Characterisation of tars from biomass gasification: Effect of the operating conditions

被引:114
作者
Hernandez, J. J. [1 ]
Ballesteros, R. [1 ]
Aranda, G. [1 ]
机构
[1] Univ Castilla La Mancha, Escuela Tecn Super Ingn Ind, E-13071 Ciudad Real, Spain
关键词
Biomass gasification; Tar characterisation; Temperature; Relative fuel/air ratio; Steam content; FIXED-BED GASIFICATION; ENTRAINED FLOW GASIFIER; RICH GAS-PRODUCTION; STEAM GASIFICATION; CO-GASIFICATION; FLUIDIZED-BED; AIR; WASTES; TEMPERATURE; THERMODYNAMICS;
D O I
10.1016/j.energy.2012.12.005
中图分类号
O414.1 [热力学];
学科分类号
摘要
Tars formation remains the main technical hurdle in the development of biomass gasification at commercial scale, due to its associated operating problems (condensation, catalyst deactivation, polymerisation). This work aims to study the effect of the operating conditions (biomass/air ratio, temperature and gasifying agent) on the production and the technical and environmental hazard (tar dew point and carcinogenic potential) of tars produced in a small-scale drop-tube gasifier, dealcoholised marc of grape being used as biomass fuel. An analytical HPLC method has been used for the detection of polycyclic aromatic hydrocarbons (PAHs), benzene, toluene, ethyl-benzene and xylenes (BTEX), phenol, and pyridine. Results show that an increase in the relative biomass/air ratio, a decrease in temperature, and higher steam content lead to a higher tar production. BTEX have been found as the main constituents of tars (60-70% wt.), whereas among PAHs, the most significant are the lighter ones (naphthalene, acenaphtylene, acenaphtene). Phenol production is favoured at lower temperatures or/and higher steam content (around 50% wt. of the tar mixture at 750 degrees C and steam gasification). A progressive aromatisation of tars has been observed when increasing the temperature, the effect of steam addition on tar composition being not significant at temperatures higher than similar to 1000 degrees C. (C) 2012 Elsevier Ltd. All rights reserved.
引用
收藏
页码:333 / 342
页数:10
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