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    原位煤气化化学链燃烧发电系统的过程模拟

    Process Simulation of In-situ Coal Gasification Chemical Looping Combustion Power Generation System

    • 摘要: 运用Aspen Plus软件构建了以Fe2O3/FeO为氧载体的600 MW原位煤气化化学链燃烧发电系统。基于系统的仿真结果,分别进行了能量、㶲和㶲成本分析。结果表明:原位煤气化化学链燃烧发电系统的净热效率为35.38%;系统中内部㶲损失最大的组件为空气反应器,占原位煤气化化学链燃烧子系统组件总内部㶲损失的28.39%;水汽系统总内部㶲损失在整个系统中占比较小,仅为化学链燃烧子系统的14%;原位煤气化化学链燃烧发电系统中单位㶲成本最大的组件为空气预热器,其值为3.88,再热器、省煤器和过热器的产品单位㶲成本也较大。

       

      Abstract: A 600 MW in-situ coal gasification chemical looping combustion (iG-CLC) power generation system using Fe2O3/FeO as oxygen carrier was constructed by Aspen Plus software. Based on the simulation results of the system, the energy, exergy and exergy cost were analyzed respectively. Results show that the net thermal efficiency of iG-CLC power generation system is 35.38%. The component with the maximum internal exergy loss in the system is the air reactor, which accounts for 28.39% of the total exergy loss of iG-CLC subsystem components. Total internal exergy loss of the water vapor system is relatively small in the entire system, and is only 14% of the chemical looping combustion subsystem. The maximum unit exergy cost is 3.88 for air preheater in the iG-CLC power generation system, while the unit exergy costs of reheater, economizer and superheater are also larger.

       

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