Abstract:The main objective of this investigation is to obtain an optimum value for the flue gas recirculation ratio in a 620 MW-Natural Gas Combined Cycle (NGCC) power plant with a 100% excess air in order to have a composition of the exhaust gas suitable for an effective absorption by amine solutions. To reach this goal, the recirculated flue gas is added to the secondary air (dilution air) used for cooling the turbine. The originality of this work is that the optimum value of a Flue Gas Recirculation (FGR) ratio of … Show more
“…In the combustor (CC), combustion takes Figure 1. Schematic representation of natural gas combined cycle [14].…”
Section: Exergy Analysismentioning
confidence: 99%
“…As shown in Figure 3, a 620 MW-natural gas combined cycle (NGCC) with a flue gas recirculation ratio of 0.42 was simulated in the first part of this study [14]. A mass flowrate of 23.81 kg/s of natural gas, which consists of 93 mol% methane, is meant to be available in a battery limit of the plant at 3.1 MPa and 25˚C.…”
Section: Process Descriptionmentioning
confidence: 99%
“…In the combustion chamber, natural gas mixes with primary air and it is assumed complete combustion where all the carbon element of the natural gas is turned into carbon dioxide. Based on the first part of this investigation [14], the temperature of the combustion gases is 2100˚C. Secondary air is mixed with recirculated flue gas to reduce its temperature to 1300˚C before entering the turbine [14].…”
Section: Process Descriptionmentioning
confidence: 99%
“…Based on the first part of this investigation [14], the temperature of the combustion gases is 2100˚C. Secondary air is mixed with recirculated flue gas to reduce its temperature to 1300˚C before entering the turbine [14].…”
Section: Process Descriptionmentioning
confidence: 99%
“…A 620 MW-Natural Gas Combined Cycle (NGCC) power generation plant using 100% excess air was simulated in the first part of this investigation [14]. In Journal of Power and Energy Engineering order to have a composition of the exhaust gas suitable for an effective absorption by amine solutions, an optimum value of a Flue Gas Recirculation (FGR) ratio of 0.42 was calculated.…”
In the first part of this investigation, a Natural Gas Combined Cycle (NGCC) producing 620 MW of electricity was simulated using the commercial software Aspen Hysys V9.0 and the Soave-Redlich-Kwong (SRK) equation of state. The aim of this second part is to use exergy-based analyses in order to calculate its exergy efficiency and evaluate its environmental impact under standard conditions. For the exergy efficiency, the performance index under investigation is the exergy destruction ratio (y D ). The results of the study show that the combustor is the main contributor to the total exergy destruction of the power plant (y D = 24.35%) and has the lowest exergy efficiency of 75.65%. On the other hand, the Heat Recovery Steam Generator (HRSG) has the lowest contribution to the exergy destruction (y D = 5.63%) of the power plant and the highest exergy efficiency of 94.37%. For the overall power plant, the exergy efficiency is equal to 53.28%. For the environmental impact of the power plant, the relative difference of exergy-related environmental impacts (r b ) is utilized as the performance index for each equipment of the plant and the environmental impact of a kWh of electricity (EIE) is used to represent the performance index of the overall power plant. In agreement with the exergy analysis, the results indicate that the combustor and the HRSG have respectively the highest (r b = 32.19%) and the lowest (r b = 5.96%) contribution to the environmental impact. The environmental impact of a kWh of electricity of the power plant is 34.26 mPts/kWh (exergy destruction only), and 34.42 mPts/kWh (both exergy destruction and exergy loss).
“…In the combustor (CC), combustion takes Figure 1. Schematic representation of natural gas combined cycle [14].…”
Section: Exergy Analysismentioning
confidence: 99%
“…As shown in Figure 3, a 620 MW-natural gas combined cycle (NGCC) with a flue gas recirculation ratio of 0.42 was simulated in the first part of this study [14]. A mass flowrate of 23.81 kg/s of natural gas, which consists of 93 mol% methane, is meant to be available in a battery limit of the plant at 3.1 MPa and 25˚C.…”
Section: Process Descriptionmentioning
confidence: 99%
“…In the combustion chamber, natural gas mixes with primary air and it is assumed complete combustion where all the carbon element of the natural gas is turned into carbon dioxide. Based on the first part of this investigation [14], the temperature of the combustion gases is 2100˚C. Secondary air is mixed with recirculated flue gas to reduce its temperature to 1300˚C before entering the turbine [14].…”
Section: Process Descriptionmentioning
confidence: 99%
“…Based on the first part of this investigation [14], the temperature of the combustion gases is 2100˚C. Secondary air is mixed with recirculated flue gas to reduce its temperature to 1300˚C before entering the turbine [14].…”
Section: Process Descriptionmentioning
confidence: 99%
“…A 620 MW-Natural Gas Combined Cycle (NGCC) power generation plant using 100% excess air was simulated in the first part of this investigation [14]. In Journal of Power and Energy Engineering order to have a composition of the exhaust gas suitable for an effective absorption by amine solutions, an optimum value of a Flue Gas Recirculation (FGR) ratio of 0.42 was calculated.…”
In the first part of this investigation, a Natural Gas Combined Cycle (NGCC) producing 620 MW of electricity was simulated using the commercial software Aspen Hysys V9.0 and the Soave-Redlich-Kwong (SRK) equation of state. The aim of this second part is to use exergy-based analyses in order to calculate its exergy efficiency and evaluate its environmental impact under standard conditions. For the exergy efficiency, the performance index under investigation is the exergy destruction ratio (y D ). The results of the study show that the combustor is the main contributor to the total exergy destruction of the power plant (y D = 24.35%) and has the lowest exergy efficiency of 75.65%. On the other hand, the Heat Recovery Steam Generator (HRSG) has the lowest contribution to the exergy destruction (y D = 5.63%) of the power plant and the highest exergy efficiency of 94.37%. For the overall power plant, the exergy efficiency is equal to 53.28%. For the environmental impact of the power plant, the relative difference of exergy-related environmental impacts (r b ) is utilized as the performance index for each equipment of the plant and the environmental impact of a kWh of electricity (EIE) is used to represent the performance index of the overall power plant. In agreement with the exergy analysis, the results indicate that the combustor and the HRSG have respectively the highest (r b = 32.19%) and the lowest (r b = 5.96%) contribution to the environmental impact. The environmental impact of a kWh of electricity of the power plant is 34.26 mPts/kWh (exergy destruction only), and 34.42 mPts/kWh (both exergy destruction and exergy loss).
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