## Abstract Gasβsolids fluidized beds are characterized by the presence of gas voids or bubbles causing a massβtransfer 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
Predictive model and deterministic mechanism in a bubbling fluidized bed
β Scribed by Gui-Bing Zhao; Ji-Zhong Chen; Yong-Rong Yang
- Publisher
- American Institute of Chemical Engineers
- Year
- 2001
- Tongue
- English
- Weight
- 919 KB
- Volume
- 47
- Category
- Article
- ISSN
- 0001-1541
No coin nor oath required. For personal study only.
β¦ Synopsis
Abstract
A predictive model based on the theory of phase space reconstruction was proposed to study the determinism and predictability of dynamics underlying pressure fluctuations by measuring and analyzing the time series of pressure signals at different locations in a bubble bed with 0.3 m in dia. and 3 m in height. Chaotic invariants (correlation dimension, K~2~ entropy, and Lyapunov exponent spectrum) of measured and modelβgenerated time series of pressure signals were nearly the same. The model captured some important nonlinear characteristics of the real system, which can be used to study the dynamics of fluidizing system. Deterministic dynamics underlying pressure signals were confirmed to exist. A new characteristic index defined as the determining level of dynamics was used to analyze deterministic degrees at different gas velocities and locations of the wall in the bed. Since prediction errors of pressure fluctuations grow exponentially with time at short time scales and the exponent separation rate between predicted and measured values is proportional to the maximal Lyapunov exponent, the longβterm predictability of pressure fluctuations is impossible. This verified chaotic properties of fluctuation dynamics in the fluidized bed with deterministic mechanism and sensitive dependence on initial conditions.
π SIMILAR VOLUMES
## Abstract Modeling and measurement of bubble size in a rotating fluidized bed (RFB) is described. A novel model of bubble growth has been proposed based on a bubble coalescence model by Darton et al. We modified the model according to the following concepts: (i) local centrifugal acceleration and