A variety of deposit compositions were examined in short-term laboratory tests with the aim of determining the corrosion mechanisms of fireside corrosion for a range of chromiaforming alloys in various combustion systems. The deposits formed in boilers are complex, and despite decades of study, the propagation mechanism of fireside corrosion is not well understood. Alkali iron trisulfates, which are stabilized by SO 3 in the gas atmosphere, have been believed to be the major corrosive species for many years. The propagation mechanism for fireside corrosion was investigated using T92 (a typical ferritic boiler steel) and a model austenitic Fe-Ni-Cr alloy and synthetic coal ash deposits. The metal loss, corrosion product morphologies, and compositions were carefully characterized in order to define a propagation mechanism. The corrosive species responsible for degradation was a (Na,K) 2 SO 4 -Fe 2 (SO 4 ) 3 solution and not alkali iron trisulfates, which is contrary to what has been believed for decades.The formation of the liquid deposit is similar to Type II hot corrosion of gas turbine engines.The mechanism is a synergistic dissolution process similar to that which can occur for hot corrosion as well. Simultaneous basic and acidic dissolution of protective Cr 2 O 3 and Fe 2 O 3 disrupts protective oxide formation and locally produces negative solubility gradients at the oxide/salt interface. The dissolved Fe 2 O 3 and Cr 2 O 3 reprecipitate where there is lower solubility, creating the observed corrosion products. The effect of the deposit composition, gas atmosphere iii composition, alloy composition, temperature, and deposit thickness were examined with respect to the proposed fireside corrosion mechanism. These measurements were found to be consistent with the proposed mechanism based on synergistic fluxing.iv Oxy-fuel firing is one of three ways in which CCS can be accomplished. The other two ways are post-combustion capture, where the CO 2 is removed from the flue gas after combustion, and pre-combustion capture, where the CO 2 is removed from the fuel before combustion. Oxy-1 fuel firing is carrying out the combustion in an environment consisting of recirculated flue gases containing primarily CO 2 , steam and pure oxygen instead of air in order to create a flue gas with minimal amounts of N 2 . A schematic diagram of the oxy-fuel process is shown below in Figure 1.
Figure 1: Schematic diagram of oxy-fuel combustionOxy-fuel combustion produces flue gases containing approximately 60%CO 2 -30%H 2 O-4%O 2 -5%N 2 , whereas traditional air-fired combustion produces flue gases containing 74%N 2 -[2] The flue gases in oxy-fuel systems are able to be recycled through the fuel burners leading to decreased CO 2 emissions. However, with the reduced amounts of nitrogen, the products of the oxy-fuel combustion process have increased amounts of CO 2 , steam and corrosive gases, such as SO 2 that can cause significant corrosion in superheater and reheater 2 tubes when compared to air-fired combustion. Bu...