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OCTOBER 19-20, 2012 - YMCA University of Science & Technology

OCTOBER 19-20, 2012 - YMCA University of Science & Technology

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Proceedings <strong>of</strong> the National Conference on<br />

Trends and Advances in Mechanical Engineering,<br />

<strong>YMCA</strong> <strong>University</strong> <strong>of</strong> <strong>Science</strong> & <strong>Technology</strong>, Faridabad, Haryana, Oct <strong>19</strong>-<strong>20</strong>, <strong>20</strong>12<br />

Compression ratio <strong>of</strong> compressor also affects the mass <strong>of</strong> fuel to be injected in combustion chamber but in an<br />

irregular fashion. Upto a pressure ratio <strong>of</strong> 15 there is decrease in fuel consumption and after that it starts<br />

increasing. Similar pattern is observed for the exergy destruction in combustion chamber.<br />

Mass <strong>of</strong> fuel injected in combustion<br />

chamber (g/Kg <strong>of</strong> air)<br />

1.8<br />

1.75<br />

1.7<br />

1.65<br />

1.6<br />

1.55<br />

1.5<br />

5 10 15 <strong>20</strong> 25 26<br />

Cycle pressure ratio<br />

Figure: 4. Fuel consumption in combustion chamber with change in CR<br />

As the turbine inlet temperature increases, exergy destruction in combustion chamber decreases (figure.5). It is<br />

due to the reason that, increase in temperature inside the combustion chamber increases the fuel utilization<br />

efficiency. Due to increased fuel utilization efficiency, exergy destruction in combustion chamber is decreased.<br />

With increase in TIT from 900°C to 1300°C, exergy destruction is decreased by 6.22%.<br />

Exergy destruction in combustion<br />

chamber<br />

27000<br />

26500<br />

26000<br />

25500<br />

25000<br />

24500<br />

24000<br />

900 950 1000 1050 1100 1150 1<strong>20</strong>0 1250 1300<br />

Turbine inlet temperature (°C)<br />

Figure: 5. Exergy destruction in combustion chamber with change in turbine inlet temperature (°C)<br />

If heat is transferred from a high temperature to lower temperature then its quality goes down and exergy<br />

destruction takes place. Exergy (or available energy, or availability) is the maximum useful work that can be<br />

extracted from a quantity <strong>of</strong> energy and refers to the quality <strong>of</strong> energy. Thus, though the energy is conserved in<br />

the process <strong>of</strong> conversion, its quality deteriorates and less work can be obtained with each conversion. The<br />

various irreversible processes encountered within the combustor leads to certain degree <strong>of</strong> exergy loss. It is<br />

observed that the second-law efficiency is the maximum for the stoichiometric supply <strong>of</strong> air. The lower product<br />

gas temperature at the exit for a lean mixture as a result <strong>of</strong> the excess air supply reduces the second-law<br />

efficiency <strong>of</strong> the combustor. This is despite the fact that all the energy stored in the fuel is contained in the<br />

product gas with the complete combustion <strong>of</strong> the fuel in case <strong>of</strong> a lean fuel–air mixture in the adiabatic<br />

combustor. Therefore, it is clear that neither the completeness <strong>of</strong> combustion nor the energy content <strong>of</strong> the<br />

product gas determines the exergy-based performance <strong>of</strong> the combustor. As the product gas temperature at the<br />

combustor exit decreases with the increase in the excess supply <strong>of</strong> air, the maximum ability <strong>of</strong> it to perform<br />

useful work decreases. Therefore, the second-law efficiency decreases. The same decrease in exergetic efficiency<br />

is also observed with the insufficient supply <strong>of</strong> air, when the exit temperature decreases because <strong>of</strong> the<br />

incomplete release <strong>of</strong> fuel’s stored energy. The maximum efficiency, which is obtained with the stoichiometric<br />

185

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