Experiments on biomass gasification using chemical looping with nickel-based oxygen carrier in a 25 kWth reactor

被引:105
作者
Ge Huijun [1 ]
Shen Laihong [1 ]
Feng Fei [1 ]
Jiang Shouxi [1 ]
机构
[1] Southeast Univ, Minist Educ, Key Lab Energy Thermal Convers & Control, Nanjing 210096, Jiangsu, Peoples R China
基金
中国国家自然科学基金;
关键词
Biomass gasification using chemical looping; Oxygen carrier; Nickel-based oxygen carrier; 25 kWth reactor; AIR-STEAM GASIFICATION; FLUIDIZED-BED; CO2; SEPARATION; COAL; COMBUSTION; REDUCTION; OXIDATION; KINETICS; HYDROGEN; SYNGAS;
D O I
10.1016/j.applthermaleng.2015.03.082
中图分类号
O414.1 [热力学];
学科分类号
摘要
Biomass gasification using chemical looping (BGCL) is an innovative biomass gasification technology, which utilizes lattice oxygen from oxygen carrier instead of molecular oxygen from air. This work attempted to investigate the BGCL performance with nickel-based oxygen carrier in a 25 kWth reactor. The new prototype is composed of a high velocity fluidized bed as an air reactor, a cyclone, a bubbling fluidized bed as a fuel reactor, and a loop-seal. At first, the major reactions in the process were presented and chemical reaction thermodynamics in the fuel reactor was analyzed. The NiO/Al2O3 oxygen carrier was then applied in the reactor. Different variables, such as gasification temperature, steam-to-biomass (S/B) ratio and NiO content, were analyzed. The carbon conversion efficiency increased smoothly within the temperature range of 650-850 degrees C, while the syngas yield reached the maximum of 0.33 Nm(3)kg(-1) at 750 degrees C. Additionally, based on the tradeoff between carbon conversion efficiency and syngas yield, it was concluded that 30 wt.% was the optimal NiO content. Besides, in order to get high quality syngas with low CO2 emission, CaO-decorated NiO/Al2O3 oxygen carrier was investigated. Experimental results showed that the addition of CaO enhanced the biomass gasification process and increased the syngas yield. (C) 2015 Elsevier Ltd. All rights reserved.
引用
收藏
页码:52 / 60
页数:9
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