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Energy conversion analysis of hydrogen and electricity co-production coupled with in situ CO_2 capture

机译:氢气和电力联产的原位CO_2捕获的能量转换分析

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摘要

CO_2 adsorption enhanced gasification process is a prospective technology to be used in hydrogen and power production with nearly zero CO_2 emission. In this paper, a gasification kinetics steady state model is developed based on the chemical kinetics mechanism with the condition of fluidization. It is used to predict the parameters of gas phase and solid phase for a continuous flow reactor with steady state. The variation of distribution of components with gasification temperature and pressure are determined. Conceptual configurations of H_2 and power co-production system are designed with the integration of CO_2 adsorption enhanced gasification process, H_2 separation unit power generation unit and other auxiliary units. Mass and heat transfer between different parts are studied systematically by flow-sheet simulation and sensitivity analysis of parameters. According to the generalized exergy efficiency of the system, the influence of gasification temperature and pressure on the system performance is investigated and the optimum gasification temperature and pressure for system operation can be determined.
机译:CO_2吸附增强气化工艺是一种可用于制氢和发电且CO_2排放几乎为零的前瞻性技术。基于流化条件下的化学动力学机理,建立了气化动力学稳态模型。它用于预测稳态连续流反应器的气相和固相参数。确定了组分分布随气化温度和压力的变化。 H_2和动力联产系统的概念配置是通过整合CO_2吸附增强气化工艺,H_2分离单元发电单元和其他辅助单元而设计的。通过流程模拟和参数敏感性分析,系统地研究了不同零件之间的质量和热传递。根据系统的广义火用效率,研究了气化温度和压力对系统性能的影响,可以确定系统运行的最佳气化温度和压力。

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