Co-pyrolysis of refinery oil sludge with biomass and spent fluid catalytic cracking catalyst for resource recovery

被引:1
作者
Sharma, Himanshi [1 ]
Singh, Ranjita [1 ]
Chakinala, Nandana [1 ]
Majumder, Supriyo [2 ]
Thota, Chiranjeevi [2 ]
Chakinala, Anand Gupta [1 ]
机构
[1] Chemical Reaction Engineering Laboratory, Department of Biotechnology and Chemical Engineering, Manipal University Jaipur, Rajasthan, Jaipur
[2] Development Centre, Uttar Pradesh, Greater Noida
关键词
Aromatics; Bio-oil; Hydrocarbons; Phenolics; Sawdust; Zeolites;
D O I
10.1007/s11356-024-34630-x
中图分类号
学科分类号
摘要
Catalytic co-pyrolysis of two different refinery oily sludge (ROS) samples was conducted to facilitate resource recovery. Non-catalytic pyrolysis in temperatures ranging from 500 to 600°C was performed to determine high oil yields. Higher temperatures enhanced the oil yields up to ~ 24 wt%, while char formation remained unchanged (~ 45%) for S1. Conversely, S2 exhibited a notably lower oil yield (~ 4 wt%) than S1. Pyrolysis oil of S1 consisted of phenolics (~ 50% at 600 °C) whereas hydrocarbons were predominant in S2 oil (~ 80% at 600 °C). Catalytic pyrolysis of S1 did not exhibit a substantial impact on oil yields but the oil composition varied significantly. High hydrocarbons, phenolics, and aromatics were obtained with molecular sieve (MS), metal slag, and ZSM-5, respectively. Catalytic co-pyrolysis of S2 with sawdust (SD) in the presence of MS enhanced the oil yield, and the resulting oil consisted of high hydrocarbons (~ 54%) and aromatics (~ 44%). © The Author(s), under exclusive licence to Springer-Verlag GmbH Germany, part of Springer Nature 2024.
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页码:52086 / 52104
页数:18
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