Abstract
Catalysts readily suffer from particle attrition in fluidized beds. In this article, a commercial fluid catalytic cracking catalyst was sieved into several particle-size intervals to investigate the size effect on particle attrition. It is shown that an exponential decay equation presents a suitable description of attrition and that catalyst attrition is dependent on particle size. Steady-state specific attrition rate decreases with increasing particle size; however, initial specific attrition rate and decay time parameter change irregularly. For comparison of attrition resistances, a long attrition test is required to reach steady-state attrition, and the steady-state specific attrition rate is recommended. It is seen that the smallest particle-size interval is the most seriously attrited, while the two largest particle-size intervals are the most attrition-resistant. Furthermore, weak interactions appear among attrition behaviors of different intervals, and a linear combination method is effective to combine all interval samples to predict the attrition of the original full-sized sample. (c) 2016 American Institute of Chemical Engineers AIChE J, 63: 914-920, 2017
| Original language | English |
|---|---|
| Pages (from-to) | 914-920 |
| Number of pages | 7 |
| Journal | AIChE Journal |
| Volume | 63 |
| Issue number | 3 |
| DOIs | |
| Publication status | Published - Mar 2017 |
| MoE publication type | A1 Journal article-refereed |
Funding
This work was supported by the National Natural Science Foundation of China (Grant Nos. 21376050 and 21176048) and the Fundamental Research Funds for the Central Universities.
Keywords
- particle size
- particle attrition
- attrition rate
- fluid catalytic cracking
- fluidized bed
- JET ATTRITION
- REACTOR
- NOZZLES
- SORBENT
- SYSTEMS
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