Contaminants found in air, fuel or water can combine in the turbine hot section to produce corrosion, erosion and/or deposition. The fundamental role of high temperature coatings is to delay the onset of substrate deterioration and attendant effects on component structural integrity. To achieve this, the total concentration of each harmful contaminant in the turbine environment should be determined in order to select the appropriate material condition necessary, coated or uncoated, for the airfoil surface to survive the expected service time successfully. A method is presented whereby the total fuel equivalent concentration of any contaminant from all sources can be calculated. Utilization of this methodology is demonstrated by means of a hypothetical case of a turbine operating under specifically defined conditions. In this example, sodium (plus potassium) concentrations in air and fuel are assumed to be well within industry-accepted standards of 1 ppmw and it is shown that the use of untreated potable water for water injection and evaporative cooling can result in unacceptably high sodium concentrations. Subsequently, the extent and cost of water clean-up can be optimized by assessing the costs of water treatment equipment and the volume of water to be treated for emissions control and evaporative cooling. Field experiences with a turbine of 12 000 horsepower further substantiate the diagnostic advantages of this approach. In three cited cases, the presence of excessive sodium in the turbine hot section resulted in Type I or high temperature hot corrosion degradation of stage 1 blades. The source of contamination was attributed to water-borne sodium, using the methodology described. Corrective action recommended was directed at reducing the sodium concentrations in both the evaporative cooling water and the injected water and with target levels specified to ensure compliance with Solar's specification limit of 1 ppmw (fuel equivalent concentration) of total sodium. A platinum-modified aluminide coating was also applied to first- and second-stage blading. It is demonstrated that, with this approach, total corrosion control can be realized by assessing the source(s) of contamination followed by application of appropriate corrective action to reduce the level of contamination economically.
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