Alkali metal emission during pyrolysis of biomass

被引:222
作者
Olsson, JG
Jaglid, U
Pettersson, JBC
Hald, P
机构
[1] GOTHENBURG UNIV,DEPT CHEM,S-41296 GOTHENBURG,SWEDEN
[2] RISO NATL LAB,DEPT ENVIRONM SCI & TECHNOL,DK-4000 ROSKILDE,DENMARK
关键词
D O I
10.1021/ef960096b
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 alkali metal release during pyrolysis of biomass is investigated with a surface ionization method. Wheat straw samples (20 mg) are pyrolyzed in a laboratory unit under Nz atmosphere, and two characteristic temperature intervals for alkali metal emission are identified. A small fraction of the alkali metal content is released in a low-temperature region (180-500 degrees C) and is attributed to a connection with the decomposition of the organic structure. The two most pronounced emission processes below 500 degrees C are well described by a first-order rate behavior, and the activation energies are found to be 156 +/- 11 and 178 +/- 8 kJ/mol, The major part of the alkali metal release takes place in the high-temperature region (> 500 degrees C), and activation energies of alkali metal emission from the ash residues are found in the range 168-238 kJ/mol. A high chlorine content is found to enhance the alkali metal emission from the ash, while the alkali metal release in the low-temperature region cannot be correlated with the chlorine content.
引用
收藏
页码:779 / 784
页数:6
相关论文
共 30 条
[1]   Inorganic compounds in biomass feedstocks .1. Effect on the quality of fast pyrolysis oils [J].
Agblevor, FA ;
Besler, S .
ENERGY & FUELS, 1996, 10 (02) :293-298
[2]   CELLULOSE PYROLYSIS KINETICS - THE CURRENT STATE KNOWLEDGE [J].
ANTAL, MJ ;
VARHEGYI, G .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1995, 34 (03) :703-717
[3]   DIRECT OBSERVATION OF ALKALI VAPOR RELEASE DURING BIOMASS COMBUSTION AND GASIFICATION .1. APPLICATION OF MOLECULAR-BEAM MASS-SPECTROMETRY TO SWITCHGRASS COMBUSTION [J].
DAYTON, DC ;
FRENCH, RJ ;
MILNE, TA .
ENERGY & FUELS, 1995, 9 (05) :855-865
[4]   Direct observation of alkali vapor release during biomass combustion and gasification .2. Black liquor combustion at 1100 degrees C [J].
Dayton, DC ;
Frederick, WJ .
ENERGY & FUELS, 1996, 10 (02) :284-292
[5]  
DAYTON DC, 1994, NRELTP4305597
[6]   Pyrolysis and combustion of pulverized wheat straw in a pressurized entrained flow reactor [J].
Fjellerup, J ;
Gjernes, E ;
Hansen, LK .
ENERGY & FUELS, 1996, 10 (03) :649-651
[7]  
HAGSTROM M, UNPUB
[8]  
Hald P, 1994, THESIS TU DENMARK LY
[9]  
HALLGREN A, 1996, THESIS LUND U LUND
[10]   CESIUM ION DESORPTION FROM OXYGEN AND CARBON ADLAYERS ON PLATINUM SURFACES WITH NANOSECOND TIME RESOLUTION - VARIATION OF DESORPTION PARAMETERS WITH TIME AVAILABLE FOR SURFACE-DIFFUSION AND DEGREE OF SURFACE HETEROGENEITY [J].
HOLMLID, L ;
MOLLER, K .
SURFACE SCIENCE, 1985, 149 (2-3) :609-620