Optimization of hydrogen production by Chemical-Looping auto-thermal Reforming working with Ni-based oxygen-carriers

Chemical-Looping auto-thermal Reforming (CLRa) is a new process for hydrogen production from natural gas that uses the same principles as Chemical-Looping Combustion (CLC). The main difference with CLC is that the desired product is syngas (H 2 + CO) instead of CO 2 + H 2O. For that, in the CLRa pro...

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Veröffentlicht in:International journal of hydrogen energy 2011-08, Vol.36 (16), p.9663-9672
Hauptverfasser: Ortiz, María, Abad, Alberto, de Diego, Luis F., García-Labiano, Francisco, Gayán, Pilar, Adánez, Juan
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Sprache:eng
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Zusammenfassung:Chemical-Looping auto-thermal Reforming (CLRa) is a new process for hydrogen production from natural gas that uses the same principles as Chemical-Looping Combustion (CLC). The main difference with CLC is that the desired product is syngas (H 2 + CO) instead of CO 2 + H 2O. For that, in the CLRa process the air-to-fuel ratio is kept low to prevent the complete oxidation of the fuel. The major advantage of this technology is that the heat needed for converting CH 4 to syngas is supplied without costly oxygen production and without mixing of air with carbon containing fuel gases. An important aspect to be considered in the design of a CLRa system is the heat balance. In this work, mass and heat balances were done to determine the auto-thermal operating conditions that maximize H 2 production in a CLRa system working with Ni-based oxygen-carriers. It was assumed that the product gas was in thermodynamic equilibrium at the exit of the air- and fuel-reactors and the equilibrium gas compositions were obtained by using the method of minimization of the Gibbs free energy of the system. It was found that to reach auto-thermal conditions the oxygen-to-methane molar ratio should be higher than 1.20, which means that the maximum H 2 yield is about 2.75 mol H 2/mol CH 4. The best option to control the oxygen-to-methane molar ratio is to control the air flow fed to the air-reactor because a lower air excess is needed to reach auto-thermal conditions. ► The auto-thermal operating conditions that maximize H 2 production in CLRa with Ni-based materials were determined. ► Low Ni-content materials could be preferred in a CLRa system. ► To reach auto-thermal conditions an excess of oxygen was needed in relation to stoichiometric conditions. ► H 2 production was maximized by controlling the oxygen excess with the air flow fed to the air-reactor. ► At optimum conditions, 2.75 mol H 2/mol CH 4 could be produced being CO 2 unmixed with nitrogen.
ISSN:0360-3199
1879-3487
DOI:10.1016/j.ijhydene.2011.05.025