Carbonation of fly ash in oxy-fuel CFB combustion

Abstract

Oxy-fuel combustion of fossil fuel is one of the most promising methods to produce a stream of concentrated CO 2 ready for sequestration. Oxy-fuel FBC (fluidized bed combustion) can use limestone as a sorbent for in situ capture of sulphur dioxide. Limestone will not calcine to CaO under typical oxy-fuel circulating FBC (CFBC) operating temperatures because of the high CO 2 partial pressures. However, for some fuels, such as anthracites and petroleum cokes, the typical combustion temperature is above 900 °C. At CO 2 concentrations of 80–85% (typical of oxy-fuel CFBC conditions with flue gas recycle) limestone still calcines, but when the ash cools to the calcination temperature, carbonation of fly ash deposited on cool surfaces may occur. This phenomenon has the potential to cause fouling of the heat transfer surfaces in the back end of the boiler, and to create serious operational difficulties. In this study, fly ash generated in a utility CFBC boiler was carbonated in a thermogravimetric analyzer (TGA) under conditions expected in an oxy-fuel CFBC. The temperature range investigated was from 250 to 800 °C with CO 2 concentration set at 80% and H 2O concentrations at 0%, 8% and 15%, and the rate and the extent of the carbonation reaction were determined. Both temperature and H 2O concentrations played important roles in determining the reaction rate and extent of carbonation. The results also showed that, in different temperature ranges, the carbonation of fly ash displayed different characteristics: in the range 400 °C < T ⩽ 800 °C, the higher the temperature the higher the CaO-to-carbonate conversion ratio. The presence of H 2O in the gas phase always resulted in higher CaO conversion ratio than that obtainable without H 2O. For T ⩽ 400 °C, no fly ash carbonation occurred without the presence of H 2O in the gas phase. However, on water vapour addition, carbonation was observed, even at 250 °C. For T ⩽ 300 °C, small amounts of Ca(OH) 2 were found in the final product alongside CaCO 3. Here, the carbonation mechanism is discussed and the apparent activation energy for the overall reaction determined.