کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
---|---|---|---|---|
237519 | 465711 | 2011 | 13 صفحه PDF | دانلود رایگان |
![عکس صفحه اول مقاله: Influence of multiple gas inlet jets on fluidized bed hydrodynamics using Particle Image Velocimetry and Digital Image Analysis Influence of multiple gas inlet jets on fluidized bed hydrodynamics using Particle Image Velocimetry and Digital Image Analysis](/preview/png/237519.png)
A rectangular fluidized bed setup was developed to study the evolution of inlet gas jets located at the distributor. Experiments were conducted with varying distributor types and bed media to understand the motion of particles and jets in the grid-zone region of a fluidized bed. Particle Image Velocimetry and Digital Image Analysis were used to quantify the parameters that characterize these jets. A grid-zone phenomenological model was developed to compare these parameters with those available in the literature. It was determined from this study that jet penetration length behavior is consistently different for fluidization velocities below and above the minimum fluidization. For velocities above minimum fluidization, jet lengths were found to increase more rapidly with increase in orifice velocity than for operating conditions below minimum fluidization.
Particle Image Velocimetry and Digital Image Analysis were used to quantify the parameters that characterize jets and understand the motion of particles surrounding them in the grid-zone region of the fluidized bed. A grid-zone phenomenological model was developed to compare these parameters with those available in the literature.Figure optionsDownload as PowerPoint slideHighlights
► PIV and DIA used to quantify and develop grid-zone phenomenological model.
► Grid-zone divided into 3 regions: particle moving zone, dead zone and jetting zone.
► Isolated, transitional and interacting jet systems defined using grid-zone parameters.
► Correlations developed for grid-zone parameters and compared with literature.
► Jet length rose sharply for velocities above minimum fluidization requiring 2 correlations to describe the jet behavior.
Journal: Powder Technology - Volume 214, Issue 1, 25 November 2011, Pages 122–134