Catalytic pyrolysis of rice husk by mixing with zinc oxide: Characterization of bio-oil and its rheological behavior

被引:110
作者
Zhou, Leiyu [1 ]
Yang, Hongmin [1 ]
Wu, Hao [1 ]
Wang, Meng [1 ]
Cheng, Daqian [1 ]
机构
[1] Nanjing Normal Univ, Sch Energy & Mech Engn, Nanjing 210042, Jiangsu, Peoples R China
基金
中国国家自然科学基金;
关键词
Biomass; Catalytic pyrolysis; Bio-oil's characterization; Rheological; BIOMASS FAST PYROLYSIS; TEMPERATURE; CONVERSION; FUELS; PARAMETERS; SAMPLES; CAKE;
D O I
10.1016/j.fuproc.2012.09.003
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
The experiments on the rice husk pyrolysis were performed in a fixed-bed reactor to produce bio-oil. The effects of the different operation factors such as pyrolysis temperature sweeping gas (N-2) flow rates and ZnO catalyst on the yields of three products and the characteristics of bio-oil were investigated. The maximum bio-oil yield of 49.91% was obtained at 550 degrees C pyrolysis temperature with a heating rate of 25 degrees C/min and nitrogen flow rate of 150 mL/min. The bio-oils yielded with and without a catalyst were characterized by FT-IR and GC/MS. The results showed that the main identified compounds of bio-oils were phenols, phenol derivatives and long-chain aliphatic compounds. It was observed that the use of catalyst decreased the bio-oil yields, but enhanced the small molecular compound yields and decreased the amount of oxygenated groups in bio-oils. A series of rheological tests were performed for the two kinds of bio-oil with cone and plate rheometer. The results indicated that both types of bio-oil were typical non-Newtonian and strongly shear thinning liquids in the flow behavior. The viscosity of the ZnO-treated bio-oil was significantly lower than that of the bio-oil without any catalyst. (c) 2012 Elsevier B.V. All rights reserved.
引用
收藏
页码:385 / 391
页数:7
相关论文
共 29 条
[1]   Evaluation of the role of the pyrolysis temperature in straw biomass samples and characterization of the oils by GUMS [J].
Ates, Funda ;
Isikdag, Muejde Asli .
ENERGY & FUELS, 2008, 22 (03) :1936-1943
[2]   Pyrolysis of two different biomass samples in a fixed-bed reactor combined with two different catalysts [J].
Ates, Funda ;
Putun, Ayse E. ;
Putun, Ersan .
FUEL, 2006, 85 (12-13) :1851-1859
[3]   Influence of temperature and alumina catalyst on pyrolysis of corncob [J].
Ates, Funda ;
Isikdag, M. Asli .
FUEL, 2009, 88 (10) :1991-1997
[4]   A techno-economic comparison of power production by biomass fast pyrolysis with gasification and combustion [J].
Bridgwater, AV ;
Toft, AJ ;
Brammer, JG .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2002, 6 (03) :181-248
[5]   Overview of applications of biomass fast pyrolysis oil [J].
Czernik, S ;
Bridgwater, AV .
ENERGY & FUELS, 2004, 18 (02) :590-598
[6]   The effects of different catalysts on the pyrolysis of industrial wastes (olive and hazelnut bagasse) [J].
Demiral, Ilknur ;
Sensoz, Sevgi .
BIORESOURCE TECHNOLOGY, 2008, 99 (17) :8002-8007
[7]   Effect of water vapor on the pyrolysis of the Moroccan (Tarfaya) oil shale [J].
El Harfi, K ;
Mokhlisse, A ;
Ben Chanâa, M .
JOURNAL OF ANALYTICAL AND APPLIED PYROLYSIS, 1999, 48 (02) :65-76
[8]   Historical developments in hydroprocessing bio-oils [J].
Elliott, Douglas C. .
ENERGY & FUELS, 2007, 21 (03) :1792-1815
[9]   SANS analysis of the microstructural evolution during the aging of pyrolysis oils from biomass [J].
Fratini, E ;
Bonini, M ;
Oasmaa, A ;
Solantausta, Y ;
Teixeira, J ;
Baglioni, P .
LANGMUIR, 2006, 22 (01) :306-312
[10]  
GAO P, 2006, IND CATAL, V14, P45