Synergistic effects of chemical looping gasification of domestic sludge with corn straw using red mud oxygen carrier for hydrogen-rich syngas production

IF 4.3 4区 工程技术 Q3 ENERGY & FUELS
Shangqing Xi, Xiaojia Wang, Ankang Liu, Didi Gai, Maoqing Tang, Jiawei Wang
{"title":"Synergistic effects of chemical looping gasification of domestic sludge with corn straw using red mud oxygen carrier for hydrogen-rich syngas production","authors":"Shangqing Xi,&nbsp;Xiaojia Wang,&nbsp;Ankang Liu,&nbsp;Didi Gai,&nbsp;Maoqing Tang,&nbsp;Jiawei Wang","doi":"10.1007/s13399-026-07269-6","DOIUrl":null,"url":null,"abstract":"<div><p>The conversion of domestic sludge into high-value syngas remains challenging because of its low reactivity and high ash content. In this study, a triple-waste chemical looping gasification (CLG) strategy was proposed by integrating domestic sludge, corn straw, and industrial red mud for the production of hydrogen-rich syngas. The effects of key operating parameters, including blending ratio, O/C ratio, reaction temperature, and steam flow rate, on gas composition, total gas yield, cold gas efficiency, carbon conversion rate, effective gas fraction, and lower heating value were systematically evaluated. The optimal conditions were identified as a corn straw/domestic sludge blending ratio of 0.6 (0.5 g sludge), an O/C ratio of 0.3, a reaction temperature of 900 °C, and a steam flow rate of 0.2 mL/min. Under these conditions, a hydrogen fraction of 56% and a total gas yield of 1.23 Nm<sup>3</sup>/kg were achieved, accompanied by a cold gas efficiency of 93.33%, a carbon conversion of 80.97%, and an effective gas fraction of 81.21%. Additionally, cyclic redox experiments confirmed that the red mud oxygen carrier maintained good reactivity and stability over five consecutive cycles. This work demonstrates a sustainable and efficient strategy for sludge-to-syngas conversion via CLG and highlights the advantages of employing industrial solid waste oxygen carriers and biomass-sludge synergistic gasification.</p></div>","PeriodicalId":488,"journal":{"name":"Biomass Conversion and Biorefinery","volume":"16 18","pages":""},"PeriodicalIF":4.3000,"publicationDate":"2026-09-21","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Biomass Conversion and Biorefinery","FirstCategoryId":"5","ListUrlMain":"https://link.springer.com/article/10.1007/s13399-026-07269-6","RegionNum":4,"RegionCategory":"工程技术","ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q3","JCRName":"ENERGY & FUELS","Score":null,"Total":0}
引用次数: 0

Abstract

The conversion of domestic sludge into high-value syngas remains challenging because of its low reactivity and high ash content. In this study, a triple-waste chemical looping gasification (CLG) strategy was proposed by integrating domestic sludge, corn straw, and industrial red mud for the production of hydrogen-rich syngas. The effects of key operating parameters, including blending ratio, O/C ratio, reaction temperature, and steam flow rate, on gas composition, total gas yield, cold gas efficiency, carbon conversion rate, effective gas fraction, and lower heating value were systematically evaluated. The optimal conditions were identified as a corn straw/domestic sludge blending ratio of 0.6 (0.5 g sludge), an O/C ratio of 0.3, a reaction temperature of 900 °C, and a steam flow rate of 0.2 mL/min. Under these conditions, a hydrogen fraction of 56% and a total gas yield of 1.23 Nm3/kg were achieved, accompanied by a cold gas efficiency of 93.33%, a carbon conversion of 80.97%, and an effective gas fraction of 81.21%. Additionally, cyclic redox experiments confirmed that the red mud oxygen carrier maintained good reactivity and stability over five consecutive cycles. This work demonstrates a sustainable and efficient strategy for sludge-to-syngas conversion via CLG and highlights the advantages of employing industrial solid waste oxygen carriers and biomass-sludge synergistic gasification.

赤泥氧载体玉米秸秆化学环气化生产富氢合成气的协同效应
由于生活污泥反应性低,灰分含量高,将其转化为高价值合成气仍然具有挑战性。本研究以生活污泥、玉米秸秆和工业赤泥为原料,提出了一种三废化学循环气化(CLG)策略,用于生产富氢合成气。系统评价了共混比、O/C比、反应温度和蒸汽流量等关键操作参数对气体组成、总产气率、冷气效率、碳转化率、有效气分率和低热值的影响。确定了玉米秸秆/生活污泥混合比为0.6 (0.5 g污泥),O/C比为0.3,反应温度为900℃,蒸汽流量为0.2 mL/min的最佳工艺条件。在此条件下,氢气馏分为56%,总产气量为1.23 Nm3/kg,冷气效率为93.33%,碳转化率为80.97%,有效气体馏分为81.21%。此外,循环氧化还原实验证实,红泥氧载体在连续5个循环中保持了良好的反应性和稳定性。这项工作展示了通过CLG将污泥转化为合成气的可持续和高效策略,并强调了使用工业固体废物氧载体和生物质-污泥协同气化的优势。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
求助全文
约1分钟内获得全文 求助全文
来源期刊
Biomass Conversion and Biorefinery
Biomass Conversion and Biorefinery Energy-Renewable Energy, Sustainability and the Environment
CiteScore
7.00
自引率
15.00%
发文量
1358
期刊介绍: Biomass Conversion and Biorefinery presents articles and information on research, development and applications in thermo-chemical conversion; physico-chemical conversion and bio-chemical conversion, including all necessary steps for the provision and preparation of the biomass as well as all possible downstream processing steps for the environmentally sound and economically viable provision of energy and chemical products.
×
引用
GB/T 7714-2015
复制
MLA
复制
APA
复制
导出至
BibTeX EndNote RefMan NoteFirst NoteExpress
×
提示
您的信息不完整,为了账户安全,请先补充。
现在去补充
×
提示
您因"违规操作"
具体请查看互助需知
我知道了
×
提示
确定
请完成安全验证×
copy
已复制链接
快去分享给好友吧!
我知道了
右上角分享
点击右上角分享
0
联系我们:info@booksci.cn Book学术提供免费学术资源搜索服务,方便国内外学者检索中英文文献。致力于提供最便捷和优质的服务体验。 Copyright © 2023 布克学术 All rights reserved.
京ICP备2023020795号-1
ghs 京公网安备 11010802042870号
Book学术文献互助
Book学术文献互助群
群 号:604180095
Book学术官方微信
小红书