2009
DOI: 10.1016/j.energy.2009.07.040
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A new approach for simplifying the calculation of flue gas specific heat and specific exergy value depending on fuel composition

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Cited by 59 publications
(29 citation statements)
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“…In industrial practice, the enthalpy graphic [11] and the enthalpy-temperature table [16] methods are widely used for the offline calculation of the specific enthalpy of the flue gas, which ignore the variant flue gas composition and are not suitable for online calculation. With respect to the density of the flue gas, the ideal gas equation of state is often utilized for engineering [10].…”
Section: Introductionmentioning
confidence: 99%
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“…In industrial practice, the enthalpy graphic [11] and the enthalpy-temperature table [16] methods are widely used for the offline calculation of the specific enthalpy of the flue gas, which ignore the variant flue gas composition and are not suitable for online calculation. With respect to the density of the flue gas, the ideal gas equation of state is often utilized for engineering [10].…”
Section: Introductionmentioning
confidence: 99%
“…The mass flow rate and the thermodynamic properties of the flue gas are dependent on its temperature, pressure, and composition [8,9]. According to the combustion theory, the composition of the flue gas is calculable with the data of offline ultimate analysis of the coal under certain excess air ratio [10,11]. However, such calculation is relatively complex and a high accuracy of the coal sample assay is a prerequisite which can rarely be met in real power plants.…”
Section: Introductionmentioning
confidence: 99%
“…Nitrogen reacts with oxygen to form NOx at about 1200℃ and above [15]. In this study, the upper limit of flue gas temperature is assumed as 11 0℃.…”
Section: Calculation Of Combustion Air Amountmentioning
confidence: 99%
“…o, nitrogen is not considered to react with oxygen during the combustion reaction. It limits the intimacy between the fuel molecules and oxygen [15]. Table 2 shows the ultimate analysis of the combustible fraction of MSW.…”
Section: Calculation Of Combustion Air Amountmentioning
confidence: 99%
“…Secondly, the temperature of the flue gas entering the filters should be between 80 • C and 140 • C. In the remainder of this work, only the flue gases are considered for waste heat recovery due to the very low temperature of the cooling loops and due to the high availability of heat at the flue gas side. The flue gas in this work has been modeled as air considering the high amount of excess air after combustion [45]. Large amounts of air infiltrate trough gaps in the furnace and before the post-combustion chamber.…”
Section: The Case Studymentioning
confidence: 99%