Modeling Product Distribution of Top-lit Updraft Gasification

被引:3
作者
James, Arthur M. R. [1 ]
Castorena, Cassie [2 ]
Yuan, Wenqiao [3 ]
机构
[1] Univ Tecnol Panama, Dept Mech Engn, Apartado 0819-07289, Panama City, Panama
[2] North Carolina State Univ, Dept Civil Construct & Environm Engn, Raleigh, NC 27695 USA
[3] North Carolina State Univ, Dept Biol & Agr Engn, Raleigh, NC 27695 USA
基金
美国国家科学基金会; 美国食品与农业研究所;
关键词
Top-lit updraft; Gasification; Kinetic model; Biomass; Producer gas; DOWNDRAFT BIOMASS GASIFIER; PARTICLE-SIZE; AIR-FLOW; PYROLYSIS; TEMPERATURE; CONVERSION; MOISTURE; BIOCHAR; SYNGAS; FUEL;
D O I
10.15376/biores.16.4.6629-6642
中图分类号
TB3 [工程材料学]; TS [轻工业、手工业、生活服务业];
学科分类号
0805 ; 080502 ; 0822 ;
摘要
A kinetic model for predicting biochar, producer gas, and tar formations of top-lit updraft (TLUD) gasification was developed. The three main zones within the TLUD gasifier, the pyrolysis, incomplete combustion, and reduction reaction zones, were incorporated into the model and sequentially solved. Validated with experimental data, the model was found capable of predicting biochar yield on pine woodchips at varying airflow rates, biomass moisture contents, and biomass compactness. However, when the particle size was varied, the model underestimated biochar yield. The model also accurately predicted the higher heating value of the producer gas that varied from 3.45 to 3.98 MJ/m(3) compared to 3.61 to 3.67 MJ/m(3) for the experimental results. The model qualitatively predicted tar content in the producer gas at varying conditions. However, accurate quantification of tar generation in TLUD gasification was not achieved.
引用
收藏
页码:6629 / 6642
页数:14
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