Termodynamiczny model elektrociepłowni gazowo-parowej

Artykuł opisuje dwa modele termodynamiczne elektrociepłowni EC-2 w Siedlcach wykorzystujący przemiany izentropowe i politropowe oraz model spalania gazu. Pokazano szczegółowy algorytm obliczeń prowadzonych w modelach. Porównano wyniki uzyskane z modeli z wynikami pomiarów uzyskując dobrą zgodność. Modele można wykorzystać do optymalizacji pracy elektrociepłowni gazowo–parowej pracującej na rynku energii.

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This article describes two thermodynamic models of plant EC-2 located in Siedlce. First model uses isentropic expansion, second- polytropic. The paper shows detailed calculation algorithm in models. Results obtained within models were compared with measurements. There were certain differences because of different places of calculations and available measurements. Relations between values were valid e.g. flue gas flow in combustion chamber computed by isentropic model was 81.5 kg/s, measured flue gas flow behind gas turbine was 88-94 kg/s (including additional cooling air flow, which was at second stage of turbine and was not included in calculations), assumed oxygen concentration 9% (=21%-12%) being involved in oxidation reaction in the combustion chamber is smaller than the measured concentration of 15%>12% in flue gases behind gas turbine. Results from models approximately show measurements. It seems that real transformation of CCGT thermodynamic system is between isentropic and polytropic process, because measurements are between results from models. It was shown that relatively simple models can be applied to modelling of gas-vapour cycle. Generated electrical power in both cycles agrees with measurements, computed gas flow in combustion chamber agrees too. It allows for applying that model in economic calculations answering e.g. questions about economic profitability of CHP.

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Opracowanie rekordu w ramach umowy 509/P-DUN/2018 ze środków MNiSW przeznaczonych na działalność upowszechniającą naukę (2018).