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两种不同再生方式下含碳能源直接制氢的比较
引用本文:乔春珍,肖云汉,徐祥,赵丽凤,田文栋.两种不同再生方式下含碳能源直接制氢的比较[J].中国电机工程学报,2006,26(18):95-100.
作者姓名:乔春珍  肖云汉  徐祥  赵丽凤  田文栋
作者单位:1. 中国科学院工程热物理研究所,北京市,海淀区,100080
2. 中国科学院研究生院,北京市,海淀区,100081
基金项目:国家863高技术基金项目(2003AA529260),国家重点基础研究发展规划基金项目(2003CB214502)。~~
摘    要:为了确定CO2吸收剂的不同再生方式对整个制氢过程的影响,根据含碳能源直接制氢的基本思路,构建了2种不同的制氢系统:碳部分转化(PCC)再生供热和化学链(氧化镍NO)反应供热。利用ASPENPlus软件,对2种不同再生方式下制氢系统的能量平衡和热平衡进行了热力学计算,分析系统的冷煤气效率,并对2种不同的再生方式对制氢过程中气体产物和固体产物组成的影响进行了初步分析。结果表明,相同的进料条件下,PCC过程中约68%的碳在气化炉中被气化时,系统可实现热平衡,此时冷煤气效率达0.74,而NO过程中只有51%的碳用于气化生成氢气,系统冷煤气效率只有0.67。即在该文的分析条件下,PCC过程更适合于为含碳能源直接制氢系统中的吸收剂再生供热。

关 键 词:含碳能源  制氢  二氧化碳吸收  再生  系统模拟
文章编号:0258-8013(2006)18-0095-06
收稿时间:2006-06-06
修稿时间:2006-06-06

Comparative Analysis of Hydrogen Production From Carbonaceous Energy Based on Two Different Absorbent Regeneration Modes
QIAO Chun-zhen,XIAO Yun-han,XU Xiang,ZHAO Li-feng,TIAN Wen-dong.Comparative Analysis of Hydrogen Production From Carbonaceous Energy Based on Two Different Absorbent Regeneration Modes[J].Proceedings of the CSEE,2006,26(18):95-100.
Authors:QIAO Chun-zhen  XIAO Yun-han  XU Xiang  ZHAO Li-feng  TIAN Wen-dong
Affiliation:1. Institute of Engineering Thermophysics of Chinese Academy of Sciences, Haidian District, Beijing 100080, China 2. Graduate University of Chinese Academy of Sciences, Haidian District, Beijing 100081, China
Abstract:In order to determine the effects of different absorbent regeneration modes on the process of hydrogen production, and based on the idea of directly-producing hydrogen from carbonaceous energy, two modes are suggested in this paper. One case is partial carbon conversion(PCC), and the remaining serves as a fuel for the regenerator, and the other is chemical reaction(nickel oxidation(NO))in the regenerator to supply heat for absorbent regeneration. ASPEN Plus was used to make thermodynamic calculation, and the mass and energy balances as well as cold gas efficiency were analyzed for two different processes. In the same feed condition, about 68% carbon was gasified in the gasification reactor and heat balances was achieved in the PCC process, and gives a higher cold gas efficiency of 0.74.While only 51% carbon was gasified in the NO process, and has a lower cold gas efficiency of 0.67.So in the operating condition of this paper, the PCC process is more feasible to the absorbent regeneration in the system of hydrogen production from carbonaceous energy.
Keywords:carbonaceous energy  hydrogen production  CO2 absorb  regeneration  system simulation
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