Solid particle mixing in a continously operated fluidized bed reactor
✍ Scribed by K. Wittmann; D. Wippern; H. Schlingmann; H. Helmrich; K. Schügerl
- Publisher
- Elsevier Science
- Year
- 1983
- Tongue
- English
- Weight
- 434 KB
- Volume
- 38
- Category
- Article
- ISSN
- 0009-2509
No coin nor oath required. For personal study only.
✦ Synopsis
In a bench-scale fluidized bed reactor, 20cm in dia., residence time distribution of solid particles (d, = 137 pm) were measured by the radionuclide technique (24NazCO%) in the absence and in the presence of the chemical reaction 2NaHC03+ NazC03 + CO2 + HZO. The residence time distributions were evaluated by a backflow cascade model by nonlinear optimization. The radial and logitudinal concentration profiles of NaHC03 in the emulsion phase of the reactor were measured during steady-state operation. The solid is well-mixed.
The connection of the measured bubble properties with the longitudinal solid dispersion coefficient and the use of the Haines-King-Woodburn model allows to calculate the solid dispersion coefficient in the bubble-free emulsion phase.
📜 SIMILAR VOLUMES
This paper describes the overall operation of a 15 cm dia. fluidizedbed reactor for silicon production via silane pyrolysis. The fluidized-bed reactor has been characterized by its performance data and parametric effects. A withdrawal system is used to selectively remove big particles. Seed generati
The effect of particle size on the reactant conversion for a pseudo-first-order reaction in a gas-liquid-solid fluidized bed catalytic reactor is rigorously examined based on a comprehensive model developed in this study. The model takes into consideration inherent transport properties of the reacto
The solids mixing in a riser with a height of 10 m and 0.186 m inner diameter was investigated by using pneumatic phosphor tracer technique. Considering the shielding effect of the bed material on the light emitted from the phosphor tracer particle, a modified method for the phosphor tracer measurem
The distribution of residence times of solid particles is examined in fluidized beds at steady state with continuous feed and discharge of solids, both for beds consisting of a single particle size and for beds consisting of a wide spectrum of particle sizes. The mean age (residence time in bed) of