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Lanthanum-based Perovskite Oxygen Carriers In Chemical Chain Steam Reforming Reactions

Posted on:2021-10-21Degree:MasterType:Thesis
Country:ChinaCandidate:Y J WangFull Text:PDF
GTID:2511306200954669Subject:Chemical Engineering
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Chemical looping reforming of methane(CLRM)process is a novel technology that can produce syngas and hydrogen simultaneously.In this technique,methane is first partially oxidized to syngas(H2+CO)by the lattice oxygen of the oxygen carrier.Subsequently,the reduced oxygen carrier recovers the missed lattice oxygen from the steam,and simultaneously produces hydrogen.The design and construction of oxygen carriers with high activity and stability is the key factor to realize this technology.La-based perovskite oxides can be used as oxygen carriers for CLRM technology due to their unique structural properties and excellent oxygen storage and release properties.The A or B cations in the perovskite structure can be partially substituted by another metal cation.Through this doping method,the valence of the cation and/or the amount of non-stoichiometric oxygen in the perovskite structure can be changed,generating more oxygen vacancies and improving the reactivity of the oxygen carrier.In this paper,Cu/Fe-doped LaMnO3-based perovskite oxygen carrier s were successfully prepared by the sol-gel method.The physical and chemical properties of oxygen carriers were characterized by XRD,BET,Raman,XPS and TPR.The reactivity of CLRM over LaMnO3,La1-x Mn CuxO3 and La1-x Mn FexO3/La Mn1-x FexO3oxygen carriers was systematically investigated.In addition,the influence of calcination temperature on the reactivity of oxygen carriers was further explored.LaMnO3 was used as an oxygen carrier for the CLRM process.It obtained a high resistance to carbon deposition,while a lower CH4 conversion due to the poor oxygen storage and release performance.La1-x Mn CuxO3 oxygen carriers exhibited good oxygen transport capacity and high reactivity during the CLR M process.In the methane partial oxidation stage,the syngas productivity of La1-x Mn CuxO3(2.79-5.20mmol/g)increased gradually with the Cu content.La0.85Mn Cu0.15O3 displayed the highest H2 productivity(2.52 mmol/g)in the water splitting cycle reaction.La1-x Mn FexO3/La Mn1-x FexO3 oxygen carriers owned higher reactivity and better resistance to carbon deposition.La 0.85Mn Fe0.15O3 sample exhibited the highest CO selectivity(?99%),syngas productivity(3.78 mmol/g)and H2 productivity(1.76mmol/g),and its H2/CO molar ratio was maintained at the ideal ratio of 2.0(1.93-2.07)during the whole process.Notably,no carbon deposition was generated over LaMnO3,La0.85Mn Fe0.15O3 and La Mn0.9Fe0.1O3 oxygen carriers even after 20 redox cycles,and La0.85Mn Fe0.15O3 exhibited superior resistance to carbon deposition due to the better structural and thermal stability.The effect of calcination temperature on structure properties of the La0.85Mn Fe0.15O3 and La Mn0.9Fe0.1O3 were investigated in detail.It was found that the series of La0.85Mn Fe0.15O3 samples exhibited a better structural stability.The samples calcined at 800 oC exhibited higher concentration of oxygen vacancies and better oxygen storage and release performance.During the 9 redox cycles,La0.85Mn Fe0.15O3-800 showed the best reactivity and thermal stability,and its H2/CO ratio maintained around the ideal value(about 2.0).
Keywords/Search Tags:Chemical looping reforming of methane, Syngas, Hydrogen, La-based perovskite oxygen carrier, Oxygen storage and release capacity
PDF Full Text Request
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