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Advantages of confining the fountain in a conical spouted bed reactor for biomass steam gasification
被引:60
作者:
Cortazar, M.
[1
]
Lopez, G.
[1
]
Alvarez, J.
[1
]
Amutio, M.
[1
]
Bilbao, J.
[1
]
Olazar, M.
[1
]
机构:
[1] Univ Basque Country, Dept Chem Engn, POB 64, E-48080 Bilbao, Spain
来源:
关键词:
Conical spouted bed;
Biomass gasification;
Tar;
Syngas;
Hydrogen;
HYDROGEN-RICH GAS;
BUBBLING FLUIDIZED-BED;
LIGNOCELLULOSIC BIOMASS;
FAST PYROLYSIS;
SEWAGE-SLUDGE;
PILOT-PLANT;
DOWNDRAFT GASIFIERS;
SCALE GASIFICATION;
WASTE BIOMASS;
CORN STOVER;
D O I:
10.1016/j.energy.2018.04.067
中图分类号:
O414.1 [热力学];
学科分类号:
摘要:
A study was carried out on the advantages of inserting a fountain confiner in conical spouted beds for biomass steam gasification and the results (gas yield and composition, tar content, carbon conversion efficiency and H-2 production) are compared with those obtained under conventional spouting regime. The experiments were carried out in a bench scale unit operating in continuous regime under the same gasification conditions in all the configurations (850 degrees C, S/B ratio of 2 and olivine as primary catalyst). The gaseous product was analyzed by on-line gas chromatography and micro-gas chromatography, and the tars by gas chromatography-mass spectrometry. The use of a fountain confiner allows enhancing process versatility, increasing gas velocity over the minimum spouting one, increasing the fountain height and reducing olivine particle size (enhanced fountain regime). Thus, as a result of a better gas-solid contact, tar content was reduced from 49.2 g Nm(-3) without fountain confiner to 20.6 g Nm(-3) under enhanced fountain regime, with the reduction of heavy PAHs being especially remarkable. In the same line, a great improvement in process conversion efficiency was attained under the enhanced fountain regime, with gas production reaching a value of 1.3 m(3) kg(-1) and that of H-2 production 5.0 wt%. (C) 2018 Elsevier Ltd. All rights reserved.
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页码:455 / 463
页数:9
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