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渣油污泥与生物质和废流化催化裂化催化剂共热解以回收资源。

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

机构信息

Chemical Reaction Engineering Laboratory, Department of Biotechnology and Chemical Engineering, Manipal University Jaipur, Jaipur, 303007, Rajasthan, India.

Bharat Petroleum Corporation Limited (BPCL), Corporate Research & Development Centre, Greater Noida, Uttar Pradesh, 201306, India.

出版信息

Environ Sci Pollut Res Int. 2024 Aug;31(39):52086-52104. doi: 10.1007/s11356-024-34630-x. Epub 2024 Aug 13.

DOI:10.1007/s11356-024-34630-x
PMID:39136925
Abstract

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%).

摘要

对两种不同炼油厂油泥(ROS)样品进行了催化共热解,以促进资源回收。在 500 至 600°C 的温度范围内进行非催化热解,以确定高油收率。较高的温度将油收率提高到了24wt%,而 S1 的炭产率保持不变(45%)。相比之下,S2 的油收率明显较低(4wt%)。S1 的热解油中含有酚类物质(在 600°C 时约为 50%),而 S2 油中则以烃类物质为主(在 600°C 时约为 80%)。S1 的催化热解对油收率没有显著影响,但油的组成有明显变化。分子筛(MS)、金属渣和 ZSM-5 分别得到了高含量的烃类、酚类和芳烃。在 MS 存在下,S2 与木屑(SD)的催化共热解提高了油收率,得到的油中含有高含量的烃类(54%)和芳烃(~44%)。

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