通过快速(催化)热解将危险有机固体废物转化为燃料和化学品

Kyriazis Rekos, I. Charisteidis, E. Tzamos, G. Palantzas, A. Zouboulis, K. Triantafyllidis
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引用次数: 1

摘要

城市和工业有机固体废物的管理已成为现代社会最关键的环境问题之一。目前,常用的管理技术有焚烧、堆肥和填埋,其中对危险有机废物最常用的是焚烧、堆肥和填埋。快速热解是一种可替代的环保方法,为危险废物管理提供了可持续且经济可行的解决方案,是石化和生物质增值行业中最重要的热化学过程之一。这项工作的目的是研究快速热解在三种废物中的应用,即石油基污泥和沉积物,废金属包装上残留的油漆,以及经杂酚油处理的木材废物,转化为高附加值的燃料,化学品和(生物)炭。在实验室规模的固定床反应器上进行快速热解实验,以确定产品收率,即热解(生物)油,气体和固体(炭)。此外,还通过Py/GC-MS测试确定了(生物)油的组成。与处理过的木材和残留油漆(也含有30 wt.%的无机物)分别提供46.9 wt.%和35 wt.%的热解油相比,由于这类废物的灰分含量非常高(74 wt.%),从石油污泥中提取的热裂解油仅为15.8 wt.%。气态产物从~7.9 wt.%(污泥)到14.7 wt.%(木材)和19.2 wt.%(油漆)不等,而相应的固体(灰分、焦炭、反应焦)值分别为75.1、35和36.9 wt.%。残余油漆的热(非催化)热解含有相对高浓度的短丙烯酸脂肪酯(即甲基丙烯酸正丁酯),是聚合物工业中有价值的单体。使用酸性沸石催化剂(ZSM-5)对热解蒸汽进行原位升级,引起了产物收率的变化(裂解反应导致油的减少,气体和焦/焦的增加),但主要是热解油的组成。ZSM-5沸石催化剂的主要作用是,对于所有三种有机废物,催化热解油都富集了增值单芳烃(BTX),特别是在处理过的木材废物和残留油漆的情况下。不凝性气体主要由CO, CO2和不同数量的C1-C4碳氢化合物组成,这取决于初始进料和催化剂的使用是否增加了乙烯和丙烯的产量。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Valorization of Hazardous Organic Solid Wastes towards Fuels and Chemicals via Fast (Catalytic) Pyrolysis
The management of municipal and industrial organic solid wastes has become one of the most critical environmental problems in modern societies. Nowadays, commonly used management techniques are incineration, composting, and landfilling, with the former one being the most common for hazardous organic wastes. An alternative eco-friendly method that offers a sustainable and economically viable solution for hazardous wastes management is fast pyrolysis, being one of the most important thermochemical processes in the petrochemical and biomass valorization industry. The objective of this work was to study the application of fast pyrolysis for the valorization of three types of wastes, i.e., petroleum-based sludges and sediments, residual paints left on used/scrap metal packaging, and creosote-treated wood waste, towards high-added-value fuels, chemicals, and (bio)char. Fast pyrolysis experiments were performed on a lab-scale fixed-bed reactor for the determination of product yields, i.e., pyrolysis (bio)oil, gases, and solids (char). In addition, the composition of (bio)oil was also determined by Py/GC-MS tests. The thermal pyrolysis oil from the petroleum sludge was only 15.8 wt.% due to the remarkably high content of ash (74 wt.%) of this type of waste, in contrast to the treated wood and the residual paints (also containing 30 wt.% inorganics), which provided 46.9 wt.% and 35 wt.% pyrolysis oil, respectively. The gaseous products ranged from ~7.9 wt.% (sludge) to 14.7 (wood) and 19.2 wt.% (paints), while the respective solids (ash, char, reaction coke) values were 75.1, 35, and 36.9 wt.%. The thermal (non-catalytic) pyrolysis of residual paint contained relatively high concentrations of short acrylic aliphatic ester (i.e., n-butyl methacrylate), being valuable monomers in the polymer industry. The use of an acidic zeolitic catalyst (ZSM-5) for the in situ upgrading of the pyrolysis vapors induced changes on the product yields (decreased oil due to cracking reactions and increased gases and char/coke), but mostly on the pyrolysis oil composition. The main effect of the ZSM-5 zeolite catalyst was that, for all three organic wastes, the catalytic pyrolysis oils were enriched in the value-added mono-aromatics (BTX), especially in the case of the treated wood waste and residual paints. The non-condensable gases were mostly consisting of CO, CO2, and different amounts of C1–C4 hydrocarbons, depending on initial feed and use or not of the catalyst that increased the production of ethylene and propylene.
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