Y. Kang; B. T. Min; J. B. Nah; S. D. Kim πŸ“‚ Article πŸ“… 1990 πŸ› American Institute of Chemical Engineers 🌐 English βš– 355 KB πŸ‘ 2 views

Bubble column reactors are widely used in the fields of petrochemical, biochemical, and chemical engineering processes. They are comparable to other multiphase reactors because of their simplicity, low operating costs, and higher heat and mass transfer coefficients between phases. Since a continuous