Enabling plastic waste gasification by autothermal chemical looping with > 90 % syngas purity for versatile feedstock handling

IF 5 Q2 ENERGY & FUELS
Eric Falascino , Rushikesh K. Joshi , Sonu Kumar, Tanay Jawdekar, Ishani K. Kudva, Shekhar G. Shinde, Zhuo Cheng, Andrew Tong, Liang-Shih Fan
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Abstract

The chemical looping gasification of plastics (CLGP) is a process that offers an innovative solution for transforming post-consumer waste plastics into high-value products. The process utilizes a co-current moving bed reducer reactor with iron-titanium-based oxygen carriers to gasify plastic feed and generate syngas autothermally. Its distinguishing feature is its ability to operate over a wide range of feed loadings and co-injection of mixed plastic species without any performance losses. Isothermal bench-scale experiments reveal a syngas purity of ∼95 %, aligning with the thermodynamic simulations. The moving bed reactor facilitates a deeper reduction of the oxygen carriers to the Fe+FeTiO3 phase, leading to the high syngas purity, which is then verified with additional TGA, XRD, and SEM analysis. For an autothermal operation of CLGP process, an active material content of 20 % is found to be sufficient to satisfy the kinetic and thermodynamic constraints. Further integration with downstream production of H2 is presented and compared to a steam gasification process. The process integration simulations show that the CLGP process outperforms the steam gasification system in terms of Cold Gas Efficiency (CGE), Effective Thermal Efficiency (ETE), and H2 yield. CO2 emissions are impressively reduced by ∼30 % in the CLGP system over that in the steam gasification system due to its ability to autothermally operate the process, unlike the highly endothermic steam gasification process.

Abstract Image

通过自热化学循环实现塑料废料气化,合成气纯度大于 90%,可处理多种原料
塑料化学循环气化(CLGP)工艺是一种将消费后废塑料转化为高价值产品的创新解决方案。该工艺利用带有铁钛氧气载体的同流移动床减速器反应器,气化塑料进料并自热生成合成气。该工艺的显著特点是能够在很宽的进料负荷范围内运行,并能在不损失任何性能的情况下同时注入混合塑料。等温台架实验表明,合成气纯度为 95%,与热力学模拟结果一致。移动床反应器有助于氧载体更深入地还原为 Fe+FeTiO3 相,从而获得高纯度合成气,并通过额外的 TGA、XRD 和 SEM 分析加以验证。在 CLGP 工艺的自热操作中,发现 20% 的活性材料含量足以满足动力学和热力学限制。此外,还介绍了与下游 H2 生产的进一步整合,并与蒸汽气化工艺进行了比较。工艺集成模拟显示,CLGP 工艺在冷气效率 (CGE)、有效热效率 (ETE) 和 H2 产量方面均优于蒸汽气化系统。与高内热的蒸汽气化工艺不同,CLGP 工艺能够自热运行,因此二氧化碳排放量比蒸汽气化工艺显著减少了 30%。
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