4. Turbulent fluidization, transported beds, circulating beds
If the fluidization speed is increased beyond the usual values for bubbling fluidization, at some point the bubbles lose their regular shape and form vertical jets of varying size in the fluidized bed. This turbulence in the fluidized bed is such that not only do bubble formation and coalescence become random, but it also becomes difficult to distinguish the bed surface. Under these conditions, the concepts and theories developed for bubbling fluidized beds are no longer valid, and cannot correctly describe the behavior of the bed, particularly with regard to bubble/suspension material transfer.
A great deal of research has been devoted to defining the limiting velocity of bubbling fluidization, known as the transition velocity. However, no particular theory has emerged from this work. In fact, the transition from bubbling to turbulent fluidization is gradual and...
Exclusive to subscribers. 97% yet to be discovered!
You do not have access to this resource.
Click here to request your free trial access!
Already subscribed? Log in!
The Ultimate Scientific and Technical Reference
This article is included in
Unit operations. Chemical reaction engineering
This offer includes:
Knowledge Base
Updated and enriched with articles validated by our scientific committees
Services
A set of exclusive tools to complement the resources
Practical Path
Operational and didactic, to guarantee the acquisition of transversal skills
Doc & Quiz
Interactive articles with quizzes, for constructive reading
Turbulent fluidization, transported beds, circulating beds
References
Exclusive to subscribers. 97% yet to be discovered!
You do not have access to this resource.
Click here to request your free trial access!
Already subscribed? Log in!
The Ultimate Scientific and Technical Reference