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because of recuperator price. These results illustrate that recuperator capability drives the cycle selection process. 4.5 4 3.5 3 2.5 2 1.5 1 0.5 0 Payback years for alternative recuperator technologies Alternative recuperator design concepts were also considered. The right-hand bar of Figure 1.2.6 reflects the projected price of a system employing a rotary recuperator (regenerator) that has the temperature capability of a Haynes 230 PSR, but the cost of a Type 347 device. Rotary recuperators were not favored for moderate pressure ratio (8:1) cycles because of the challenge to provide a reliable seal between the high-pressure and low-pressure gases within moving compartments. The analysis used to generate the results shown in Figure 1.2.6 assumed a 4% leak rate for the rotary recuperator and a 0% leak rate for the PSR. It is apparent that under these assumptions, the rotary device could be a viable candidate. 1.2.3 System Study Summary and Enabling Technologies As a consequence of these system analyses and conclusions, the desired AMS was a combination of an enhanced microturbine and an ORC that converted the exhaust into additional electrical power. The enhanced microturbine used ceramic turbine technology and modestly higher recuperator materials to permit a hotter, more efficient Brayton cycle. Improved generator/inverter components were assumed, but lean premixed combustion technology had to be adapted for the hotter cycle. Therefore, enabling technologies for: • ceramic turbines • low emission combustors • ORC systems were targeted for development and risk reduction in Task 2 of the program. Baseline Haynes 230 Inconel 625 Stainless Rotary Figure 1.2.6 19 Ceramic Turbine ST5 Turbine Ceramic Turbine Ceramic Turbine Advanced Metal Turbine Ceramic TurbinePDF Image | ADVANCED MICROTURBINE SYSTEMS Final Report for Tasks 1 Through 4 and Task 6
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