ABSTRACT
Combustion of coal in air leads to a gaseous product stream (flue gas) that mainly contains nitrogen (N2), carbon dioxide (CO2), water vapor, and small quantities of many other gases such as sulphur oxides (SO2 and SO3) and nitrogen oxides (NOx mainly, NO, and NO2) as well as particulates (mainly coal fly ash (CFA)) at different concentrations depending upon the content of the coal and the quantity of air used for its combustion. The need to maintain reliable power while reducing greenhouse gas emissions has been driving governments and companies worldwide toward CO2 capture and storage/utilization. One such initiative is SaskPower's Integrated Carbon Capture and Storage (CCS) project at its Boundary Dam Unit 3 (BD3), which is amine based and just passed 10 years of commercial operation. The listed impurities in coal flue gas, of which CFA is the current focus, can cause degradation of the amines and have many other adverse effects on the capture process. Indeed, current electrostatic precipitators or fabric filters are designed to remove most of the CFA (typically up to ~ 99.9% or 99.99%, respectively), yet accumulation of the relatively small unremoved fraction within the CCS process is documented as causing physical barriers to the operation. One aspect of the effect of CFA on the amine-based CO2 capture system which is very poorly elucidated is its interactions with the gaseous acidic impurities in the flue gas and with added treatment chemicals as it traverses various sections of the process under different conditions such as pH and temperature, and how these can affect the overall performance of CCS systems. In this current paper we present the chemistry behind changes in the composition of CFA as it travels through the flue gas pretreatments and the integrated amine-based post-combustion SO2 and CO2 capture process at the BD3 CCS facility. Generally, through the various stages of treatment, CFA is modified in various ways including a) extensive depletion of water or acid leachable ions of metals like aluminium (Al), iron (Fe), magnesium (Mg), sodium (Na), and potassium (K) at the pre-scrubbing stage (pH ~2); b) co-deposition with CFA of sulphate and phosphate salts of Na, Fe, and barium (Ba) due to leaching of the respective ions from CFA (and from steel material corrosion in the case of Fe) at the flue gas cooling and the SO2 absorption stages, at high enough levels to exceed their saturation point or solubility products; and c) silicon dioxide or silica (SiO2) removal at certain sections within the CO2 capture stage due to its leaching from CFA under some high pH and temperature conditions.
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