Chemical and Environmental Department, Faculty of Engineering of Bilbao, University of the Basque Country (UPV/EHU), Plaza Ingeniero Torres Quevedo 1, 48013 Bilbao, Spain.
Chemical and Environmental Department, Faculty of Engineering of Bilbao, University of the Basque Country (UPV/EHU), Plaza Ingeniero Torres Quevedo 1, 48013 Bilbao, Spain.
Waste Manag. 2021 Jun 1;128:73-82. doi: 10.1016/j.wasman.2021.04.044. Epub 2021 May 7.
In this work, a novel method to valorize the polymeric matrix of residual carbon fiber reinforced polymers (CFRP) in the recycling process of carbon fibers by pyrolysis is presented. The experiments have been carried out with an expired epoxy-based pre-preg and in a lab-scale installation composed of two reactors. In the first one, pyrolysis and oxidation have been carried out, while in the second one, the gases and vapors resulting from the thermal decomposition of the polymeric resin have been thermally treated. The following operating parameters have been studied in the pyrolysis step: dwell time, the use of N (N flow, no N flow and not even to inert the reaction medium) and the solid bed material of the second reactor. In the oxidation step, temperature and time have been optimized by using the theory of experiments based on 2 factorial design was used. It has been demonstrated that clean carbon fibers and a gaseous fraction with 75% by volume of H can be obtained. This is possible through a combined process of (1) CFRP thermal decomposition at 500 °C, (2) thermal treatment of gases and vapors at 900 °C in a solid bed tubular reactor filled with a waste refractory material and (3) oxidation of pyrolysis solid at 500 °C during 165 min in presence of 1.3 L air min.
在这项工作中,提出了一种通过热解将废弃碳纤维增强聚合物(CFRP)的聚合物基质在碳纤维回收过程中增值的新方法。实验使用过期的环氧树脂预浸料,并在由两个反应器组成的实验室规模装置中进行。在第一个反应器中进行热解和氧化,而在第二个反应器中,对聚合物树脂热分解产生的气体和蒸气进行热处理。在热解步骤中研究了以下操作参数:停留时间、使用 N(N 流量、无 N 流量甚至不使反应介质惰性)和第二反应器的固体床材料。在氧化步骤中,通过使用基于 2 因素设计的实验理论优化了温度和时间。结果表明,可以获得清洁的碳纤维和体积分数为 75%的 H 的气态馏分。这是通过(1)在 500°C 下进行 CFRP 热解、(2)在填充废耐火材料的固体床管式反应器中在 900°C 下对气体和蒸气进行热处理以及(3)在存在 1.3 L 空气 min 的情况下在 500°C 下对热解固体进行 165 min 氧化的组合工艺实现的。