A novel technique for measuring the kinetics of high-temperature gasification of biomass char with steam

被引:26
作者
Woodruff, R. Bryan [1 ]
Weimer, Alan W. [1 ]
机构
[1] Univ Colorado, Dept Chem & Biol Engn, Boulder, CO 80309 USA
基金
美国农业部;
关键词
Gasification; Biomass char; Kinetics; Random pore model; Langmuir-Hinshelwood; REACTOR; COMBUSTION; PRESSURE; HYDROGEN; PRODUCT; FUELS; CO2;
D O I
10.1016/j.fuel.2012.09.035
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
Solar thermal gasification of biomass is a promising technology that allows for operation at high temperature without burning a large portion of the biomass feedstock. Additionally, the process allows for solar energy to be stored and transported in chemical form. In order to design efficient solar reactors, a kinetic rate expression for high-temperature steam gasification is needed. Various methods have been used to measure the steam gasification rate of coal and biomass char at temperatures up to 1000 degrees C. These conventional techniques often fail to collect accurate kinetic data at temperatures above 1000 degrees C due to heat and mass transfer resistance, and the time constants associated with the analysis system. In this paper we discuss a novel kinetics measurement technique based on a modified fixed bed and data collected solely from a gas flow meter. The technique was used to collect kinetic rate data for switchgrass char over a range of reaction conditions between 1000 degrees C and 1150 degrees C. An empirical expression to predict the kinetic rate as a function of the degree of conversion, temperature, steam concentration, and hydrogen concentration was developed. The random pore model was used to predict the reaction rate as a function of conversion, and the initial kinetic rate was fit using a Langmuir-Hinshelwood type expression. (C) 2012 Published by Elsevier Ltd.
引用
收藏
页码:749 / 757
页数:9
相关论文
共 21 条
[1]   Kinetics of woodchips char gasification with steam and carbon dioxide [J].
Ahmed, I. I. ;
Gupta, A. K. .
APPLIED ENERGY, 2011, 88 (05) :1613-1619
[2]   Parameters of high temperature steam gasification of original and pulverised wood pellets [J].
Alevanau, Aliaksandr ;
Ahmed, Islam ;
Gupta, Ashwani K. ;
Yang, Weihong ;
Blasiak, Wlodzimierz .
FUEL PROCESSING TECHNOLOGY, 2011, 92 (10) :2068-2074
[3]  
BHATIA SK, 1980, AICHE J, V26, P379, DOI 10.1002/aic.690260308
[4]   Development and characterization of a lab-scale entrained flow reactor for testing biomass fuels [J].
Biagini, E ;
Cioni, M ;
Tognotti, L .
FUEL, 2005, 84 (12-13) :1524-1534
[5]   Combustion and gasification rates of lignocellulosic chars [J].
Di Blasi, Colomba .
PROGRESS IN ENERGY AND COMBUSTION SCIENCE, 2009, 35 (02) :121-140
[6]   Kinetic modelling of steam gasification of various woody biomass chars: Influence of inorganic elements [J].
Dupont, Capucine ;
Nocquet, Timothee ;
Da Costa, Jose Augusto, Jr. ;
Verne-Tournon, Christele .
BIORESOURCE TECHNOLOGY, 2011, 102 (20) :9743-9748
[7]   Inhibition of steam gasification of biomass char by hydrogen and tar [J].
Fushimi, Chihiro ;
Wada, Tomoko ;
Tsutsumi, Atsushi .
BIOMASS & BIOENERGY, 2011, 35 (01) :179-185
[8]   THE KINETICS OF THE REACTIONS OF THE STEAM-CARBON SYSTEM [J].
GADSBY, J ;
HINSHELWOOD, CN ;
SYKES, KW .
PROCEEDINGS OF THE ROYAL SOCIETY OF LONDON SERIES A-MATHEMATICAL AND PHYSICAL SCIENCES, 1946, 187 (1009) :129-151
[9]   Kinetic studies of char gasification by steam and CO2 in the presence of H2 and CO [J].
Huang, Zhimin ;
Zhang, Jiansheng ;
Zhao, Yong ;
Zhang, Hai ;
Yue, Guanxi ;
Suda, Toshiyuki ;
Narukawa, Masahiro .
FUEL PROCESSING TECHNOLOGY, 2010, 91 (08) :843-847
[10]   THE CARBON-STEAM REACTION AT ELEVATED PRESSURE - FORMATIONS OF PRODUCT GASES AND HYDROGEN INHIBITIONS [J].
HUTTINGER, KJ ;
MERDES, WF .
CARBON, 1992, 30 (06) :883-894