Depolymerization of Household Plastic Waste via Catalytic Hydrothermal Liquefaction

高密度聚乙烯 聚乙烯 低密度聚乙烯 解聚 聚丙烯 材料科学 水热液化 产量(工程) 催化作用 石脑油 聚苯乙烯 液化 机油 化学工程 废物管理 聚合物 化学 有机化学 高分子化学 复合材料 物理 热力学 工程类
作者
Tawsif Rahman,Hossein Jahromi,Poulami Roy,Ashish Bhattarai,Mohamed Ammar,Jonas Baltrušaitis,Sushil Adhikari
出处
期刊:Energy & Fuels [American Chemical Society]
卷期号:37 (17): 13202-13217 被引量:20
标识
DOI:10.1021/acs.energyfuels.3c01706
摘要

An unprecedented use of plastics has caused many environmental issues, and as usual, there is a growing interest in recycling and reusing single-use household plastics. In this work, a mixture of five prominent plastic polymers, as simulated household waste, was depolymerized via the hydrothermal liquefaction (HTL) process using a pretreated red mud catalyst (RM) for the liquid product at 430 ± 20 °C reaction temperature for an average 2 h residence time. The selected plastics were polyethylene terephthalate (PET), high-density polyethylene (HDPE), low-density polyethylene (LDPE), polypropylene (PP), and polystyrene (PS), which were blended at a ratio of 42, 20, 20, 4, and 14 wt %, respectively, to form a plastic mixture (PM) as a simulated household plastic waste. Additionally, each plastic type was treated individually for control experiments. Among the single plastics, HDPE generated a maximum crude oil yield of 76 wt %, whereas PET produced mainly solid (80 wt %) and gaseous products. The crude oil yield production from noncatalytic reactions followed this trend: HDPE > PS > PP > LDPE. The plastic crude oil possessed 36–92 wt % gasoline-range compounds. Without a catalyst, HDPE decomposed into straight-chain alkanes, whereas PP- and PS-derived products consisted of cyclic compounds. The noncatalytic PM HTL reaction produced 23 wt % liquid crude product and 23 wt % solid from PET. Though the use of a catalyst decreased the single plastic crude yield by 5–60%, it reduced viscosity by 20–80%, minimized acidity by 14–57%, and increased low boiling products (gasoline range) of HTL oil by 5–80%. The use of the RM catalyst increased the crude yield of PM by 63%, decreased solid output from PET by 10%, improved energy recovery by 4.7%, promoted aromatization in PM-derived crudes by 11.4%, and increased the gasoline boiling range compounds by 18.3%. Additionally, the RM catalyst was recycled without significant change in the PM crude yield. This liquefaction study can help in mitigating plastic recycling issues with liquid fuel production.
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