4. Direct gas-solid contact heat exchange
The type of contactor and the material transport mode in the [22] contactor can be defined according to the value of the relative speed ur in relation to the fall limit speed and the minimum fluidization speed umf (table 10).
As a reminder, the minimum fluidization velocity represents the apparent fluid velocity required to support the solid and give it properties relatively similar to those of a fluid [48]. It can be deduced from the following...
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Direct gas-solid contact heat exchange
Bibliography
References
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(1) - PERRY (R.H.) (coordinateur) - Chemical engineers' handbook. - McGraw-Hill New York 1984.
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(2) - KOLEV (N.I.) - Fragmentation and Coalescence Dynamics in Multiphase Flows. - Experimental Thermal and Fluid Science 6 p. 211-251 1993.
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