Experimental study on fast pyrolysis of free-falling millimetric biomass particles between 800°C and 1000°C

被引:28
作者
Chen, Li [1 ]
Dupont, Capucine [1 ]
Salvador, Sylvain [2 ]
Grateau, Maguelone [1 ]
Boissonnet, Guillaume [1 ]
Schweich, Daniel [3 ]
机构
[1] CEA Grenoble, DRT, LITEN, DTBH,LTB, F-38054 Grenoble, France
[2] CNRS Mines Albi Carmaux, Ctr RAPSODEE, UMR 5302, F-81013 Route De Teillet, Albi, France
[3] CPE Lyon, CNRS, LGPC, F-69616 Villeurbanne, France
关键词
Biomass; Fast pyrolysis; Drop tube; Particle size; Kinetics; HIGH-TEMPERATURE; RAPID PYROLYSIS; AGRICULTURAL RESIDUES; REACTOR; WOOD; GAS; MODEL;
D O I
10.1016/j.fuel.2012.11.058
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
Pyrolysis experiments were performed between 800 degrees C and 950 degrees C on wood particles with diameters from 350 to 800 mu m in a lab-scale drop tube reactor to reproduce surface heat flux representative of gasifiers conditions. It was shown that particle size affected the required pyrolysis time but changed neither gas/tar/char mass yields nor composition of the products at the end of pyrolysis. The initial particle size also affected the resulting char morphology: the larger the biomass particles, the more fibrous the char. Temperature had influence neither on gas/tar/char mass yields nor on gas and solid elemental composition at the end of pyrolysis, but significantly changed the yields of individual gas species. Whatever the conditions tested, a significant shrinkage could be observed on particles during pyrolysis. These experimental results confirm the strong coupling between chemical reactions, particle geometrical properties and heat transfers during pyrolysis under these conditions. (C) 2012 Elsevier Ltd. All rights reserved.
引用
收藏
页码:61 / 66
页数:6
相关论文
共 20 条
[1]   Effects of intraparticle heat and mass transfer on biomass devolatilization: Experimental results and model predictions [J].
Bharadwaj, A ;
Baxter, LL ;
Robinson, AL .
ENERGY & FUELS, 2004, 18 (04) :1021-1031
[2]  
Commandre J.-M., 2002, FORMATION OXYDES AZO
[3]   Is it possible to predict gas yields of any biomass after rapid pyrolysis at high temperature from its composition in cellulose, hemicellulose and lignin? [J].
Couhert, Carole ;
Commandre, Jean-Michel ;
Salvador, Sylvain .
FUEL, 2009, 88 (03) :408-417
[4]   Suspension combustion of wood: Influence of pyrolysis conditions on char yield, morphology, and reactivity [J].
Dall'Ora, Michelangelo ;
Jensen, Peter Arendt ;
Jensen, Anker Degn .
ENERGY & FUELS, 2008, 22 (05) :2955-2962
[5]   TG-FTIR pyrolysis of coal and secondary biomass fuels:: Determination of pyrolysis kinetic parameters for main species and NOx precursors [J].
de Jong, W. ;
Di Nola, G. ;
Venneker, B. C. H. ;
Spliethoff, H. ;
Wojtowicz, M. A. .
FUEL, 2007, 86 (15) :2367-2376
[7]  
Dupont C, 2006, VAPOGAZEIFICATION BI, p[1, 2006]
[8]   Biomass pyrolysis experiments in an analytical entrained flow reactor between 1073 K and 1273 K [J].
Dupont, Capucine ;
Commandre, Jean-Michel ;
Gauthier, Paola ;
Boissonnet, Guillaume ;
Salvador, Sylvain ;
Schweich, Daniel .
FUEL, 2008, 87 (07) :1155-1164
[9]   Pyrolysis of two agricultural residues: Olive and grape bagasse, influence of particle size and temperature. [J].
Encinar, JM ;
Beltran, FJ ;
Bernalte, A ;
Ramiro, A ;
Gonzalez, JF .
BIOMASS & BIOENERGY, 1996, 11 (05) :397-409
[10]  
Gronli M.G., 1996, THEORETICAL EXPT STU