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
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.
引用
收藏
页码:455 / 463
页数:9
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