ISSN: 2250-3005 - ijcer

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CP fgas [KJ/KgK]International Journal Of Computational Engineering Research (ijceronline.com) Vol. 2 Issue. 8Table 7: Results For Variation Of Flue Gas S pecific Heat With Furnace Temperature For Difference In Values OfExcess Air Ratio.CP fgas(KJ/KgK)n T fg(K)CP fgas(KJ/KgK)n T fg(K)CP fgas(KJ/KgK)n T fg(K)0.8460 1 700 0.7737 1.2 700 0.7128 1.4 7000.8989 1 1100 0.8220 1.2 1100 0.7573 1.4 11000.9491 1 1300 0.8679 1.2 1300 0.7996 1.4 13000.9976 1 1500 0.9123 1.2 1500 0.8405 1.4 15001.0450 1 1700 0.9558 1.2 1700 0.8806 1.4 17001.0920 1 1900 0.9987 1.2 1900 0.9201 1.4 19001.1390 1 2100 1.0410 1.2 2100 0.9593 1.4 21001.1850 1 2300 1.0840 1.2 2300 0.9984 1.4 23001.2310 1 2500 1.1260 1.2 2500 1.0370 1.4 25001.2780 1 2700 1.1690 1.2 2700 1.0770 1.4 27001.11.0510.95n=1n=1.2n=1.4n=1.6n=1.80.90.850.80.750.7750 1150 1550 1950 2350 2750T fg [K]Figure 5: Variation of flue gas specific heat with furnace temperature for difference in values of excess air ratio.Table 8: Results for Variation of flue gas specific exergy with furnace temperature for difference in values ofexcess air ratio.Ψ[KJ/Kg]n T fg(K)Ψ[KJ/Kg]n T fg(K)Ψ[KJ/Kg]n T fg(K)230.6 1 700 210.9 1.2 700 194.3 1.4 700371.1 1 1100 339.4 1.2 1100 312.6 1.4 1100534.4 1 1300 488.7 1.2 1300 450.2 1.4 1300718.7 1 1500 657.2 1.2 1500 605.5 1.4 1500923.0 1 1700 844.1 1.2 1700 777.6 1.4 17001147.0 1 1900 1049.0 1.2 1900 966.0 1.4 19001387.0 1 2100 1271.0 1.2 2100 1170.0 1.4 21001651.0 1 2300 1510.0 1.2 2300 1391.0 1.4 23001931.0 1 2500 1766.0 1.2 2500 1627.0 1.4 25002230.0 1 2700 2039.0 1.2 2700 1879.0 1.4 2700Issn 2250-3005(online) November| 2012 Page 17
International Journal Of Computational Engineering Research (ijceronline.com) Vol. 2 Issue. 820001600n=1n=1.2n=1.4n=1.6n=1.81200Ex[KJ/Kg-flue gas]8004000750 1150 1550 1950 2350 2750T fg [K]Figure 6: Variation of flue gas specific exergy with furnace temperature for difference in values of excess air ratio.4.3 Influence Of Moisture ContentWastes with different moisture contents have different drying characteristics. Those with higher moisture contentrequire a longer drying time and much more heat energy, causing a lower temperature in the furnace; and vice versa. If themoisture content is too high, the furnace temperature will be too low for combustion, such that auxiliary fuel is needed toraise the furnace temperature and to ensure normal combustion. In order to evaluate the effect of moisture content on thecombustion process, numerical simulation and analysis were made with ten different values of moisture content .Theresults of the analysis show that those wastes with a lower moisture content give rise to higher furnace temperatures andlarger high-temperature zones during combustion, because the wastes with lower moisture contents have higher heatingvalues and are more combustibles, being easier and faster to burn. Hence, to increase the efficiency of the boiler, refuseconditioner was used in this work to dry the wastes before they were conveyed to the furnace.Table 9: Result for variation of flue gas Temperature with moisture content for difference in value of excessoxygen.moisture Excess O 2(% )T fg(K)moistureExcessO 2(% )T fg(K)moistureExcessO 2(% )0.030 5 2206 0.030 25 1941 0.030 45 17400.050 5 2115 0.050 25 1862 0.050 45 16700.070 5 2024 0.070 25 1782 0.070 45 16000.090 5 1932 0.090 25 1702 0.090 45 15290.011 5 1839 0.011 25 1622 0.011 45 14580.013 5 1749 0.013 25 1541 0.013 45 13870.015 5 1651 0.015 25 1460 0.015 45 13150,017 5 1557 0.017 25 1370 0.017 45 12430.019 5 1461 0.019 25 1295 0.019 45 11710.021 5 1365 0.021 25 1213 0.021 45 1098T fg(K)Issn 2250-3005(online) November| 2012 Page 18
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ISSN: 2250-3005 - ijcer

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