𝔖 Bobbio Scriptorium
✦   LIBER   ✦

Bubbles in a fluidized bed: A fast X-ray scanner

✍ Scribed by R. F. Mudde


Publisher
American Institute of Chemical Engineers
Year
2010
Tongue
English
Weight
447 KB
Volume
57
Category
Article
ISSN
0001-1541

No coin nor oath required. For personal study only.


πŸ“œ SIMILAR VOLUMES


Controlling bubble coalescence in a flui
✍ Robert Jan de Korte; Jaap C. Schouten; Cor M. van den Bleek πŸ“‚ Article πŸ“… 2001 πŸ› American Institute of Chemical Engineers 🌐 English βš– 179 KB πŸ‘ 2 views

## Abstract Gas–solids fluidized beds are characterized by the presence of gas voids or bubbles causing a mass‐transfer resistance. Enhancing the mass transfer from the bubbles to the emulsion phase by reducing the bubble size can be advantageous for the chemical performance (like the conversion an

Fluidization of Ultrafine Particles in a
✍ Q. Guo; M. Wang; Y. Li; C. Yang πŸ“‚ Article πŸ“… 2005 πŸ› John Wiley and Sons 🌐 English βš– 234 KB πŸ‘ 1 views

However, the bubbling up vapor flows just through the downcomer bottom-orifices. The vapor occupies the part the of orifice area, so the orifice area for liquid descending is reduced and the downcomer liquid height increases which causes a premature downcomer flood as well. Moreover, the orifice are

Estimation of bed expansions in a freely
✍ A. Hepbasli πŸ“‚ Article πŸ“… 1998 πŸ› John Wiley and Sons 🌐 English βš– 178 KB πŸ‘ 2 views

Knowledge of bed expansions is important in the design and operation of gas-solid fluidized beds. This paper presents a study on the estimation of expanded bed height in a large three-dimensional gas-fluidized bed with a square section of 0)61;0)61 m. All experiments were performed at the freely bub

Fluid dynamic simulation of O3 decomposi
✍ Madhava Syamlal; Thomas J. O'Brien πŸ“‚ Article πŸ“… 2003 πŸ› American Institute of Chemical Engineers 🌐 English βš– 285 KB πŸ‘ 2 views

## Abstract Recent advances in dense, multiphase, computational fluid dynamics (CFD) have allowed accurate simulation of the gas and particle motion in bubbling and circulating fluidized beds. Since fluidized‐bed reactors are used for many chemical processes, a simulation must also be able to accur