化学链燃烧
合成气
双金属片
氢
非阻塞I/O
制氢
氧气
化学工程
氧化物
燃烧室
材料科学
产量(工程)
化学
碳纤维
减速器
冶金
燃烧
催化作用
热力学
有机化学
工程类
物理
复合数
复合材料
作者
Chuanbao Luan,Qifan Cheng,Naiping Zhu,Andrew Tong,Yinan Zhang,Usina Martha Moatswi,Shiyu Li,Liang Zeng,Liang‐Shih Fan
摘要
Abstract The syngas chemical looping (SCL) process is an advanced thermochemical approach for hydrogen production with in situ carbon capture. This article proposes a novel Ni–Fe bimetallic oxide in a three‐reactor chemical looping system. In the moving bed reducer, a mixture of NiO and Fe 3 O 4 is countercurrently reduced by syngas to Ni and Fe/FeO. In the oxidizer, the Fe/FeO mixture is oxidized back to Fe 3 O 4 by steam, producing high‐purity H 2 , while Ni remains unchanged. In the combustor, Ni is oxidized to NiO by air to supply heat, while Fe 3 O 4 is maintained without further oxidation to Fe 2 O 3 . The reducer's operating conditions are optimized using the operating line diagram method and the multistage equilibrium model. Process simulation results show that the Ni–Fe oxygen carrier can increase blue hydrogen production efficiency by more than 5% compared to the Fe‐based SCL process, while ensuring a carbon capture rate of over 99%.
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