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Figure 55 Mechanical power losses in the simulated ORC case 5.4 Power output vs. Cycle efficiency For ORC adapted to waste heat recovery the main goal is to produce the maximum power economically and efficiently using the available heat source as organic fluids are restricted to a small range of applicability depending on their thermodynamic conditions. This means that one organic fluid best suited for application for a temperature range, may not be so good for other temperature ranges. It is possible to have many organic fluids which satisfy the desirable characteristics at different temperature ranges. Figure 56 shows the complex relationship between net power output, heat absorbed and cycle efficiency. The net output increase with the increasing waste heat being absorbed (which is due to a larger evaporator sizes hence, increasing the temperature difference between the inlet and the outlet of the waste heat source) but decreases the corresponding cycle efficiency. Hence, considering a sequence of optimised cycles in which the heat increase in each case is related to the exit temperature of the waste heat source from the feed heater. It can be seen that beyond a certain point cycle efficiency must drop, even if the power output rises due to greater heat recovery. Therefore, an optimization process for the maximum cycle temperature is not required. However, it is important to notice that this maximum temperature would require an infinitely large vapour generator. The optimization procedure used above is based on the evaluation of the cycle efficiency, the specific net output and the UA. For the simulated case the results indicate that an 850 KW rated preheater & evaporator unit provides the best compromise conditions between cycle efficiency and the specific net power output. Further criteria are 91PDF Image | study of ORC with the expansion process twin screw machines
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