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Appendix A 3.3 Hybrid Heat Rejection For the purposes of the study, the following wet cooling tower duties in each 125 MWe plant have been selected for the hybrid tower designs: 2.5 in HgA: 130 MWt; 4 in. HgA: 80 MWt; 6 in. HgA: 45 MWt; and 8 in. HgA: 15 MWt. 3.4 Annual Performance Summary A plot of the net plant output (as a fraction of the wet tower plant output) as a function of the wet cooling tower water consumption (as a fraction of the water consumption of the wet cooling tower case) is shown in Figure 6. As might be expected, the largest incremental gains occur with the first water used; i.e., switching from a dry system to the 8 in. HgA hybrid system increases the net output by 8,300 kWhe per ton of water consumed. As the water consumption is increased, the performance improvements become smaller; i.e., switching from the 2.5 in. HgA hybrid system to the wet cooling tower increases the net output by only 5 kWhe per ton of water consumed. 1.00 0.99 0.98 0.97 0.96 0.95 0.94 4 in. HgA 6 in. HgA 8 in. HgA Dry 2.5 in. HgA Wet 0.0 0.1 Figure 6 Net Plant Output as a Function of Wet Cooling Tower Water Consumption 0.2 0.3 Fraction of wet cooling tower water consumption 0.9 1.0 0.4 0.5 0.6 0.7 0.8 x Fraction of wet cooling tower net plant outputPDF Image | Concentrating Solar Power Commercial Application
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