Study of catalytic post-treatment of the vapours from sewage sludge pyrolysis by means of γ-Al2O3

被引:30
作者
Azuara, M. [1 ]
Fonts, I. [1 ,2 ]
Barcelona, P. [1 ]
Murillo, M. B. [1 ]
Gea, G. [1 ]
机构
[1] Univ Zaragoza, Aragon Inst Engn Res I3A, Thermochem Proc Res Grp GPT, E-50018 Zaragoza, Spain
[2] Ctr Univ Def Zaragoza, Zaragoza 50090, Spain
关键词
Pyrolysis; Sewage sludge; Gamma-alumina; Biomass; Catalytic treatment; FLUIDIZED-BED; OPERATIONAL CONDITIONS; BIOMASS PYROLYSIS; BIO-OIL; LIQUID; TEMPERATURE; FUELS; HYDROCARBONS; PRODUCTS; REACTOR;
D O I
10.1016/j.fuel.2013.02.017
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
The present work describes an experimental study on sewage sludge pyrolysis in a Fluidised Bed Reactor (FluBR) and the effect on the pyrolysis liquid product of passing the hot exhaust (pyrolysis) vapours through a Fixed Bed Reactor (FixBR) filled with gamma-alumina (gamma-Al2O3). Experiments have been done at temperatures of 450 and 550 degrees C (FluBR) and 400 and 500 degrees C (FixBR). In the FixBR experiments, the bed was filled with inert sand and two different bed quantities of gamma-Al2O3 (97.3 g, 194.6 g) giving a weight hour space velocity (WHSV) of between 0.6 and 1.8 h (-1). By means of this treatment, the pyrolysis liquid phase separation was improved, obtaining a liquid with two phases (organic and aqueous) instead of the three (two organic and an aqueous phase) usually obtained in sewage sludge pyrolysis without applying gamma-Al2O3. This organic phase is quite interesting from the point of view of a possible application as bio-oil. Although the product distribution results using gamma-Al2O3 show a slight liquid yield decrease for both temperatures (compared to sewage sludge pyrolysis without applying gamma-Al2O3), there is a clear increase in the organic phase yield at 450 degrees C. Therefore, gamma-Al2O3 application makes it possible to lower the pyrolysis temperature in order to maximise the organic phase in the sewage sludge pyrolysis liquid. Furthermore, a general improvement in the higher heating value of the organic phases has been achieved. (c) 2013 Elsevier Ltd. All rights reserved.
引用
收藏
页码:113 / 121
页数:9
相关论文
共 44 条
[1]   PRODUCTION OF HYDROCARBONS BY CATALYTIC UPGRADING OF A FAST PYROLYSIS BIO-OIL .1. CONVERSION OVER VARIOUS CATALYSTS [J].
ADJAYE, JD ;
BAKHSHI, NN .
FUEL PROCESSING TECHNOLOGY, 1995, 45 (03) :161-183
[2]  
Al-Senawi S, 2008, INT J CHEM REACT ENG, V6
[3]  
[Anonymous], 2002, DISP REC ROUT SEW SL
[4]   Evaluation of various types of Al-MCM-41 materials as catalysts in biomass pyrolysis for the production of bio-fuels and chemicals [J].
Antonakou, Eleni ;
Lappas, Angelos ;
Nilsen, Merete H. ;
Bouzga, Aud ;
Stocker, Michael .
FUEL, 2006, 85 (14-15) :2202-2212
[5]   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
[6]   Influence of temperature and alumina catalyst on pyrolysis of corncob [J].
Ates, Funda ;
Isikdag, M. Asli .
FUEL, 2009, 88 (10) :1991-1997
[7]  
Aznar M, 2007, INT J CHEM REACT ENG, V5
[8]  
Azuara M, 2010, P 18 EUR BIOM C EXH
[9]   Thermolytical treatment of dried sewage sludge and other biogenic materials - including upgrading of pyrolysis vapours by a cracking catalyst and examination of heavy metals by X-ray fluorescence [J].
Beckers, W ;
Schuller, D ;
Vaizert, O .
JOURNAL OF ANALYTICAL AND APPLIED PYROLYSIS, 1999, 50 (01) :17-30
[10]   Biomass pyrolysis/gasification for product gas production: the overall investigation of parametric effects [J].
Chen, G ;
Andries, J ;
Luo, Z ;
Spliethoff, H .
ENERGY CONVERSION AND MANAGEMENT, 2003, 44 (11) :1875-1884