Rotary kiln slow pyrolysis for syngas and char production from biomass and waste - Part I: Working envelope of the reactor

被引:50
作者
Fantozzi, Francesco
Colantoni, Simone
Bartocci, Pietro
Desideri, Umberto
机构
[1] Univ Perugia, Dept Ind Engn, I-06125 Perugia, Italy
[2] Univ Perugia, Biomass Res Ctr, I-06125 Perugia, Italy
来源
JOURNAL OF ENGINEERING FOR GAS TURBINES AND POWER-TRANSACTIONS OF THE ASME | 2007年 / 129卷 / 04期
关键词
biomass; pyrolysis; rotary kiln; residence time; syngas; tar; char;
D O I
10.1115/1.2720521
中图分类号
TH [机械、仪表工业];
学科分类号
0802 ;
摘要
A microscale electrically heated rotary kiln for slow pyrolysis of biomass and waste was designed and built at the University of Perugia. The reactor is connected to a wet scrubbing section, for tar removal, and to a monitored combustion chamber to evaluate the lower heating value of the syngas. The system allows the evaluation of gas, tar and char yields for different pyrolysis temperatures and residence times. The feeding screw conveyor and the kiln are rigidly connected; therefore, a modification of the flow rate implies a modification of the inside solid motion and of residence time. The paper provides the theoretical and experimental calculation of the relationships between residence time and flow rate used to determine the working envelope of the reactor as a function of the feedstock bulk density and moisture content, given the actual heat rate of the electric heaters. The methodology is extendable to any rotary kiln reactor with a rigidly connected feeding screw conveyor given its geometric and energetic specifications. Part H of the paper will extend the energy balance, also introducing the yields of pyrolysis products.
引用
收藏
页码:901 / 907
页数:7
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