Informazioni sul documento
- Università
- Politecnico di Milano
- Corso di laurea
- Energy Engineering
- Materia
- Energy Conversion A
- Classificazione
- Esercizi · Divisi per argomento
- Formato originale
- Testo
- Testo ricercabile
Divisi per argomento di Energy Conversion A per il corso di Energy Engineering presso Politecnico di Milano. Materiale proveniente dall’archivio storico Studwiz e classificato per la consultazione online.
Divisi per argomento di Energy Conversion A per il corso di Energy Engineering presso Politecnico di Milano. Materiale proveniente dall’archivio storico Studwiz e classificato per la consultazione online.
Qualità dell’importazione: il testo è stato estratto direttamente dal documento originale.
Passaggi rappresentativi riconosciuti nelle diverse parti del materiale. Il testo completo resta presente nella pagina per la ricerca, mentre l’anteprima compatta rende più semplice la lettura.
ENERGY CONVERSION A 2019-20 1 Exercises Second-law analysis of power cycles Exercise 1 Consider four different gas turbines operating with the following common conditions: • ambient temperature: 15 °C; • ambient pressure: 1.01325 bar; • compression pressure ratio: 40; • (total) turbine intel temperature (TIT): 1400 °C; • breathed air mass flow rate: 100 kg/s. The gas turbine differ by a localized pressure drop of 0.1 bar alternatively located at: 1. compressor suction; 2. compressor discharge; 3. turbine suction; 4. turbine discharge. Please, for all cases: i. plot a realistic cycle on the T-s diagram, for all alternative designs, highlighting the differences; ii. compute and compare the second-law efficiency losses due to only the pressure drop; iii. comment without computing how all other losses change from case to case. Note: the exercise could be setup as a single gas turbine operating in four off -design conditions (see off-design exercises). Exercise 2 Consider an air-cooled single-level combined cycle that features the following parameters: • (total) turbine outlet temperature (TOT) in combined cycle configuration: 600 °C; • exhaust gas mass flow rate: 200 kg/s; • steam cycle evaporation pressure: 35 bar (absolute); • evaporation enthalpy at 35 bar (absolute): 1750 kJ/kg; • evaporation temperature at 35 bar (absolute): 242 °C. Moreover, consider two extreme cases: 1. ΔT of subcooling between EVAP and ECO outlet of 20 °C; 2. ΔT of subcooling between EVAP and ECO outlet of 0 °C, employing a valve between them with a pressure loss, Δp, of 10 bar; Please: i. sketch the plant layouts; ii. plot the temperature-heat transfer (T-Q) diagram of the HRSG for the two cases on a single chart; iii. compute and compare the wasted power due to the following irreversibilities: o…
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