高温堆甲烷蒸汽重整制氢系统性能热力学分析  

Thermodynamic Analysis of Performance of Steam Methane Reforming Hydrogen Production System Connected With High-Temperature Gas-Cooled Reactor

作　　者：银华强[1] 姜胜耀[1] 张佑杰[1] 

机构地区：[1]清华大学核能与新能源技术研究院,北京100084

出　　处：《原子能科学技术》2006年第6期688-692,共5页Atomic Energy Science and Technology

基　　金：国家自然科学杰出青年基金(50325620);"跨世纪人才培养计划"基金

摘　　要：从热力学的角度分析高温堆甲烷蒸汽重整制氢系统的性能,为进一步研究实际的制氢系统提供框架。建立了完全反应模型和平衡反应模型,研究系统效率、产氢量随过程参数的变化关系,得到各性能指标的极限值以及过程参数的最优值。通过与实验数据的比较,采用平衡反应模型对系统进行初步分析是合适的。Thermodynamic analysis of performance of steam methane reforming hydrogen production system connected with High-Temperature Gas-Cooled Reactor is presented, which provides a framework for further detailed research. Complete reaction model and equilibrium reaction model were developed. System efficiency and hydrogen output variation related to process parameters were researched. Limit value of performance index and optimum process parameter were determined. The comparison of equilibrium reaction model prediction to experimental data shows that the equilibrium reaction model is appropriate for preliminarsy analysis for the system.

关 键 词：高温气冷堆 制氢 热力学 效率 

分 类 号：TL417[核科学技术—核技术及应用]