早稲田大学 · 工学
Manuel Bailera教授の研究室は、鉄鋼業界の脱炭素化に向けた革新的な技術開発を主眼としています。特に、再生可能エネルギーを活用した「パワー・トゥ・X」プロセス(Power to Iron, Power to Gasなど)の統合的アプローチや、酸素吹き出し高炉とPower to Gas技術の融合による炭素循環型鉄鋼プロセスの構築を推進しています。また、Rist図を拡張した新規シミュレーション手法や、Ca-Loopingを用いた太陽熱エネルギー貯蔵の高精度モデリングなど、熱化学的プロセスの最適化にも貢献しています。
Figures are computed from collected data and may differ slightly.
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
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