Ultrafast cross‐sectional imaging of gas‐particle flow in a fluidized bed
Ultrafast cross‐sectional imaging of gas‐particle flow in a fluidized bed
复制标题
流化床中气体-颗粒流的超快横截面成像
DOI:
10.1002/aic.12121
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发表时间:
2009
期刊:
影响因子:
3.7
通讯作者:
U. Hampel
中科院分区:
文献类型:
--
作者:
M. Bieberle;F. Fischer;E. Schleicher;H.;H. Mayer;U. Hampel
Gas–solid fluidized beds are widely used in chemical and process engineering, for instance in fluid catalytic cracking, drying of particulate solids, polyolefin production, calcination, coal gasification, and more recently for carbon nanotube production and oxycombustion. The gas-particle flow in fluidized beds is generally complex and difficult to observe, but exact information on voidage distribution and solid transport is urgently needed for assessment, monitoring, and optimization of fluidized bed operation. Commonly, fluidization is characterized by flow regimes as in gas–liquid flow. Thus, bubbly, turbulent, and annular flow is known. The gas–solids distribution and its dynamics strongly influence the performance of the running process. As an example, the conversion of gaseous reactants depends on bubble sizes and solids content inside the bubbles. It is thus desirable to recover the inner structure and dynamics of fluidized beds at given flow mechanical and thermodynamic conditions, defined by mass flow rates, pressure, particle sizes, bed geometry, etc. For this purpose measurement techniques are needed, which provide dynamic void fraction information at high spatial and temporal resolution. Currently, there are many flow measurement techniques but only few are applicable to dense fluidized beds. 1 Optical imaging, laser-based methods and ultrasound techniques generally fail to disclose the voidage distribution inside a fluidized bed, since the particles are opaque to visible light and scatter ultrasound waves unpredictably. Such measurement techniques are at the most able to capture the peripheral structure of the solids phase. Instead, local optical and capacitance probes2–4 are widely used to measure local phase fractions at selected points in the fluidized bed with high temporal resolution. However, they give no crosssectional view on the voidage distribution and even disturb the flow itself to a considerable degree. More suitable seems electrical capacitance tomography (ECT), 5 which has already been successfully applied to fluidized beds. ECT reaches high temporal resolution of up to 1000 frames per second (fps), but is limited in spatial resolution to about 10% of the pipe diameter. It can therefore neither visualize single particles nor small void volumes. Positron emission tomography6 is yet another imaging technique which has the capability to image the distribution of tracer particles in the temporal range of about 1s and with spatial resolution of about 5mm. Radioactive particle tracking methods7 provide even better temporal information and can be used to measure velocities and trajectories of single particles. But the spatial distribution of particles is obtained as a time-average only. Magnetic resonance imaging8 (MRI) has been adapted for ultrafast measurements of the axial solids content in a fluidized bed and therein reaches a temporal resolution between 1 and 2ms. Conventional X-ray and gamma ray computed tomography can reach a spatial resolution in the millimeter range, but are slow and can therefore only measure timeaveraged density distributions. 9 In recent years, some proposals have been made to increase the time resolution of