钙环
烟气
电弧炉
废物管理
工艺工程
灵活性(工程)
碳捕获和储存(时间表)
烟道
残余物
工程类
过程(计算)
生物量(生态学)
混合(物理)
固体燃料
煤
碳纤维
选矿
环境科学
陶瓷
化学链燃烧
燃料效率
平炉
精炼(冶金)
钢厂
材料科学
冶金
作者
Néstor D. Montiel-Bohórquez,Manuele Gatti,Matteo C. Romano
标识
DOI:10.1016/j.ccst.2025.100504
摘要
This study presents a techno-economic analysis of four configurations of the Calcium Looping (CaL) technology, tailored to enhance system flexibility for capturing CO 2 from the fluctuating flue gases generated by a scrap-based Electric Arc Furnace with a capacity of 112 t steel /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 CO2 captured. Under the assumptions considered, the CaL system achieved a CO 2 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 2 removal rates of 13-26 t CO2 /h, corresponding to 100-200 kg CO2 removed per t steel produced. From an economic standpoint, increment in steel cost ranged from 26 to 36 €/t steel (assuming a carbon tax of 100 €/t CO2 ), with costs of CO 2 avoided of 202-255 €/t CO2 .
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