CO2 Capture from Coal Combustion Using Chemical-Looping Combustion - Reactivity Investigation of Fe, Ni and Mn Based Oxygen Carriers Using Syngas

Chemical-looping combustion (CLC) is a combustion technology where an oxygen carrier is used to transfer oxygen from the combustion air to the fuel, thus avoiding direct contact between air and fuel. The system is composed of two reactors, a fuel and an air reactor, where the flue gas from the fuel reactor contains CO2 and H2O and the flue gas from the air reactor contains only N2 and some unreacted O2. Thus, CO2 and H2O are inherently separated from the rest of the flue gases, and no major energy is expended for this separation. This paper investigates the use of three promising oxygen carriers based on the metals Mn, Fe and Ni together with syngas from coal gasification. Reactivity investigations in a laboratory fluidized bed reactor under alternating oxidizing and reducing conditions, using 50% H2 and 50% CO for the reducing period, and 5% O2 for the oxidation period, found that the reactivity of all three was high at 950°C. For the Mn and Ni based oxygen carriers, there was full conversion of the fuel gas using bed masses of 46 and 173 kg oxygen carrier per MW of syngas. The Fe based carrier had a somewhat lower reactivity, but the gas yield to CO2 was still high. The effect of temperature was investigated, and manganese oxide showed high reactivity and conversion interval in the temperature range 650-950°C. For Ni and Fe based carriers the degree of conversion decreased as a function of temperature, although the initial reactivity was high. At lower temperatures there was formation of both carbon and methane for some of the oxygen carriers. This was associated with low degrees of gas yields, and is not expected in a real system. For comparison methane was also used as fuel. The nickel based carrier showed a much higher reactivity in comparison to manganeseand iron oxide at 950°C. Thus one implication of the results in this paper are that when using syngas as fuel, the cheaper and more environmentally sound Mn or Fe-based particles may be better candidates compared to Ni. On the other hand, when using natural gas, which has a high content of methane, Ni based particles would be the preferred oxygen carrier.

[1]  A. Abad,et al.  Reduction and Oxidation Kinetics of a Copper-Based Oxygen Carrier Prepared by Impregnation for Chemical-Looping Combustion , 2004 .

[2]  Anders Lyngfelt,et al.  The use of petroleum coke as fuel in chemical-looping combustion , 2007 .

[3]  Anders Lyngfelt,et al.  Investigation of Mn3O4 With Stabilized ZrO2 for Chemical-Looping Combustion , 2006 .

[4]  H. Richter,et al.  Reversibility of combustion processes , 1983 .

[5]  A. Lyngfelt,et al.  Thermal Analysis of Chemical-Looping Combustion , 2006 .

[6]  A. Abad,et al.  Mapping of the range of operational conditions for Cu-, Fe-, and Ni-based oxygen carriers in chemical-looping combustion , 2007 .

[7]  A. Lyngfelt,et al.  Capture of CO2 using chemical-looping combustion , 2001 .

[8]  Anders Lyngfelt,et al.  Chemical-looping combustion in a 300 W continuously operating reactor system using a manganese-based oxygen carrier , 2006 .

[9]  J. Houghton,et al.  Climate change 2001 : the scientific basis , 2001 .

[10]  A. Lyngfelt,et al.  A fluidized-bed combustion process with inherent CO2 separation; Application of chemical-looping combustion , 2001 .

[11]  D. Zheng,et al.  Evaluation of a chemical-looping-combustion power-generation system by graphic exergy analysis , 1987 .

[12]  A. Abad,et al.  Selection of Oxygen Carriers for Chemical-Looping Combustion , 2004 .

[13]  A. Lyngfelt,et al.  Combustion of Syngas and Natural Gas in a 300 W Chemical-Looping Combustor , 2006 .

[14]  A. Lyngfelt,et al.  Construction and 100 h of operational experience of a 10-kW chemical looping combustor , 2005 .