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作 者:顾菁[1,2,3,4,5] 程磊磊 王亚琢 张原翔[2] 袁浩然 GU Jing;CHENG Lei-lei;WANG Ya-zhuo;ZHANG Yuan-xiang;YUAN Hao-ran(Guangzhou Institute of Energy Conversion,Chinese Academy of Sciences(CAS),Guangzhou 510640,China;Southern Marine Science and Engineering Guangdong Laboratory(Guangzhou),Guangzhou 511458,China;CAS Key Laboratory of Renewable Energy,Guangzhou 510640,China;Guangdong Provincial Key Laboratory of New and Renewable Energy Research and Development,Guangzhou 510640,China;Foshan Kehengbo Environmental Protection Technology Co.LTD,Foshan 528200,China)
机构地区:[1]中国科学院广州能源研究所,广东广州510640 [2]南方海洋科学与工程广东省实验室(广州),广东广州511458 [3]中国科学院可再生能源重点研究室,广东广州510640 [4]广东省新能源和可再生能源研究开发与应用重点研究室,广东广州510640 [5]佛山市科恒博环保技术有限公司,广东佛山528200
出 处:《燃料化学学报》2021年第3期395-406,共12页Journal of Fuel Chemistry and Technology
基 金:国家重点研发计划项目(2018YFC1901200);国家自然科学基金(51976223);南方海洋科学与工程广东省实验室(广州)人才团队引进重大专项(GML2019ZD0101)资助。
摘 要:塑料废弃物数量日益增加,实现低能耗、高值化利用是促进塑料废弃物回收利用的关键。在380℃设定温度和(1−5)×10^(5)Pa初始压力条件下分别开展聚乙烯高压热裂解和催化热解实验,记录反应过程温度曲线,分析聚乙烯高压热裂解/催化热解产物分布。研究结果表明,反应过程中反应物相态是影响热解反应历程的重要因素;因反应路径而异,压力变化对聚乙烯热裂解和催化热解产生不同程度的影响。聚乙烯高压热裂解实验过程中存在飞温现象,飞温峰值随初始压力的增加呈现单调增加的趋势;峰值温度的升高带来聚乙烯断链程度的加深,即获得更多小分子量产物。在相同设定温度和初始压力条件下的聚乙烯高压催化热解实验中不存在飞温现象,利用锌负载的ZSM-5催化剂实现聚乙烯高选择性制备芳香烃,液体产物中单环芳烃占比达82.53%,积炭产率在1.5%以下。With the increasing waste disposal problems,high-value utilization technology using less energy is important to incentivize better recycling of plastic waste.Polyethylene high-pressure thermal cracking and catalytic pyrolysis experiments were conducted at a set temperature of 380℃and low initial pressures(1−5)×10^(5)Pa.The process temperature curves were recorded and the hydrocarbon distribution of products was analyzed.The results suggest that the phase state in the pyrolysis system is a critical issue for reaction pathways.Thus,the pressure changes have different effects on the thermal cracking and catalytic pyrolysis of polyethylene.There is a phenomenon of thermal runaway during the polyethylene high-pressure pyrolysis process.The peak temperature represents a monotonous increase with the increasing initial pressure;the higher peak temperature leads to deeper cracking of polyethylene,giving more low-molecular-weight products.In the high-pressure catalytic pyrolysis experiments under the same other conditions,no thermal runaway is observed.The Zn-supported ZSM-5 catalyst converts polyethylene into aromatics,and the selectivity for monocyclic aromatics in the liquid phase is up to 82.53%.Moreover,the coke yield is less than 1.5%.
分 类 号:X705[环境科学与工程—环境工程]
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