| نویسندگان | سیدابوالفضل رضوی علوی,ابراهیم نعمتی لای,سید کمال افضلی,امیر حسین علیزاده مخملی |
| همایش | The 9th International Chemical Engineering Congress & Exhibition (IChEC 2015) |
| تاریخ برگزاری همایش | 2016-12-26 |
| محل برگزاری همایش | شیراز |
| نوع ارائه | سخنرانی |
| سطح همایش | بین المللی |
چکیده مقاله
In this research, firstly, identify the cyclone as a device that accomplishes a solid-gas separation by
imparting a spinning motion to the two-phase system. In this equipment the solid particulates
move outward to the wall of the cyclone because of the centrifugal force and subsequently travel
downward to enter a discharge hopper. The gas that is freed from solids leaves at the top through a
central outlet. Furthermore, geometric structure, gas-solid flow characteristics and produced forces
in the cyclone are described. In the next step, the collection efficiency of the cyclone is defined
and moreover, geometry of cyclone, inlet flow rate of gas, particle size distribution, temperature
and pressure drop are introduced as parameters related to the efficiency, and then with regard to
the practical tests were taken on industrial cyclone used in fluidized bed drying unit of high
density polyethylene (HDPE) particles, the process of change in the operational parameters is
carefully monitored and show their relationship with the separation efficiency of double-cyclone.
Finally, we will see that the performance of industrial cyclone can cause the proper functioning of
the fluidized bed drying and also optimizing the effective operational parameters of the cyclone
can be used to facilitate working conditions in the fluidized bed dryer and produce HDPE powdery
particles with good quality.