کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
---|---|---|---|---|
154726 | 456852 | 2015 | 10 صفحه PDF | دانلود رایگان |
• Catalyst attrition arises from mixed particle fragmentation and surface abrasion.
• A relative attrition rate is suggested to represent the attrition process.
• The relative attrition rate tends to a constant after nonsteady-state attrition.
• An exponential decay model is proposed to describe the time-dependent attrition.
Attrition of fluid catalytic cracking catalysts is investigated in a laboratory-scale fluidized bed. It is shown that the catalyst attrition arises from a mixed mechanism of particle fragmentation and surface abrasion. The measured conventional attrition rate always decreases with time, even for a long-time attrition; therefore, a relative attrition rate is suggested. Experiments indicate that after a nonsteady-state attrition where the measured relative attrition rate decreases with time, the attrition gets into a steady state and the measured relative attrition rate tends to a constant value. Furthermore, the time-dependence of particle attrition is discussed. It is seen that the widely-used Gwyn equation cannot model the catalyst attrition accurately. Alternatively, an exponential decay attrition model is proposed and confirmed to describe the time-dependent attrition behavior. It is found that the model parameters have definite meanings and are strongly related to the particle properties, fluidization conditions and fluidized bed structure.
Journal: Chemical Engineering Science - Volume 135, 2 October 2015, Pages 431–440