In-situ steam reforming of biomass tar over sawdust biochar in mild catalytic temperature

被引:43
作者
Feng, Dongdong [1 ]
Zhao, Yijun [1 ]
Zhang, Yu [1 ,2 ]
Zhang, Zhibo [1 ]
Zhang, Linyao [1 ]
Sun, Shaozeng [1 ]
机构
[1] Harbin Inst Technol, Sch Energy Sci & Engn, Harbin 150001, Heilongjiang, Peoples R China
[2] Univ Nottingham, Fac Engn, Nottingham NG7 2TU, England
关键词
In-situ; Mild temperature; Tar reforming; Steam; Biomass tar; Sawdust biochar; VICTORIAN BROWN-COAL; VOLATILE-CHAR INTERACTIONS; SUPPORTED IRON CATALYST; FLUIDIZED-BED; GASIFICATION PROCESSES; FOURIER-TRANSFORM; NASCENT TAR; RICE HUSK; PYROLYSIS; ELIMINATION;
D O I
10.1016/j.biombioe.2017.10.007
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
In order to fully understand the catalytic activities of sawdust biochar on in-situ tar steam reforming in mild catalysis temperatures (650-800 degrees C), the experiment was carried out in a two-stage fluidized bed/fixed bed reactor. The structural characteristics of biochar were analyzed by the Raman and XPS spectroscopies. The results of in-situ tar steam reforming over biochar were performed by gas chromatograph/mass spectrometer (GC/MS). Kinetic aspects of tar steam reforming in mild temperatures were calculated to evaluate the catalytic effect of sawdust biochar on in-situ tar reforming. The results indicate that sawdust biochar has a positive effect on in-situ tar steam reforming, while the effect is not proportional to biochar amount. During the in-situ tar steam reforming over biochar, the changes of oxygen-containing functional groups on biochar surface are mainly caused by the C-O bonds. The first order kinetic rate constant of sawdust biochar for the heterogeneous reforming of biomass tar at 650-800 degrees C is found to have an apparent activation energy (Eapp) of 35.03 kJ/mol with the apparent pre-exponential factor (k(app)) of 1.8 x 10(4) m(3) kg(-1)h(-1). The biochar structures were considerably transformed during the tar steam reforming. According to GC/MS analysis of biomass tar, the biochar seems to promote the cracking of large ring polyaromatic tar compounds to form 1-ring aromatic ones.
引用
收藏
页码:261 / 270
页数:10
相关论文
共 73 条
[1]   Review of catalysts for tar elimination in Biomass gasification processes [J].
Abu El-Rub, Z ;
Bramer, EA ;
Brem, G .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2004, 43 (22) :6911-6919
[2]   Rh-perovskite catalysts for conversion of tar from biomass pyrolysis [J].
Ammendola, P. ;
Lisi, L. ;
Piriou, B. ;
Ruoppolo, G. .
CHEMICAL ENGINEERING JOURNAL, 2009, 154 (1-3) :361-368
[3]   Effects of biomass char structure on its gasification reactivity [J].
Asadullah, Mohammad ;
Zhang, Shu ;
Min, Zhenhua ;
Yimsiri, Piyachat ;
Li, Chun-Zhu .
BIORESOURCE TECHNOLOGY, 2010, 101 (20) :7935-7943
[4]   Hydrogen from biomass - Present scenario and future prospects [J].
Balat, Havva ;
Kirtay, Elif .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2010, 35 (14) :7416-7426
[5]   Inhibition of steam gasification of char by volatiles in a fluidized bed under continuous feeding of a brown coal [J].
Bayarsaikhan, B ;
Sonoyama, N ;
Hosokai, S ;
Shimada, T ;
Hayashi, J ;
Li, CZ ;
Chiba, T .
FUEL, 2006, 85 (03) :340-349
[6]   Characteristics of evolution of tar from wood pyrolysis in a fixed-bed reactor [J].
Brage, C ;
Yu, QH ;
Sjostrom, K .
FUEL, 1996, 75 (02) :213-219
[7]   Steam reforming of gasification-derived tar for syngas production [J].
Chang, Alex C. -C. ;
Chang, Lung-Shiang ;
Tsai, Cheng-You ;
Chan, Yu-Chun .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2014, 39 (33) :19376-19381
[8]   THE ACTIVE SURFACE SPECIES IN ALKALI-CATALYZED CARBON GASIFICATION - PHENOLATE (C-O-M) GROUPS VS CLUSTERS (PARTICLES) [J].
CHEN, SG ;
YANG, RT .
JOURNAL OF CATALYSIS, 1993, 141 (01) :102-113
[9]   Experimental Investigation on Tar Formation and Destruction in a Lab-Scale Two-Stage Reactor [J].
Chen, Yi ;
Luo, Yong-hao ;
Wu, Wen-guang ;
Su, Yi .
ENERGY & FUELS, 2009, 23 (09) :4659-4667
[10]   Two advanced models for the kinetics of the variation of the tar composition in its catalytic elimination in biomass gasification [J].
Corella, J ;
Caballero, MA ;
Aznar, MP ;
Brage, C .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2003, 42 (13) :3001-3011