Shihao Guo , Mengyao Gu , Yun Luo , Juan Chen , Hong Yao
{"title":"Enhanced gasification of waste plastics for hydrogen production: experiment and simulation","authors":"Shihao Guo , Mengyao Gu , Yun Luo , Juan Chen , Hong Yao","doi":"10.1016/j.joei.2025.102114","DOIUrl":null,"url":null,"abstract":"<div><div>The quality of hydrogen produced from waste plastic steam gasification is compromised by CO<sub>2</sub> and tar. While the use of CaO for CO<sub>2</sub> adsorption and tar catalytic cracking has been explored, the impact of the heat released during CaO carbonation on hydrogen production has not been sufficiently studied. This work investigates the role of Fe-doped CaO in enhancing hydrogen production and tar removal during gasification. Aspen Plus is used to evaluate the impact of CaO carbonation heat on hydrogen generation via waste plastic steam gasification. Experimental results show that, at 700 °C and 20 vol% H<sub>2</sub>O, the H<sub>2</sub> concentration and yield increase to 67.9 vol% and 288.6 mL/g, respectively, with a liquid production rate of 17 % when Ca<sub>90</sub>Fe<sub>10</sub>/PE mass ratio is 2.0. In simulations, with the gasifier operating at 700 °C and maintaining thermal equilibrium, H<sub>2</sub> molar percentage is 58.5 % for an O<sub>2</sub> inflow of 13.03 kg/h. At 700 °C and Ca<sub>90</sub>Fe<sub>10</sub>/PE mass ratio of 2.2, the heat generated by the CO<sub>2</sub> adsorption reaction of CaO is 76.51 MJ/h and requires 6.9 kg/h of O<sub>2</sub> and the molar percent of H<sub>2</sub> is 80.76 %. To achieve material circulation, 0.8 kg/h of CH<sub>4</sub> is combusted in the calciner to regenerate CaO, consuming 3.2 kg/h of O<sub>2</sub>. Overall, O<sub>2</sub> consumption for the entire cycle is reduced by 2.93 kg/h, compared to processes without CaO.</div></div>","PeriodicalId":17287,"journal":{"name":"Journal of The Energy Institute","volume":"120 ","pages":"Article 102114"},"PeriodicalIF":5.6000,"publicationDate":"2025-04-19","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Journal of The Energy Institute","FirstCategoryId":"5","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S1743967125001424","RegionNum":2,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q2","JCRName":"ENERGY & FUELS","Score":null,"Total":0}
引用次数: 0
Abstract
The quality of hydrogen produced from waste plastic steam gasification is compromised by CO2 and tar. While the use of CaO for CO2 adsorption and tar catalytic cracking has been explored, the impact of the heat released during CaO carbonation on hydrogen production has not been sufficiently studied. This work investigates the role of Fe-doped CaO in enhancing hydrogen production and tar removal during gasification. Aspen Plus is used to evaluate the impact of CaO carbonation heat on hydrogen generation via waste plastic steam gasification. Experimental results show that, at 700 °C and 20 vol% H2O, the H2 concentration and yield increase to 67.9 vol% and 288.6 mL/g, respectively, with a liquid production rate of 17 % when Ca90Fe10/PE mass ratio is 2.0. In simulations, with the gasifier operating at 700 °C and maintaining thermal equilibrium, H2 molar percentage is 58.5 % for an O2 inflow of 13.03 kg/h. At 700 °C and Ca90Fe10/PE mass ratio of 2.2, the heat generated by the CO2 adsorption reaction of CaO is 76.51 MJ/h and requires 6.9 kg/h of O2 and the molar percent of H2 is 80.76 %. To achieve material circulation, 0.8 kg/h of CH4 is combusted in the calciner to regenerate CaO, consuming 3.2 kg/h of O2. Overall, O2 consumption for the entire cycle is reduced by 2.93 kg/h, compared to processes without CaO.
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