Catalytic steam reforming of biomass tar: Prospects and challenges

被引:507
作者
Guan, Guoqing [1 ]
Kaewpanha, Malinee [2 ]
Hao, Xiaogang [3 ]
Abudula, Abuliti [1 ]
机构
[1] Hirosaki Univ, NJRISE, 2-1-3 Matsubara, Aomori 0300813, Japan
[2] Hirosaki Univ, Grad Sch Sci & Technol, 1 Bunkyocho, Hirosaki, Aomori 0368560, Japan
[3] Taiyuan Univ Technol, Dept Chem Engn, Taiyuan 030024, Peoples R China
基金
日本科学技术振兴机构;
关键词
Biomass; Tar; Gasification; Catalyst; Steam reforming; Activity; Stability; HYDROGEN-RICH GAS; BED REACTOR INFLUENCE; CO-GASIFICATION; SYNGAS PRODUCTION; MODEL TAR; LIGNOCELLULOSIC BIOMASS; OPERATING-CONDITIONS; OLIVINE CATALYSTS; FAST PYROLYSIS; NI CATALYSTS;
D O I
10.1016/j.rser.2015.12.316
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Tar is unavoidable by-product during biomass gasification process. Catalytic steam reforming of tar to syngas is a promising way for the removal of tar from the gas products. However, the key issue for this way is catalyst development. To date, the developed catalysts always have advantages and disadvantages: nickel-based catalysts have high activity, but they are easily deactivated by coking; noble metal based catalysts have high catalytic activity, long-term stability and high carbon deposition resistance, but they are expensive; other transition metal catalysts such as Fe, Co and Cu exhibit a good performance, but they are also deactivated easily by carbon deposition in the case of high heavy-tar content in the tar; alkali metal catalysts also have high catalytic activity for tar reforming, but they are easy to be evaporated with the generated gases; natural catalysts have been widely applied for the steam reforming of tar due to its inexpensive, abundant and disposable, but their catalytic activities are lower than those man-made ones, and especially have low mechanical strength, making them not suitable to be used in fluidized bed reactor; zeolite is suggested to be a good catalyst support due to its high thermal/hydrothermal stability, high resistance to sulfur compounds, and easy to be regenerated; biomass char has been used as the catalyst or catalyst support in the steam reforming of tar due to its low cost and its natural production inside the biomass gasifier; even biomass ash now is considered to be a good catalyst for tar removal. In this review, to get better understanding of the mechanism of catalytic steam reforming of tar derived from biomass, tar formation, tar properties and catalytic reaction mechanism are also introduced, and prospects and challenges are summarized. (C) 2016 Elsevier Ltd. All rights reserved.
引用
收藏
页码:450 / 461
页数:12
相关论文
共 121 条
[71]   Catalytic steam gasification of Miscanthus X giganteus in fluidised bed reactor on olivine based catalysts [J].
Michel, Rudy ;
Rapagna, Sergio ;
Di Marcello, Manuela ;
Burg, Philippe ;
Matt, Muriel ;
Courson, Claire ;
Gruber, Rene .
FUEL PROCESSING TECHNOLOGY, 2011, 92 (06) :1169-1177
[72]   Catalytic reforming of tar during gasification. Part II. Char as a catalyst or as a catalyst support for tar reforming [J].
Min, Zhenhua ;
Yimsiri, Piyachat ;
Asadullah, Mohammad ;
Zhang, Shu ;
Li, Chun-Zhu .
FUEL, 2011, 90 (07) :2545-2552
[73]   Catalytic reforming of tar during gasification. Part I. Steam reforming of biomass tar using ilmenite as a catalyst [J].
Min, Zhenhua ;
Asadullah, Mohammad ;
Yimsiri, Piyachat ;
Zhang, Shu ;
Wu, Hongwei ;
Li, Chun-Zhu .
FUEL, 2011, 90 (05) :1847-1854
[74]   Gasification of woody biomass char with CO2: The catalytic effects of K and Ca species on char gasification reactivity [J].
Mitsuoka, Keiichirou ;
Hayashi, Shigeya ;
Amano, Hiroshi ;
Kayahara, Kenji ;
Sasaoaka, Eiji ;
Uddin, Md Azhar .
FUEL PROCESSING TECHNOLOGY, 2011, 92 (01) :26-31
[75]   Catalytic performance of supported Ni catalysts in partial oxidation and steam reforming of tar derived from the pyrolysis of wood biomass [J].
Miyazawa, Tomohisa ;
Kimura, Takeo ;
Nishikawa, Jin ;
Kado, Shigeru ;
Kunimori, Kimio ;
Tomishige, Keiichi .
CATALYSIS TODAY, 2006, 115 (1-4) :254-262
[76]   Catalytic tar decomposition of biomass pyrolysis gas with a combination of dolomite and silica [J].
Myrén, C ;
Hörnell, C ;
Björnbom, E ;
Sjöström, K .
BIOMASS & BIOENERGY, 2002, 23 (03) :217-227
[77]   Gasification of biomass and waste in a staged fluidized bed gasifier: Modeling and comparison with one-stage units [J].
Nilsson, Susanna ;
Gomez-Barea, Alberto ;
Fuentes-Cano, Diego ;
Ollero, Pedro .
FUEL, 2012, 97 :730-740
[78]   Steam reforming of naphthalene as model biomass tar over iron-aluminum and iron-zirconium oxide catalyst catalysts [J].
Noichi, Hiroyuki ;
Uddin, Azhar ;
Sasaoka, Eiji .
FUEL PROCESSING TECHNOLOGY, 2010, 91 (11) :1609-1616
[79]   Modelling of tar formation and evolution for biomass gasification: A review [J].
Palma, Carolina Font .
APPLIED ENERGY, 2013, 111 :129-141
[80]   Steam reforming of biomass gasification tar using benzene as a model compound over various Ni supported metal oxide catalysts [J].
Park, Hyun Ju ;
Park, Sung Hoon ;
Sohn, Jung Min ;
Park, Junhong ;
Jeon, Jong-Ki ;
Kim, Seung-Soo ;
Park, Young-Kwon .
BIORESOURCE TECHNOLOGY, 2010, 101 :S101-S103