Project Year #3 research work has included a model/paper study of the effects of chemical additives on the performance in spray drying and induct injection processes. A one-dimensional model formulated by the Energy and Environmental Research Corporation (EER, 1989) was selected as the basic vehicle for this study. The basic EER model was modified to allow for a range of additive effects. A brief experimental study was made in a effort to quantify the effects of both magnesium and "inert" contents on the low temperature dry capture effectiveness of hydrated lime. The results of this experimental study were inconclusive. High Temperature Studies. Cole et al. [1986], using an isothermal reactor at 2000°F, Ca/S=2, and 2000 ppm SO2 showed that calcitic hydrates were more reactive that calcitic carbonates. They attributed this observation to a combination of three reasons: (1) Dehydration occurs much more rapidly than CO2 evolution, therefore the time available for sulfation after the calcination process is significantly greater for hydrates than for carbonates, (2) hydrates begin with a much higher initial surface area, and (3) the dehydration process generally produces a reduction in the mean particle size of the sorbent thereby reducing the internal diffusion resistance to SO= diffusion. Between the two types of calcium-based sorbents generally used in in-furnace injection, it is well documented that CaO derived from Ca(OH)= (h-CaO) is more 1-1 reactive than CaO derived from CaC03 (c-CaO) [Silcox et al., 1987]. This is attributed in part to the smaller particle size of h-CaO, and more importantly, to the pore structure of the CaO produced. The h-CaO has a slit or plate-like structure while the structure of c-CaO is in the form of cylindrical pores (or spherical grains). The platelike structure retains its porosity to a greater extent by allowing for particle expansion [Gullett and Bruce, 1987], and results in higher rates of diffusion of the reactant through the product layer [Bruce et al., 1989]. 1.2.2 Calcium/Maqnesium R,,.atio High Temperature Studies. Snow et al. [1986], injecting sorbents into a flue gas stream produced by the combustion of Pittsburgh No. 8 coal (injection temperature = 2210°F; quench rate = 468°F/s; average residence time at reaction temperature = 1.3 s; Ca/S mole ratio = 2; 1900 ppm S02) found that sorbent SO2 capture reactivity varied in the order dolomitic hydrates > calcitic hydrates > carbonates (based on equal molar Ca/S ratios). However, for a given sorbent type there was no clear correlation between physical properties (BET surface area, mass mean particle size, elemental stoichiometry) and SO2 capture performance. A summary of their data is given in Table 1-1. Teixeira et al. [1986], testing sorbents for S02 removal from flue gases generated by burning low-sulfur Western coals (injection temperature = 2000°F; average residence time = 0.33 s; 500 ppm S02) also found that SO 2 capture reactivity varied in the order dolomitic hydrates > calcitic hydrates > carbonates. This observation w...