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硫碘热化学循环水分解制氢流程优化与模拟
引用本文:陈云,王书婕,王智化,林祥东,张彦威,周俊虎,岑可法.硫碘热化学循环水分解制氢流程优化与模拟[J].能源工程,2013(6):26-31,49.
作者姓名:陈云  王书婕  王智化  林祥东  张彦威  周俊虎  岑可法
作者单位:[1]浙江浙能北仑发电有限公司,浙江宁波315800 [2]浙江大学能源清洁利用国家重点实验室,浙江杭州310027
摘    要:选择大型化工流程模拟软件Aspen Plus对硫碘循环制氢系统进行流程优化设计与模拟,计算系统的质量平衡、能量平衡,并对系统热效率进行评估.碘化氢相中HI浓度采用本生反应实验中的过恒沸浓度,避免高能耗电渗析的使用,从而大大提高系统效率.在不考虑废热发电情况下,与文献值56.8%相比,系统产氢热效率高达68.46%.

关 键 词:制氢  热化学水分解制氢  硫碘循环  Aspen  Plus  热效率  超恒沸

Optimization design and stimulation of hydrogen production by sulfur-iodine thermo-chemical cycle process
Affiliation:CHEN Yun1 , WANG Shu-jie2, WANG Zhi-hua2, et al (1. Zhejiang Energy Beilun Power Generation Co., Ltd, Ningbo 315800, China; 2. State Key Laboratory of Clean Energy Utilization, Zhejiang University, Hangzhou 310027, China)
Abstract:A flowsheet of sulfuriodine (SI) thermochemical cycle for the hydrogen production was designed and simu lated by Aspen Plus. The heat and mass balance as well as thermal efficiency of SI process were calculated at fixed H2 production rate of 0. 348mol/s. To avoid the high energy consumption of EED, our experimental data in Bunsen reac tion was used as the HI concentration in HIx phase. Comparing with literature data 56.8% , thermal efficiency for hy drogen production is 68.46% without wasteheat power generation.
Keywords:hydrogen production  thermo-chemical water splitting  sulfur-iodine cycle  Aspen Plus  thermal efficien-cy  over-azeotropic HI concentration
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