In situ catalytic conversion of tar using rice husk char/ash supported nickel-iron catalysts for biomass pyrolytic gasification combined with the mixing-simulation in fluidized-bed gasifier

被引:175
作者
Shen, Yafei [1 ]
Zhao, Peitao [2 ,3 ]
Shao, Qinfu [4 ]
Takahashi, Fumitake [1 ]
Yoshikawa, Kunio [1 ]
机构
[1] Tokyo Inst Technol, Interdisciplinary Grad Sch Sci & Engn, Dept Environm Sci & Technol, Yokohama, Kanagawa 2268502, Japan
[2] Southeast Univ, Sch Energy & Environm, Minist Educ, Key Lab Energy Thermal Convers & Control, Nanjing 210096, Jiangsu, Peoples R China
[3] China Univ Min & Technol, Sch Elect Power Engn, Xuzhou 221116, Peoples R China
[4] Univ Tokyo, Grad Sch Frontier Sci, Dept Environm Syst, Chiba 2778563, Japan
关键词
Biomass gasification; Tar conversion; Rice husk char; Catalysts; Mixing-simulation; CRACKING; GAS; NAPHTHALENE; REMOVAL; SYNGAS; ELIMINATION; COMBUSTION; CO; PERFORMANCE; REDUCTION;
D O I
10.1016/j.apenergy.2014.10.074
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
A catalytic gasification technology has been proposed for tar in situ conversion using the rice husk char (RHC) or rice husk ash (RHA) supported nickel-iron catalysts. Biomass tar could be converted effectively by co-pyrolysis with the RHC/RHA supported nickel-iron catalysts at 800 degrees C, simplifying the follow-up tar removal process. Under the optimized conditions, the tar conversion efficiency could reach about 923% by the RHC Ni-Fe, which exhibited more advantages of easy preparation and energy-saving. In addition, the tar conversion efficiency could reach about 93% by the RHA Ni. Significantly, partial metal oxides (e.g., MO, Fe2O3) in the carbon matrix of RHC could be in-situ carbothermally reduced into the metallic state (e.g., Ni-0) by reducing gases (e.g., CO) or carbon atom, thereby enhancing the catalytic performance of tar conversion. Furthermore, mixing with other solid particles such as sand and RHA Ni, can also improve biomass (e.g., RH) fluidization behavior by optimizing the operation parameters (e.g., particle size, mass fraction) in the mode of fluidized bed gasifier (FBG). After the solid-solid mixing simulation, the RH mass fraction of 0.5 and the particle diameter of 0.5 mm can be employed in the binary mixture of RH and RHA. (C) 2014 Elsevier Ltd. All rights reserved.
引用
收藏
页码:808 / 819
页数:12
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