Document information
- University
- Politecnico di Milano
- Degree programme
- Energy Engineering
- Subject
- Energy Conversion A
- Classification
- Other study material
- Original format
- Text
- Searchable text
University study material for Energy Conversion A in the Energy Engineering degree programme at Politecnico di Milano. The document covers: COURSE OF ENERGY CONVERSION A 2014/2015 Prof. G. Valenti 3rd Project Analysis of diverse heat recovery steam cycles Consider a combined cycle with the same simple cycle gas turbine described in the second project. With the aid of the software package Turbogas, determine (i) the
University study material for Energy Conversion A in the Energy Engineering degree programme at Politecnico di Milano. The document covers: COURSE OF ENERGY CONVERSION A 2014/2015 Prof. G. Valenti 3rd Project Analysis of diverse heat recovery steam cycles Consider a combined cycle with the same simple cycle gas turbine described in the second project. With the aid of the software package Turbogas, determine (i) the
Import quality: text was extracted directly from the original document.
Representative passages recognised in different parts of the material. The full extracted text remains available to search, while this compact preview makes the page easier to read.
COURSE OF ENERGY CONVERSION A 2014/2015 Prof. G. Valenti 3rd Project Analysis of diverse heat recovery steam cycles Consider a combined cycle with the same simple cycle gas turbine described in the second project. With the aid of the software package Turbogas, determine (i) the air mass flow rate supplied to t he compressor, (ii) the turbine inlet temperature (TIT) and (iii) the compressor pressure ratio that ensure the most similar performance to those of the gas turbine engine of the second project. Examine the different obtainable performances of the following heat recovery steam cycles: a) one evaporation level b) two evaporation levels c) three evaporation levels with superheating of the high pressure steam Within the software Turbogas, consider the following calculation assumptions: case a: evaporation pressure equal to the optimised value of the previous project; case b: LP / HP pressures: 6.3 / 76 bar ; case c: LP / IP / HP pressures: 3 / 25 / 150 bar, with superheating pressure equal to the IP one; Use the following data for all the considered cases (a,b,c): Condensing pressure : 0.05 bar Tap : 25 C Deareator pressure : 2.0 bar Tsc : 10 C Tpp : 10 C p/peconomizzatore : 10 % Assume the software default values for all the other parameters that have not been specified. It is required to: 1) cases a,b,c : report in a table the efficiencies of cycle ( CV), thermal recovery (rec th), recovery(rec), second-law (II), as well as the steam cycle net power and the exhaust gas stack temperature; report in a table and compare the following entropy losses terms (referred to the reversible power of the exhaust gases that do not include the chemical exergy term): efficiency loss of the heat recovery steam generator (HRSG) and at the stack (stack); 2)…
First page of the document.