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A fluidized bed reactor model is presented which describes the catalytic reaction occurring in a fluid bed as an absorption from the bubble phase with a subsequent pseudohomogeneous reaction in the catalyst suspension phase surrounding the bubbles.
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The new endoscopic-laser PIV/DIA technique (ePIV/DIA) allows to determine simultaneously information from the emulsion and bubble phase with high spatial and temporal resolution in a pseudo-2D columns.
The volume ratio of the wake to the bubble phases decreases with an increase in gas velocity.
The variation of visible bubble phase voidage with bed thickness follows a logarithmic relationship.
There is a good chance that the Nasdaq has entered the final bubble phase of a bull market.
The mean voidage corresponding at the bubble phase increased with gas superficial velocity according to a first-order model, and the mean voidage in emulsion phase rose proportionally with gas superficial velocity.
In my Nov. 18, 1996 column, I cautioned that the stock market was in a bubble phase, and when compared with bonds, stocks were expensive.
The solids mass flux and hold-up profiles were determined together with the bubble phase properties (equivalent bubble diameter and bubble rise velocity) for different operating conditions and different membrane bundle configurations.
Two two-phase models are used to simulate DME synthesis in the lab fluidized-bed reactor with the bubble phase assumed to be in plug flow, and the dense phase in plug flow (P P model) and in fully back-mixed flow (P M model).
Firstly, the motion of the fuel particle with regards to the bubble phase and dense phase is proved to be realistic.
The solids, which are in the emulsion phases, are considered to be completely back-mixed; the gaseous bubble phase travels in plug-flow but exchanges with the emulsion phase.
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CEO of Professional Science Editing for Scientists @ prosciediting.com