PETROLEUM PROCESSING AND PETROCHEMICALS ›› 2026, Vol. 57 ›› Issue (4): 15-19.
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Abstract: Addressing technical challenges in the reactor-regenerator section of a 1.2 Mt/a catalytic cracking unit, such as afterburning in the regenerator dilute phase and severe catalyst loss, a systematic revamp focused on flow field optimization was implemented during the 2021 overhaul. Key technical measures included optimizing the main air distribution system, improving the catalyst distributor, applying PLS-type dual-inlet cyclones, and adding dense phase grids. These measures fundamentally improved gas-solid distribution uniformity and carbon-air matching efficiency. Post-revamp, afterburning in the dilute phase was eliminated, catalyst loss reduced from 3―7 t/d to 1.5 t/d, achieving long-term, stable, and safe operation.
Key words: catalytic cracking, dilute phase afterburning, cyclone separator, main air distribution, catalyst loss, flow field optimization
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http://www.sylzyhg.com/EN/Y2026/V57/I4/15