2019
DOI: 10.1016/j.energy.2018.11.106
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Syngas production by chemical looping gasification using Fe supported on phosphogypsum compound oxygen carrier

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Cited by 36 publications
(5 citation statements)
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“…When considering the presence of both the lines of the oxidation of H 2 to H 2 O and C to CO, it is possible to find a region where partial oxidation is thermodynamically preferred, ensuring a high selectivity for syngas production during chemical looping. While only the oxidation of Fe to FeO in Figure 8 lies between these lines, some oxidation reactions of mixed metal oxides can be found inside this area [140,141]. It should also be noted that this area becomes smaller when higher pressure is applied due to a shift in Gibbs free energy.…”
Section: Thermodynamic Limitationsmentioning
confidence: 89%
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“…When considering the presence of both the lines of the oxidation of H 2 to H 2 O and C to CO, it is possible to find a region where partial oxidation is thermodynamically preferred, ensuring a high selectivity for syngas production during chemical looping. While only the oxidation of Fe to FeO in Figure 8 lies between these lines, some oxidation reactions of mixed metal oxides can be found inside this area [140,141]. It should also be noted that this area becomes smaller when higher pressure is applied due to a shift in Gibbs free energy.…”
Section: Thermodynamic Limitationsmentioning
confidence: 89%
“…As the Gibbs free energy for the oxidation of this Cu/CuO pair is almost zero, it is even eligible for CLOU. Next to the original metal/metal oxide pairs, other materials can also be plotted when developing oxygen carrier materials [140,141]. Because of this, Ellingham diagrams are great tools when developing oxygen carrier materials to assess whether certain materials are suitable for CLC or even for CLR.…”
Section: Thermodynamic Limitationsmentioning
confidence: 99%
“…Chuayboon et al [15] reported that ZnO can oxidize biomass, and biomass/ZnO ratios have an important impact on gasification performance. In addition, Yang et al [24] studied chemical looping gasification using Fe supported on phosphogypsum compound as an oxygen carrier, and reported that this material has high oxygen exchange capacity, high selective conversion ability of C to CO, excellent activity and recyclability. Furthermore, the effect of equivalence ratio on the CO selectivity of Fe/Ca-based oxygen carriers in biochar chemical looping gasification was investigated [25], and the CO selectivity of Fe 2 O 3 decreased markedly with increasing equivalence ratio.…”
Section: Introductionmentioning
confidence: 99%
“…Nowadays, the utilization of fossil fuels has been considered as one of the biggest problems to the increasing emission of CO 2 . Chemical looping has emerged as a promising technology for coal utilization as it decreases the irreversible entropy production to increase the energy utilization efficiency. , It takes advantage of the redox behavior of oxygen carriers (OCs) between two individual reactors to realize initial CO 2 separation and NO x emission control without the enrollment of pure oxygen. In situ gasification chemical looping combustion (CLC) is known as a typical strategy for coal utilization for complete oxidization between the fuel and the OC in the reducer. , Conversely, chemical looping gasification (CLG) was proposed to achieve plenty of syngas (H 2 and CO) through partial oxidization, as is shown in Figure .…”
Section: Introductionmentioning
confidence: 99%