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Keyword: steam re-heating

  • MACHINES

    Energy analysis of a steam turbine with two cylinders and steam re-heating

    • Mrzljak Vedran
    • Prpić-Oršić Jasna
    • Medica-Viola Vedran
    • Poljak Igor
    Machines. Technologies. Materials., Vol. 16 (2022), Issue 5, pg(s) 155-158
    • Abstract
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    This paper presents an energy analysis of middle-power steam turbine with two cylinders (High Pressure Cylinder – HPC and Low Pressure Cylinder – LPC) and steam re-heater after the HPC (and before the LPC). Based on a steam operating parameters from the literature, performed energy analysis show that LPC develops higher power and has higher energy efficiency (81.45%) in comparison to HPC (which energy efficiency equals 80.12%). Re-heater is a heat exchanger (flue gases are used for steam heating) which has low energy loss (824.19 kW) and high energy efficiency (97.76%), what is expected energy performance of such heat exchanger. The entire analyzed turbine develops a power of 127480.60 kW and has energy loss equal to 29848.21 kW with energy efficiency of 81.03%.

  • Thermodynamical analysis of heat exchange and fuel consumption in marine re-heat steam generator

    • Mrzljak Vedran
    • Poljak Igor
    • Orović Josip
    • Prpić-Oršić Jasna
    Trans Motauto World, Vol. 4 (2019), Issue 1, pg(s) 40-43
    • Abstract
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    The paper presents analysis of heat exchange and fuel consumption in the entire Marine Steam Generator (MSG) with steam reheating and in all of its components. Analysis is performed by using operating parameters from the steam generator exploitation. The highest heat amount transferred from combustion gases is used in the evaporator (48.17 % of the cumulative heat amount transferred in MSG). Proportionally, evaporator uses the highest fuel mass flow of 0.5172 kg/s when compared to other MSG components. In the high-pressure pipeline heat losses amounts 82.64 kW. Cumulative heat transferred from combustion gases to water/steam in all MSG components amounts 42048.47 kW. Cumulative water/steam specific entropy and temperature increase in the entire MSG is 4.5677 kJ/kg·K and 454.18 K, while the fuel mass flow in the entire MSG is equal to 1.0736 kg/s.

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