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 |
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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. |
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ISSN: | 0360-3199 1879-3487 |
DOI: | 10.1016/j.ijhydene.2011.05.025 |