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Oxygen migration characteristics during bamboo torrefaction process based on the properties of torrefied solid, gaseous, and liquid products
被引:108
作者:
Ma, Zhongqing
[1
,2
]
Zhang, Yu
[1
]
Shen, Yunfang
[3
]
Wang, Junhao
[1
]
Yang, Youyou
[1
]
Zhang, Wenbiao
[1
]
Wang, Shurong
[2
]
机构:
[1] Zhejiang A&F Univ, Zhejiang Prov Collaborat Innovat Ctr Bamboo Resou, Sch Engn, Hangzhou 311300, Zhejiang, Peoples R China
[2] Zhejiang Univ, State Key Lab Clean Energy Utilizat, 38 Zheda Rd, Hangzhou 310027, Zhejiang, Peoples R China
[3] Zhejiang Shenghua Yunfeng Greeneo Co LTD, Huzhou 313220, Zhejiang, Peoples R China
基金:
中国博士后科学基金;
关键词:
Bamboo biomass;
Torrefaction;
Deoxygenation mechanism;
Gaseous product;
Solid product;
Liquid product;
PYROLYSIS BEHAVIOR;
GASIFICATION PERFORMANCE;
OXIDATIVE TORREFACTION;
BIOMASS TORREFACTION;
MOSO BAMBOO;
RICE HUSK;
TGA-FTIR;
TEMPERATURE;
HEMICELLULOSE;
YIELD;
D O I:
10.1016/j.biombioe.2019.105300
中图分类号:
S2 [农业工程];
学科分类号:
0828 ;
摘要:
Bamboo is a potentially renewable biomass resource which can be converted into bio-fuels and bio-chemicals by thermochemical conversion technology. Torrefaction deoxygenation pretreatment can effectively upgrade bamboo into high-grade fuels with a lower content of water and higher energy density. Therefore, it is essential to establish the deoxygenation mechanism and oxygen migration characteristics during the bamboo torrefaction process, based on the properties of torrefied solid, gaseous, and liquid products. In this study, these three types of torrefied product (solid, gaseous, and liquid) were produced at different torrefaction temperatures (210, 240, 270 and 300 degrees C) by the tube furnace, TGA-FTIR, and Py-GC/MS. Results showed that following a series of deoxygenation reactions, the oxygen removal efficiency of bamboo reached a maximum of 28.52% at 300 degrees C, resulting in the highest HHV of 23.12 MJ kg(-1). Oxygen in the torrefied solid product was released in the form of torrefied gaseous components (CO2, H2O and CO) and torrefied liquid oxygen-containing compounds (E.g. acids, phenols, furans and ketones). CO2 was the dominant oxygen carrier in the torrefied gaseous product, with oxygen distribution in the torrefied gaseous components ranked in the order: CO2 (82.1-86.6%) > CO (10.9-13.9%) > H2O (2.4-4.1%). In the torrefied liquid product, oxygen transferred to acids, furans, ketones and aldehydes was favored under lower torrefaction temperatures, while more oxygen was transferred to phenols under higher torrefaction temperatures.
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页数:11
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