Waseda University · 공학
Manuel Bailera 교수의 연구실은 철강 산업의 탄소중립화를 위한 혁신적 기술 개발에 초점을 맞추고 있습니다. 전기로 기반의 Power to X 기술, 특히 Power to Gas와 연계한 산재 공정 최적화, 그리고 Ca-Looping 기반 열에너지 저장 기술을 핵심 연구 분야로 다룹니다. 특히, 재생 가능 에너지와 연계된 철강 공정의 탄소 순환 및 에너지 효율성 향상 전략을 체계적으로 분석하고 있습니다. 이는 탄소 배출을 줄이고, 지속 가능한 철강 생산을 실현하기 위한 종합적 접근입니다.
표시된 성과는 수집된 데이터 기준으로 산출되며, 일부 차이가 있을 수 있습니다.
In this paper we present the first systematic review of Power to X processes applied to the iron and steel industry. These processes convert renewable electricity into valuable chemicals through an electrolysis stage that produces the final product or a necessary intermediate. We have classified them in five categories (Power to Iron, Power to Hydrogen, Power to Syngas, Power to Methane and Power to Methanol) to compare the results of the different studies published so far, gathering specific en
Ca-Looping represents one of the most promising technologies for thermochemical energy storage. This process based on the carbonation-calcination cycle of CaO offers a high potential to be coupled with solar power plants for its long-term storage capacity and high temperatures. Previous studies analyzed different configurations of CaL integrated into power cycles aiming to improve efficiency. However, most of these assessments based on lumped models did not account for scale effect in the most c
<b>Background:</b> The Rist diagram is useful for predicting changes in blast furnaces when the operating conditions are modified. In this paper, we revisit this methodology to provide a general model with additions and corrections. The reason for this is to study a new concept proposal that combines oxygen blast furnaces with Power to Gas technology. The latter produces synthetic methane by using renewable electricity and CO <sub>2</sub> to partly replace the fossil input in the blast furnace.
This paper assesses the injection of different syngas in air-blown blast furnaces, oxygen blast furnaces, and advanced oxygen blast furnaces. The selected types of syngas come from biomass gasification, plastic gasification, CO2 electrolysis, and reverse water–gas shift reaction. An Aspen Plus model, based on the new extended operating line methodology, was used for the simulation. This methodology is a generalization of the conventional Rist diagram, to extend its application to cases in which