Catalytic Co-pyrolysis of Biomass and Plastics (Polypropylene and Polystyrene) Using Spent FCC Catalyst

乙苯 热解 聚苯乙烯 催化作用 产量(工程) 聚丙烯 苯乙烯 化学工程 化学 生物量(生态学) 二甲苯 分数(化学) 甲苯 甲醇 材料科学 有机化学 核化学 聚合物 复合材料 共聚物 海洋学 工程类 地质学
作者
Kanduri Praveen Kumar,Srinivas Seethamraju
出处
期刊:Energy & Fuels [American Chemical Society]
卷期号:34 (1): 460-473 被引量:102
标识
DOI:10.1021/acs.energyfuels.9b03135
摘要

In situ catalytic co-pyrolysis (CCP) of mixtures of lignocellulosic biomass (LB) and plastic (polypropylene (PP) and polystyrene (PS)) with spent FCC catalyst (10% w/w loading) was performed in a semibatch reactor. The experiments were carried out using 30 g of feed at 510 °C and three different feed ratios of LB to plastic (1:2, 1:1, and 2:1). The effect of feed ratio on bio-oil yield, composition, and carbon yield of products (mainly, aromatics and olefins) was evaluated. A maximum aromatic selectivity of ∼49%C with PP and ∼82%C with PS was observed at a feed ratio of 0.5. Co-processing LB with PP produced more valuable chemicals like toluene and xylene at equal mixing ratios. The total yield of monoaromatics and olefins was maximum (∼73%C) at an LB to PP ratio of 0.5. When LB was co-fed with PS, the more valuable styrene monomers and ethylbenzene were found significantly in the product at intermediate mixing ratios. While co-feeding PP with LB improved the (H/C)eff ratio of the pyrolysis liquid, the change in the (H/C)eff ratio was insignificant in the case of biomass and PS mixtures. The spent FCC catalyst helps in oxygen removal from the bio-oil and improves its quality (higher aromatic fraction) compared to oil obtained from thermal co-pyrolysis of the biomass and plastic mixtures.
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