通过皂化作用探索和了解生物基环氧热固性塑料的回收利用

Fakhri-Eddin N. Lahfaidh, Nathanaël Guigo, Luc Vincent and Nicolas Sbirrazzuoli*, 
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引用次数: 0

摘要

通过开发一种创新的原位监测方法,研究了一种全生物基热固性材料的化学回收。在这项研究中,针对环氧/酸交联聚合物 SuccELO 的脆弱酯键,成功开发出了利用 KOH/EtOH 或 NaOH/ 水进行溶解的两种不同回收途径。热量计、傅立叶变换红外光谱、质量损失测量和光学显微镜对溶解过程进行了监测。通过量热法评估的动力学参数可以从溶解机制的角度进行解释,并用于区分回收过程的四个阶段,首先是扩散控制阶段。第二阶段结合了扩散和溶解两个过程,后一个过程与羧酸根离子的形成相对应。第三个阶段是钠盐形成的自催化阶段,它是甘油三酯的增溶剂。最后,小链的扩散被确定为过程末端的限速步骤。利用显微镜和傅立叶变换红外技术进行的综合表面分析进一步证实了这些发现。除了通过量热法监测溶解过程这一新颖方法外,还在此基础上开发了一种模拟工具。这些模拟结果与质量损失测量结果进行了比较,突出了这些质量损失测试所用程序的缺点。最后,研究还展示了如何利用动力学建模来预测实验无法获得的各种温度下的溶解情况,从而促进工艺设计和优化策略的制定。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

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Exploring and Understanding the Recycling of a Bio-Based Epoxy Thermoset via Saponification

The chemical recycling of a fully bio-based thermoset has been investigated by developing an innovative in situ monitoring methodology. Within this study, two distinct recycling pathways utilizing KOH/EtOH or NaOH/water were successfully developed for the solvolysis process of SuccELO, an epoxy/acid cross-linked polymer, by targeting its fragile ester bonds. The solvolysis was monitored by calorimetry, FT-IR, mass loss measurements, and optical microscopy. The kinetic parameters evaluated by calorimetry have been interpreted in terms of solvolysis mechanisms and used to discriminate four stages of the recycling process, beginning with a diffusion-controlled stage. The second step combines both diffusion and solvolysis, the later process corresponding to the formation of carboxylate ions. A third stage was identified and is associated with an autocatalytic step driven by the formation of sodium salts acting as a solubilizer for triglycerides. Finally, the diffusion of small chains is identified as the rate-limiting step at the end of the process. Validation of these findings is reinforced by comprehensive surface analysis using microscopy and FT-IR techniques. Besides the novelty of monitoring solvolysis by calorimetry, a simulation tool was developed based upon this method. These simulations were compared with mass loss measurements, highlighting drawbacks in the procedure used for these mass loss tests. Lastly, it is shown how prediction of the solvolysis at various temperatures not experimentally accessible can be achieved using kinetic modeling, facilitating process design and optimization strategies.

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