Co-Gasification of Biomass Wastes and Coal Coke Blends in an Entrained Flow Gasifier: An Experimental Study

被引:97
作者
Hernandez, Juan J. [1 ]
Aranda-Almansa, Guadalupe [1 ]
Serrano, Clara [2 ]
机构
[1] Univ Castilla La Mancha, Dept Mecan Aplicada & Ingn Proyectos, Escuela Tecn Super Ingenieros Ind, E-13071 Ciudad Real, Spain
[2] Univ Castilla La Mancha, Inst Invest Energias Renovables, Albacete 02071, Spain
关键词
FLUIDIZED-BED; STEAM GASIFICATION; CATALYTIC BEHAVIOR; PYROLYSIS; KINETICS; CHAR; IRON; HYDROGASIFICATION; DEVOLATILISATION; REACTIVITY;
D O I
10.1021/ef901585f
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
An experimental study of entrained flow, air-blown cogasification of biomass and a coal coke mixture has been performed in order to evaluate the effect of the relative fuel/air ratio (ranging between 2.5 and 7.5), the reaction temperature (ranging between 750 and 1150 degrees C), and the biomass content in the fuel blend on the producer gas composition and the process performance. Dealcoholized grape mare, a waste coming from the wine industry and with high potential in the south-central regions of Spain, has been chosen as biomass fuel. On the other hand, the coal coke blend (composed of a low-rank autochthonous coal and a solid residue from refineries) is an abundant fossil fuel which is used in a commercial IGCC power plant. The results obtained show that an increase of the biomass content in the fuel blend upgrades the producer gas quality and improves the cold gas efficiency. Some hints of synergy between biomass and coal coke have been found, especially at low fuel/air ratios and low reaction temperatures, which might be mainly related to the content and composition of the blend ash (especially due to the catalytic effect of Ca and K coming from the biomass ash, and the Fe, Ni, and Zn contents of the coal coke ash). However, thermogravimetric analyses have not provided enough information about possible interaction between biomass and coal coke.
引用
收藏
页码:2479 / 2488
页数:10
相关论文
共 45 条
[1]   New effects during steam gasification of naphthalene:: the synergy between CaO and MgO during the catalytic reaction [J].
Alarcón, N ;
García, X ;
Centeno, MA ;
Ruiz, P ;
Gordon, A .
APPLIED CATALYSIS A-GENERAL, 2004, 267 (1-2) :251-265
[2]   Fluidised bed co-gasification of coal and olive oil industry wastes [J].
André, RN ;
Pinto, F ;
Franco, C ;
Dias, M ;
Gulyurtlu, I ;
Matos, MAA ;
Cabrita, I .
FUEL, 2005, 84 (12-13) :1635-1644
[3]  
*BASF CAT LLC, 2007, BS8496 BASF CAT LLC
[4]  
BI J, 2005, 2 BIOM AS WORKSH BAN
[5]   THE TECHNICAL AND ECONOMIC-FEASIBILITY OF BIOMASS GASIFICATION FOR POWER-GENERATION [J].
BRIDGWATER, AV .
FUEL, 1995, 74 (05) :631-653
[6]   Co-gasification of biomass and coal for methanol synthesis [J].
Chmielniak, T ;
Sciazko, M .
APPLIED ENERGY, 2003, 74 (3-4) :393-403
[7]   The effect of calcium on the rate and products of steam gasification of char from low rank coal [J].
Clemens, AH ;
Damiano, LF ;
Matheson, TW .
FUEL, 1998, 77 (9-10) :1017-1020
[8]  
COCA P, 2009, FLEXGAS WORKSH COG C
[9]   Co-pyrolysis and co-gasification of coal and biomass in bench-scale fixed-bed and fluidised bed reactors [J].
Collot, AG ;
Zhuo, Y ;
Dugwell, DR ;
Kandiyoti, R .
FUEL, 1999, 78 (06) :667-679
[10]   Coal/biomass co-gasification in a pressurised fluidised bed reactor [J].
de Jong, WB ;
Andries, J ;
Hein, KRG .
RENEWABLE ENERGY, 1999, 16 (1-4) :1110-1113