Experimental Study of the Conversion of Polyethylene and Polypropylene to Non-Condensable Gases Using a Lab-Scale Bubble Column Reactor with Molten Metal Catalysis
Eunji Lee, Won Yang, Uendo Lee, Yongwoon Lee, Youngjae Lee
{"title":"Experimental Study of the Conversion of Polyethylene and Polypropylene to Non-Condensable Gases Using a Lab-Scale Bubble Column Reactor with Molten Metal Catalysis","authors":"Eunji Lee, Won Yang, Uendo Lee, Yongwoon Lee, Youngjae Lee","doi":"10.1007/s11814-024-00281-4","DOIUrl":null,"url":null,"abstract":"<div><p>Sustainable solutions for recycling waste plastics are necessary to replace conventional processing techniques. Plastic pyrolysis is a promising technology for converting waste plastic into useful chemicals. This study aimed to produce hydrogen (H<sub>2</sub>) via plastic pyrolysis using a molten metal catalyst. The characteristics of plastic conversion to non-condensable gas under various operating conditions, such as the number of reactors, reaction temperature, and type of molten metal catalyst used, were investigated. Nitrogen (N<sub>2</sub>) was introduced into a molten metal bubble column reactor containing a metal catalyst, and plastic was then uniformly mixed inside the catalyst through the formed rotating flow. Polyethylene and polypropylene were pyrolyzed at 700–900 ℃. In the single reactor, the fraction of H<sub>2</sub> was similar to that reported in previous studies; however, the fraction of light hydrocarbons increased. As the number of reactors increased in the multi-stage reactor, the fraction of CH<sub>4</sub> increased to 58%. At elevated reactor temperatures, the fraction of H<sub>2</sub> increased to 40% as the decomposition of light hydrocarbons increased. The dominant influence on H<sub>2</sub> production was C<sub>2</sub>H<sub>4</sub> decomposition. The present study derived the optimal operating conditions for increasing H<sub>2</sub> production during plastic pyrolysis with molten metal catalysts.</p></div>","PeriodicalId":684,"journal":{"name":"Korean Journal of Chemical Engineering","volume":"42 4","pages":"745 - 756"},"PeriodicalIF":2.9000,"publicationDate":"2024-09-27","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Korean Journal of Chemical Engineering","FirstCategoryId":"5","ListUrlMain":"https://link.springer.com/article/10.1007/s11814-024-00281-4","RegionNum":4,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q2","JCRName":"CHEMISTRY, MULTIDISCIPLINARY","Score":null,"Total":0}
引用次数: 0
Abstract
Sustainable solutions for recycling waste plastics are necessary to replace conventional processing techniques. Plastic pyrolysis is a promising technology for converting waste plastic into useful chemicals. This study aimed to produce hydrogen (H2) via plastic pyrolysis using a molten metal catalyst. The characteristics of plastic conversion to non-condensable gas under various operating conditions, such as the number of reactors, reaction temperature, and type of molten metal catalyst used, were investigated. Nitrogen (N2) was introduced into a molten metal bubble column reactor containing a metal catalyst, and plastic was then uniformly mixed inside the catalyst through the formed rotating flow. Polyethylene and polypropylene were pyrolyzed at 700–900 ℃. In the single reactor, the fraction of H2 was similar to that reported in previous studies; however, the fraction of light hydrocarbons increased. As the number of reactors increased in the multi-stage reactor, the fraction of CH4 increased to 58%. At elevated reactor temperatures, the fraction of H2 increased to 40% as the decomposition of light hydrocarbons increased. The dominant influence on H2 production was C2H4 decomposition. The present study derived the optimal operating conditions for increasing H2 production during plastic pyrolysis with molten metal catalysts.
期刊介绍:
The Korean Journal of Chemical Engineering provides a global forum for the dissemination of research in chemical engineering. The Journal publishes significant research results obtained in the Asia-Pacific region, and simultaneously introduces recent technical progress made in other areas of the world to this region. Submitted research papers must be of potential industrial significance and specifically concerned with chemical engineering. The editors will give preference to papers having a clearly stated practical scope and applicability in the areas of chemical engineering, and to those where new theoretical concepts are supported by new experimental details. The Journal also regularly publishes featured reviews on emerging and industrially important subjects of chemical engineering as well as selected papers presented at international conferences on the subjects.