4.7 Article

Kinetic and thermodynamic analysis of iron oxide reduction by graphite for CO2 mitigation in chemical-looping combustion

期刊

INTERNATIONAL JOURNAL OF ENERGY RESEARCH
卷 44, 期 5, 页码 3865-3882

出版社

WILEY
DOI: 10.1002/er.5184

关键词

chemical-looping combustion; Coats-Redfern model; distributed activation energy model; iron oxide and graphite; kinetics and thermodynamics; TGA

资金

  1. Ministry of Science and Technology [108-3116-F-006-007-CC1]
  2. Ministry of Education
  3. Ministry of Science and Technology of Taiwan [MOST 108-3116-F-006-007-CC1, MOST 107-2811-E-006-529, MOST 106-2923-E-006-002-MY3]

向作者/读者索取更多资源

Chemical-looping combustion (CLC) provides a platform to generate energy streams while mitigating CO2 using iron oxide as a carrier of oxygen. Through the reduction process, iron oxide experiences phase transformation to ultimately produce metallic iron. To understand iron oxide reduction characteristics and optimally design the fuel reactor, kinetic and thermodynamic analyses were proposed, utilizing graphite. This study aims to evaluate the reduction behavior under the non-isothermal process of various mixture ratios of hematite and graphite via thermogravimetric analysis with simultaneously evaluating evolved gases using a Fourier transform infrared spectrometer. The Coats-Redfern model was employed to approximate the kinetic and thermodynamic parameters which assessed the different reaction mechanisms together with the distributed activation energy model (DAEM). The results revealed that the hematite-to-graphite ratio of 4:1 had the highest reduction degree and had three distinct peaks representing three iron oxide reduction phases. The zero-order reaction mechanism agreed with the experimental results compared with other reaction models. The thermodynamic analysis showed an overall endothermic spontaneous reaction for the three phases which signified the direct reduction of the iron oxides. The DAEM result validated a stepwise reduction of iron oxides to metallic iron. The study aids the optimal design of the CLC fuel reactor for enhanced system performance.

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