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Coal conversion is dependent upon the reactor temperatures of each stage. The temperature coefficients of each stage are virtually the same; therefore, each is of equal importance. The interaction of the two stage temperatures is negative, which dampens the temperature effect of a single stage. According to the model, an increase in Temp1 and Temp2 from the lowest of the ranges (762 ¡ãF/679 ¡ãF) to the highest (834 ¡ãF/824 ¡ãF) would cause only a 4 wt % MAF increase in coal conversion. However, these specific combinations of reactor temperature have not been demonstrated at the pilot plant. In Figure 7, the first-stage temperature seems to be more significant. This is due to the interaction term with Temp2 and the fact that the average second stage temperature is higher that the first. The effect of 1/SpRate (nominal residence time) on coal conversion is small but significant. Much of the dissolution of Illinois No. 6 seam coal occurs in the initial time period. Thereafter, the conversion increase with longer residence time is only incremental, as observed in Figure 7. An increase in the process solvent resid (PSR) level causes only a minor increase in coal conversion, as shown in Figure 7. Over the entire range of PSR values (24-50 wt % MAF), the change in coal conversion is only _2 wt %. The hydrogen-donating properties of the residuum may help to prevent some retrogressive reactions and, thus, increase conversion of coal to cresolsolubles. Because of operability and pump ability problems, the PSR could not be increased beyond 50 wt %.
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