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Simulation and comparative exergy analyses of oxy-steam combustion and O-2/CO2 recycled combustion pulverized-coal-fired power plants

机译:氧蒸汽燃烧和O-2 / CO2循环燃烧煤粉电厂的模拟和比较火用分析

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摘要

Oxy-steam combustion is proposed as an alternative for the next generation oxy-fuel combustion technology. In order to justify the economic feasibility of this novel oxy-fuel combustion, a conventional 600 MWe pulverized-coal-fired power plant in China is selected to be retrofitted to oxy-steam combustion and O-2/CO2 recycled combustion separately, whilst the O-2/CO2 recycled combustion system serves as the base case for comparisons. The modeling and simulation of these two systems are carried out with Aspen Plus version 11.1. Simulation results indicate that on the same boundary conditions, the mass flow of the main steam and reheated steam in the oxy-steam combustion system must be reduced by 0.84%, which makes the net energy efficiency of the oxy-steam combustion system decrease by 0.15%. The comparative exergy analyses reveal that the net exergy efficiency of the oxy-steam combustion system is 0.153% lower than that of the O-2/CO2 recycled combustion system. The marked increase of the exergy destruction happening in the oxy-steam combustion furnace is the fundamental cause of the decrease of the exergy efficiency
机译:提出了氧气蒸汽燃烧作为下一代氧气燃料燃烧技术的替代方法。为了证明这种新型氧气燃料燃烧的经济可行性,选择了中国传统的600 MWe煤粉发电厂,分别改造为氧气蒸汽燃烧和O-2 / CO2循环燃烧,而O-2 / CO2循环燃烧系统是进行比较的基础。这两个系统的建模和仿真是使用Aspen Plus版本11.1进行的。仿真结果表明,在相同的边界条件下,氧气蒸汽燃烧系统中的主蒸汽和再热蒸汽的质量流量必须降低0.84%,这使得氧气蒸汽燃烧系统的净能量效率降低了0.15。 %。比较的火用分析表明,氧蒸汽燃烧系统的净火用效率比O-2 / CO2循环燃烧系统低0.153%。在氧气蒸汽燃烧炉中发生的火用破坏的明显增加是火用效率降低的根本原因

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