Production of high purity H2 through chemical-looping water-gas shift at reforming temperatures - The importance of non-stoichiometric oxygen carriers

被引:24
作者
de Leeuwe, Christopher [1 ,2 ]
Hu, Wenting [1 ]
Evans, John [3 ]
von Stosch, Moritz [1 ]
Metcalfe, Ian S. [1 ]
机构
[1] Newcastle Univ, Sch Engn, Newcastle Upon Tyne NE1 7RU, Tyne & Wear, England
[2] Univ Manchester, Dept Chem Engn & Analyt Sci, Manchester M1 3AL, Lancs, England
[3] Univ Durham, Dept Chem, Durham DH1 3LE, England
基金
英国工程与自然科学研究理事会; 欧洲研究理事会;
关键词
Hydrogen production; Reactor modelling; Chemical looping; Carbon capture and storage; BED REACTOR; HYDROGEN; COMBUSTION;
D O I
10.1016/j.cej.2021.130174
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
H2 is an important feedstock for many industrial processes and could be used as an energy carrier in a low carbon economy. This means that carbon neutral methods for H2 production are of vital importance. Chemical looping allows for H2 production with inherent carbon separation, making it an ideal system to produce low carbon H2. This work generates insights into the production of high purity H2 using a chemical looping packed bed reactor system containing an oxygen carrier of variable oxygen non-stoichiometry. Such a system has been shown to achieve 95% conversion of H2O to H2 at 1073 K outperforming the maximum theoretical conversions of 50% achieved by a conventional water gas shift reactor at that temperature. A numerical model was developed from theoretical consideration, with no fitted parameters and used to simulate the working reactor. Operando measurement of gas conversions and changes in solid oxygen capacity, through synchrotron X-ray diffraction, were used to validate the numerical model and confirmed that the reaction was thermodynamically limited. The model the model was shown to reproduce the conversion of the oxygen carrier, the reactant conversion and the product evolution. Sensitivity analysis showed that the relationship between the oxygen carrier material oxygen content and the chemical potential of oxygen in the carrier was the key consideration for the design and operation of a packed bed chemical looping reactor using an oxygen carrier of variable non-stoichiometry.
引用
收藏
页数:18
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