Continuous operation characteristics of chemical looping hydrogen production system

被引:72
作者
Cho, Won Chul [1 ,2 ]
Lee, Do Yeon [2 ]
Seo, Myung Won [3 ]
Kim, Sang Done [2 ]
Kang, KyoungSoo [1 ]
Bae, Ki Kwang [1 ]
Kim, Change Hee [1 ]
Jeong, SeongUk [1 ]
Park, Chu Sik [1 ]
机构
[1] Korea Inst Energy Res, Hydrogen & Fuel Cell Dept, Taejon 305343, South Korea
[2] Korea Adv Inst Sci & Technol, Dept Chem & Biomol Engn, Taejon 305701, South Korea
[3] Korea Inst Energy Res, Clean Fuel Dept, Taejon 305343, South Korea
关键词
Three-reactor chemical looping (TRCL); Hydrogen; CO2; separation; Iron oxide (Fe2O3); Redox reaction; IRON-OXIDE; OXYGEN CARRIERS; REDUCTION; KINETICS; FUEL; OXIDATION; CAPTURE; MODEL; BED;
D O I
10.1016/j.apenergy.2013.08.078
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Three-reactor chemical looping (TRCL) is a hydrogen and electricity production technology with inherent separation of carbon dioxide by use of the iron-based oxygen carrier particles. In this study, an integrated continuous operation test unit (300 W-th) using 20 wt% Fe2O3/ZrO(2)as an oxygen carrier was successfully operated over 13 h. The average CH4 conversion was 94.15% in a fuel reactor in a moving bed mode. Nearly pure hydrogen (99.95%) was obtained from a steam reactor (SR). The steam conversion to H-2 was around 63% of the thermodynamic limit in the SR. The hydrogen containing CO was observed from the SR when the carbon deposited particles were introduced into the SR. During the continuous operation, the oxygen carrier particles maintained its physical and chemical properties with high durability in the TRCL system. (C) 2013 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1667 / 1674
页数:8
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