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
[21]   Effect of catalyst on yield of liquid products from biomass via pyrolysis [J].
Güllü, D .
ENERGY SOURCES, 2003, 25 (08) :753-765
[22]   On the pyrolysis of sewage sludge:: the influence of pyrolysis conditions on solid, liquid and gas fractions [J].
Inguanzo, M ;
Domínguez, A ;
Menéndez, JA ;
Blanco, CG ;
Pis, JJ .
JOURNAL OF ANALYTICAL AND APPLIED PYROLYSIS, 2002, 63 (01) :209-222
[23]   FLUIDIZED-BED PYROLYSIS OF DIGESTED SEWAGE-SLUDGE [J].
KAMINSKY, W ;
KUMMER, AB .
JOURNAL OF ANALYTICAL AND APPLIED PYROLYSIS, 1989, 16 (01) :27-35
[24]   Characterisation of products from pyrolysis of waste sludges [J].
Karayildirim, Tamer ;
Yanik, Jale ;
Yuksel, Mithat ;
Bockhorn, Henning .
FUEL, 2006, 85 (10-11) :1498-1508
[25]  
Kersten S. R. A., 2007, OPTIONS CATALYSIS TH
[26]   A technical and economic evaluation of the pyrolysis of sewage sludge for the production of bio-oil [J].
Kim, Y. ;
Parker, W. .
BIORESOURCE TECHNOLOGY, 2008, 99 (05) :1409-1416
[27]   FUELS AND CHEMICALS FROM SEWAGE-SLUDGE .3. HYDROCARBON LIQUIDS FROM THE CATALYTIC PYROLYSIS OF SEWAGE-SLUDGE LIPIDS OVER ACTIVATED ALUMINA [J].
KONAR, SK ;
BOOCOCK, DGB ;
MAO, V ;
LIU, JN .
FUEL, 1994, 73 (05) :642-646
[28]   Organic contaminants from sewage sludge applied to agricultural soils - False alarm regarding possible problems for food safety? [J].
Laturnus, Frank ;
von Arnold, Karin ;
Gron, Christian .
ENVIRONMENTAL SCIENCE AND POLLUTION RESEARCH, 2007, 14 (01) :53-60
[29]   Pyrolysis of triglyceride materials for the production of renewable fuels and chemicals [J].
Maher, K. D. ;
Bressler, D. C. .
BIORESOURCE TECHNOLOGY, 2007, 98 (12) :2351-2368
[30]   Pyrolysis of wood/biomass for bio-oil: A critical review [J].
Mohan, Dinesh ;
Pittman, Charles U., Jr. ;
Steele, Philip H. .
ENERGY & FUELS, 2006, 20 (03) :848-889