电弧炉炼钢中捕集二氧化碳的柔性钙环:技术经济分析

Néstor D. Montiel-Bohórquez, Manuele Gatti, Matteo C. Romano
{"title":"电弧炉炼钢中捕集二氧化碳的柔性钙环:技术经济分析","authors":"Néstor D. Montiel-Bohórquez,&nbsp;Manuele Gatti,&nbsp;Matteo C. Romano","doi":"10.1016/j.ccst.2025.100504","DOIUrl":null,"url":null,"abstract":"<div><div>This study presents a techno-economic analysis of four configurations of the Calcium Looping (CaL) technology, tailored to enhance system flexibility for capturing CO<sub>2</sub> from the fluctuating flue gases generated by a scrap-based Electric Arc Furnace with a capacity of 112 t<sub>steel</sub>/h. The configurations differ based on the solids circulation strategy between reactors (constant or variable) and the presence of one or two intermediate solids storage vessels. Configurations incorporating intermediate solids storage demonstrated operational advantages, including enhanced process stability and downsized calciner island components. Moreover, the plant configuration with two intermediate solids storages led to the lowest specific fuel consumption of 5.85 MJ per kg<sub>CO2</sub> captured.</div><div>Under the assumptions considered, the CaL system achieved a CO<sub>2</sub> capture rate of 91 % from the EAF off-gas. Moreover, using residual forestry biomass as fuel in the calciner enabled to achieve negative emissions with net CO<sub>2</sub> removal rates of 13-26 t<sub>CO2</sub>/h, corresponding to 100-200 kg<sub>CO2</sub> removed per t<sub>steel</sub> produced.</div><div>From an economic standpoint, increment in steel cost ranged from 26 to 36 €/t<sub>steel</sub> (assuming a carbon tax of 100 €/t<sub>CO2</sub>), with costs of CO<sub>2</sub> avoided of 202-255 €/t<sub>CO2</sub>.</div></div>","PeriodicalId":9387,"journal":{"name":"Carbon Capture Science & Technology","volume":"17 ","pages":"Article 100504"},"PeriodicalIF":0.0000,"publicationDate":"2025-09-04","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Flexible calcium looping for CO2 capture in electric Arc Furnace steelmaking: A techno-economic analysis\",\"authors\":\"Néstor D. Montiel-Bohórquez,&nbsp;Manuele Gatti,&nbsp;Matteo C. Romano\",\"doi\":\"10.1016/j.ccst.2025.100504\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><div>This study presents a techno-economic analysis of four configurations of the Calcium Looping (CaL) technology, tailored to enhance system flexibility for capturing CO<sub>2</sub> from the fluctuating flue gases generated by a scrap-based Electric Arc Furnace with a capacity of 112 t<sub>steel</sub>/h. The configurations differ based on the solids circulation strategy between reactors (constant or variable) and the presence of one or two intermediate solids storage vessels. Configurations incorporating intermediate solids storage demonstrated operational advantages, including enhanced process stability and downsized calciner island components. Moreover, the plant configuration with two intermediate solids storages led to the lowest specific fuel consumption of 5.85 MJ per kg<sub>CO2</sub> captured.</div><div>Under the assumptions considered, the CaL system achieved a CO<sub>2</sub> capture rate of 91 % from the EAF off-gas. Moreover, using residual forestry biomass as fuel in the calciner enabled to achieve negative emissions with net CO<sub>2</sub> removal rates of 13-26 t<sub>CO2</sub>/h, corresponding to 100-200 kg<sub>CO2</sub> removed per t<sub>steel</sub> produced.</div><div>From an economic standpoint, increment in steel cost ranged from 26 to 36 €/t<sub>steel</sub> (assuming a carbon tax of 100 €/t<sub>CO2</sub>), with costs of CO<sub>2</sub> avoided of 202-255 €/t<sub>CO2</sub>.</div></div>\",\"PeriodicalId\":9387,\"journal\":{\"name\":\"Carbon Capture Science & Technology\",\"volume\":\"17 \",\"pages\":\"Article 100504\"},\"PeriodicalIF\":0.0000,\"publicationDate\":\"2025-09-04\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Carbon Capture Science & Technology\",\"FirstCategoryId\":\"1085\",\"ListUrlMain\":\"https://www.sciencedirect.com/science/article/pii/S2772656825001411\",\"RegionNum\":0,\"RegionCategory\":null,\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"\",\"JCRName\":\"\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Carbon Capture Science & Technology","FirstCategoryId":"1085","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/S2772656825001411","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
引用次数: 0

摘要

本研究对钙环(CaL)技术的四种配置进行了技术经济分析,旨在提高系统的灵活性,以便从容量为112吨钢/小时的废钢电弧炉产生的波动烟气中捕获二氧化碳。根据反应器(恒定或可变)之间的固体循环策略以及一个或两个中间固体储存容器的存在,配置不同。结合中间固体存储的配置展示了操作优势,包括增强的工艺稳定性和缩小的分解炉岛组件。此外,具有两个中间固体储存库的工厂配置导致最低的比燃料消耗为5.85 MJ / kgCO2捕获。在考虑的假设下,CaL系统从EAF废气中实现了91%的二氧化碳捕集率。此外,在煅烧炉中使用剩余的林业生物质作为燃料能够实现负排放,净CO2去除率为13-26 tCO2/h,相当于每生产一吨钢去除100-200 公斤CO2。从经济角度来看,钢铁成本的增量在26 - 36欧元/吨(假设碳税为100欧元/吨二氧化碳)之间,二氧化碳成本的减少为202-255欧元/吨二氧化碳。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Flexible calcium looping for CO2 capture in electric Arc Furnace steelmaking: A techno-economic analysis
This study presents a techno-economic analysis of four configurations of the Calcium Looping (CaL) technology, tailored to enhance system flexibility for capturing CO2 from the fluctuating flue gases generated by a scrap-based Electric Arc Furnace with a capacity of 112 tsteel/h. The configurations differ based on the solids circulation strategy between reactors (constant or variable) and the presence of one or two intermediate solids storage vessels. Configurations incorporating intermediate solids storage demonstrated operational advantages, including enhanced process stability and downsized calciner island components. Moreover, the plant configuration with two intermediate solids storages led to the lowest specific fuel consumption of 5.85 MJ per kgCO2 captured.
Under the assumptions considered, the CaL system achieved a CO2 capture rate of 91 % from the EAF off-gas. Moreover, using residual forestry biomass as fuel in the calciner enabled to achieve negative emissions with net CO2 removal rates of 13-26 tCO2/h, corresponding to 100-200 kgCO2 removed per tsteel produced.
From an economic standpoint, increment in steel cost ranged from 26 to 36 €/tsteel (assuming a carbon tax of 100 €/tCO2), with costs of CO2 avoided of 202-255 €/tCO2.
求助全文
通过发布文献求助,成功后即可免费获取论文全文。 去求助
来源期刊
自引率
0.00%
发文量
0
×
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