𝔖 Bobbio Scriptorium
✦   LIBER   ✦

Minimum fluidization velocity and gas holdup in gas–liquid–solid fluidized bed reactors

✍ Scribed by K Ramesh; T Murugesan


Publisher
Wiley (John Wiley & Sons)
Year
2002
Tongue
English
Weight
173 KB
Volume
77
Category
Article
ISSN
0268-2575

No coin nor oath required. For personal study only.

✦ Synopsis


Abstract

Experiments were performed to study the hydrodynamics of a cocurrent three‐phase fluidized bed with liquid as continuous phase. Based on the 209 experimental data (with four liquid systems and five different particles) along with 115 literature data from six different sources on minimum fluidization velocity, a unique correlation for the estimation of minimum fluidization velocity in two‐phase (u~g~ = 0) as well as in three‐phase systems is developed. A data bank consisting of 1420 experimental measurements for the fractional gas phase holdup data with a wide range of variables is used for developing empirical correlations. Separate correlations are developed for two flow regimes observed in this present work. The proposed correlations are more accurate and simpler to use.

© 2002 Society of Chemical Industry


📜 SIMILAR VOLUMES


Gas holdup in a three-phase fluidized be
✍ M. Safoniuk; J. R. Grace; L. Hackman; C. A. McKnight 📂 Article 📅 2002 🏛 American Institute of Chemical Engineers 🌐 English ⚖ 258 KB 👁 3 views
Local phase holdups in gas-solids fluidi
✍ Hsiaotao T. Bi; Peng-Cheng Su 📂 Article 📅 2001 🏛 American Institute of Chemical Engineers 🌐 English ⚖ 197 KB 👁 2 views

## Abstract A two‐phase structural model consisting of a dense phase and a dilute phase with allowance for the dense‐phase expansion and the solids holdup in the dilute phase was developed and successfully applied to the analysis of local voidage fluctuation signals. Such a model can be used to der

Particle holdup in a liquid–solid circul
✍ Kenichi Hashizume; Shinichi Morita 📂 Article 📅 2008 🏛 John Wiley and Sons 🌐 English ⚖ 417 KB 👁 1 views

## Abstract An experiment was conducted to acquire a set of systematic data of particle holdup in risers of a liquid–solid circulating fluidized bed. In the experiment, two kinds of riser were provided, their inner diameter being 24 mm and 36 mm, respectively. Tested particles were of glass and cer

Modified gas-perturbed liquid model (GPL
✍ V Sivasubramanian; M Velan 📂 Article 📅 2006 🏛 Wiley (John Wiley & Sons) 🌐 English ⚖ 154 KB 👁 1 views

## Abstract In the present investigation minimum fluidization velocity, __U__~mf~, in a two‐phase inverse fluidized bed reactor is determined using low‐density polyethylene and polypropylene particles of different diameters (4,6 and 8 mm) by measuring pressure drop. In a glycerol system __U__~mf~ d