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Second Law Results: Input exergy (fuel): 150 BTU/sec Thermodynamic Process Net electrical exergy output: 44.5 BTU/sec Net thermal exergy output: 24.5 BTU/sec 1>2 2>3 3>4,6>7 4+11>5 5>6 9>10 7>8,12>13 10>11 Generator Air Compressor Recuperator Combustor Turbine Gas Compressor Heat Recovery Unit Gas Throttle Exergy Transport BTU/sec 49.3 86.6 17 150.4 4.7 24.5 Exergy Destruction BTU/sec 1.5 3.6 4.7 58 6.4 0 23.7 0.2 Cycle 2nd Law efficiency, electric: 30% Cycle 2nd Law efficiency, combined: 46% Total Exergy Destruction: 98.1 BTU/sec Economic Modeling The goal here is to determine under what conditions microturbine operation results in cost savings for the building owner, the City of Milwaukee. The cost of microturbine operation must be compared to the purchase of electricity and purchase of natural gas for the building’s hot water boilers. Rates for natural gas and electricity will vary with time of year, and may vary with time of day. Development of a model is underway that will take real-time data on building loads and rates for electricity and gas and determine a point at which the microturbine should be dispatched. The model should be capable of displaying the net benefit, or cost, of microturbine operation under different operating scenarios. Proceedings of the 2004 American Society of Engineering Education Annual Conference & Exposition Copyright © 2004, American Society for Engineering EducationPDF Image | A 60-kW Microturbine Demonstration Facility Phase II: Instrumentation, Website Development, and Evaluation
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