Catalytic steam reforming of biomass over Ni-based catalysts: Conversion from poplar leaves to hydrogen-rich syngas

被引:13
|
作者
Cao, Lingyan [1 ]
Jia, Zhigang [1 ]
Ji, Shengfu [1 ]
Hu, Jinyong [1 ]
机构
[1] Beijing Univ Chem Technol, State Key Lab Chem Resource Engn, Beijing 100029, Peoples R China
来源
JOURNAL OF NATURAL GAS CHEMISTRY | 2011年 / 20卷 / 04期
关键词
biomass; steam reforming; hydrogen-rich syngas; Ni-basic catalyst; CaO; FUEL GAS-PRODUCTION; SBA-15; CATALYSTS; WOODY BIOMASS; CO2; SORBENT; GASIFICATION; CAO; PROMOTER; METHANE;
D O I
10.1016/S1003-9953(10)60195-8
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
A series of Ni/SBA-15 catalysts with Ni contents from 5 wt%-20 wt% and CaO-12.5%Ni/SBA-15 catalysts with CaO contents from 1.4 wt%-9.8 wt% have been prepared. The structure of the catalysts was characterized using X-ray diffraction (XRD), N-2 adsorption-desorption, transmission electron microscopy (TEM) and X-ray photoelectron spectroscopy (XPS). The performance of catalytic steam reforming of the poplar leaves to the hydrogen-rich syngas was tested in a fixed-bed reactor. The results indicate that the 7.0wt%CaO-12.5wt%Ni/SBA-15 catalyst exhibits the best performance for the catalytic steam reforming of poplar leaves to hydrogen-rich syngas. The ratio of H-2 : CO can reach ca 5 : 1 in the hydrogen-rich syngas. The yield of H-2 can reach 273.30 mL/g (poplar leaves). In the CaO-Ni/SBA-15 catalyst, Ni active component mainly fills the role of catalytic steam reforming of the poplar leaves, and CaO active component mainly plays the role as water-gas shift and CO2 sorbent.
引用
收藏
页码:377 / 383
页数:7
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