YIN Hua-qiang, JIANG Sheng-yao, ZHANG You-jie. Numerical Analysis of Performance of Steam Reformer of Methane Reforming Hydrogen Production System Connected With High-Temperature Gas-Cooled Reactor[J]. Atomic Energy Science and Technology, 2007, 41(1): 69-73. DOI: 10.7538/yzk.2007.41.01.0069
Citation: YIN Hua-qiang, JIANG Sheng-yao, ZHANG You-jie. Numerical Analysis of Performance of Steam Reformer of Methane Reforming Hydrogen Production System Connected With High-Temperature Gas-Cooled Reactor[J]. Atomic Energy Science and Technology, 2007, 41(1): 69-73. DOI: 10.7538/yzk.2007.41.01.0069

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

  • Methane conversion rate and hydrogen output are important performance indexes of the steam reformer. The paper presents numerical analysis of performance of the reformer connected with high-temperature gas-cooled reactor HTR-10. Setting helium inlet flow rate fixed, performance of the reformer was examined with different helium inlet temperature, pressure, different process gas temperature, pressure, flow rate, and different steam to carbon ratio. As the range concerned, helium inlet temperature has remarkable influence on the performance, and helium inlet temperature, process gas temperature and pressure have little influence on the performance, and improving process gas flow rate, methane conversion rate decreases and hydrogen output increases, however improving steam to carbon ratio has reverse influence on the performance.
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