化工进展 ›› 2022, Vol. 41 ›› Issue (3): 1470-1478.DOI: 10.16085/j.issn.1000-6613.2021-0815
收稿日期:
2021-04-18
修回日期:
2021-08-30
出版日期:
2022-03-23
发布日期:
2022-03-28
通讯作者:
侯远东
作者简介:
王月(1990—),女,博士,高级工程师,研究方向为石油炼制。E-mail:WANG Yue(), ZHAO Qinfeng, ZHANG Zhanquan, LEI Junwei, HOU Yuandong()
Received:
2021-04-18
Revised:
2021-08-30
Online:
2022-03-23
Published:
2022-03-28
Contact:
HOU Yuandong
摘要:
人类生产生活对塑料制品日益增长的需求使得塑料废弃物迅速增加,由此引起的环境问题和社会问题亟待解决。本文综述了碳中和背景下国内外废塑料裂解法回收进展,从废塑料裂解催化剂、废塑料裂解反应器、废塑料与其他固废共裂解三个方面对废塑料裂解技术进展进行总结,归纳了国内外塑料回收企业和石油石化企业在废塑料裂解回收方面的进展,分为裂解法制油和裂解法制化学品两个方面。阐明了废塑料回收在节约能源、碳减排和经济性方面的意义,指出国内废塑料裂解法回收存在法规缺失、废塑料分类不清晰、产业链条不完善、相关学术研究不深入等问题,提出国内石油石化企业应从全生命周期角度出发对废塑料进行裂解法回收处理,结合上下游产业链,分阶段实施废塑料裂解产油品路线和产化学品路线。
中图分类号:
王月, 赵秦峰, 张占全, 雷俊伟, 侯远东. 碳中和背景下国内外废塑料裂解法回收进展[J]. 化工进展, 2022, 41(3): 1470-1478.
WANG Yue, ZHAO Qinfeng, ZHANG Zhanquan, LEI Junwei, HOU Yuandong. Plastic waste recycling by pyrolysis at home and abroad under the background of carbon neutrality[J]. Chemical Industry and Engineering Progress, 2022, 41(3): 1470-1478.
年份 | 产量/×106t |
---|---|
1950 | 1.5 |
1980 | 60 |
1990 | 105 |
2000 | 187 |
2010 | 265 |
2017 | 348 |
2018 | 359 |
2019 | 400 |
表1 1950—2019年全球塑料产量
年份 | 产量/×106t |
---|---|
1950 | 1.5 |
1980 | 60 |
1990 | 105 |
2000 | 187 |
2010 | 265 |
2017 | 348 |
2018 | 359 |
2019 | 400 |
国家或地区 | 产量占比/% |
---|---|
北美 | 18 |
拉丁美洲 | 4 |
欧洲 | 17 |
中东、非洲 | 7 |
中亚 | 3 |
中国 | 30 |
日本 | 4 |
其他 | 17 |
表2 全球塑料产量分布
国家或地区 | 产量占比/% |
---|---|
北美 | 18 |
拉丁美洲 | 4 |
欧洲 | 17 |
中东、非洲 | 7 |
中亚 | 3 |
中国 | 30 |
日本 | 4 |
其他 | 17 |
原料 | 反应工艺 | 催化剂 | 反应温度/℃ | 反应器 | 产物分布 | 参考文献 |
---|---|---|---|---|---|---|
废塑料袋(PE) | 热裂解-催化改质 | 三氯化铁-钠基膨润土 | 500 | 高压裂解釜-填料式催化反应器 | 80%产油率 | [ |
PS、PP、LDPE、HDPE | 热裂解-催化改质 | 膨润土 | 500 | 反应釜-固定床 | 88%产油率 | [ |
LDPE | 催化裂解 | 水泥砂浆 | 410 | 管式固定床 | 86.7%液收 | [ |
LDPE、PS | 热裂解 | DeLaZSM-5 | 430 | 反应釜 | 82.2%液收 | [ |
PE | 催化氢解 | 钌/碳 | 200 | 反应釜 | 45%液态烷烃收率 | [ |
表3 废塑料裂解催化剂及裂解性能
原料 | 反应工艺 | 催化剂 | 反应温度/℃ | 反应器 | 产物分布 | 参考文献 |
---|---|---|---|---|---|---|
废塑料袋(PE) | 热裂解-催化改质 | 三氯化铁-钠基膨润土 | 500 | 高压裂解釜-填料式催化反应器 | 80%产油率 | [ |
PS、PP、LDPE、HDPE | 热裂解-催化改质 | 膨润土 | 500 | 反应釜-固定床 | 88%产油率 | [ |
LDPE | 催化裂解 | 水泥砂浆 | 410 | 管式固定床 | 86.7%液收 | [ |
LDPE、PS | 热裂解 | DeLaZSM-5 | 430 | 反应釜 | 82.2%液收 | [ |
PE | 催化氢解 | 钌/碳 | 200 | 反应釜 | 45%液态烷烃收率 | [ |
原料 | 反应工艺 | 催化剂 | 反应温度/℃ | 反应器 | 产物分布 | 参考文献 |
---|---|---|---|---|---|---|
聚乙烯、聚丙烯与煤 | 热裂解 | — | 520 | 固定床 | 油产率18.588% | [ |
废聚乙烯与废植物油脂 | 催化裂解 | ZrO2/Al2O3/TiO2 | 430 | 高压反应釜 | 液收65.9% | [ |
聚丙烯与铜藻 | 热裂解 | — | 375 | 裂解釜 | 液收64.79% | [ |
HDPE、LDPE、PP与松木屑 | 热裂解 | — | 300~500 | 热重分析仪 | — | [ |
HDPE与玉米秸秆 | 催化裂解 | HZSM-5 | 550 | 管式炉 | 芳烃82.7% | [ |
废塑料与焦化蜡油 | 催化裂解 | FCC催化剂 | 460 | 常压反应釜 | 液收96.67% | [ |
废塑料与废机油 | 催化裂解 | ZSM-5/50H | 420 | 裂解炉 | 液收89% | [ |
表4 废塑料共裂解工艺及裂解性能
原料 | 反应工艺 | 催化剂 | 反应温度/℃ | 反应器 | 产物分布 | 参考文献 |
---|---|---|---|---|---|---|
聚乙烯、聚丙烯与煤 | 热裂解 | — | 520 | 固定床 | 油产率18.588% | [ |
废聚乙烯与废植物油脂 | 催化裂解 | ZrO2/Al2O3/TiO2 | 430 | 高压反应釜 | 液收65.9% | [ |
聚丙烯与铜藻 | 热裂解 | — | 375 | 裂解釜 | 液收64.79% | [ |
HDPE、LDPE、PP与松木屑 | 热裂解 | — | 300~500 | 热重分析仪 | — | [ |
HDPE与玉米秸秆 | 催化裂解 | HZSM-5 | 550 | 管式炉 | 芳烃82.7% | [ |
废塑料与焦化蜡油 | 催化裂解 | FCC催化剂 | 460 | 常压反应釜 | 液收96.67% | [ |
废塑料与废机油 | 催化裂解 | ZSM-5/50H | 420 | 裂解炉 | 液收89% | [ |
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