Effects of slow-pyrolysis conditions on the products yields and properties and on exergy efficiency: A comprehensive assessment for wheat straw

被引:31
|
作者
Greco, Gianluca [1 ]
Di Stasi, Christian [1 ]
Rego, Filipe [2 ]
Gonzalez, Belen [1 ]
Manya, Joan J. [1 ]
机构
[1] Univ Zaragoza, Technol Coll Huesca, Aragon Inst Engn Res I3A, Crta Cuarte S-N, E-22071 Huesca, Spain
[2] Aston Univ, Energy & Bioprod Res Inst EBRI, Birmingham B4 7ET, W Midlands, England
关键词
Wheat straw; Slow pyrolysis; Char; Pyrolysis conditions; Energy and exergy analysis; PEAK TEMPERATURE; RICE HUSK; GASIFICATION REACTIVITY; PRESSURIZED PYROLYSIS; OPERATING PARAMETERS; BIOMASS PYROLYSIS; CO2; GASIFICATION; PARTICLE-SIZE; BIOCHAR; ENERGY;
D O I
10.1016/j.apenergy.2020.115842
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
In the present work, the effects of the peak temperature (400550 degrees C), absolute pressure (0.20.9 MPa), gas residence time (100-200 s) and reactor atmosphere (pure N-2 or a mixture of CO2/N-2) on the pyrolysis behavior of wheat straw pellets were investigated. A factorial design of experiments was adopted to assess the effects of the above-mentioned factors on the pyrolysis products, the exergy efficiencies related to them and to the overall process, and the heat required. The pyrolysis energy/exergy assessment is nowadays of great interest, for the scaling of the installations from lab-scale to commercial-scale. Results showed that, as expected, the peak temperature was the most influential factor on the yields and distributions of all the pyrolysis products as well as the char properties related to its potential stability and pore size distribution. However, an increased pressure enhanced the release of the gas species at the expense of the liquid products, without altering the final char yield. The char exergy efficiency was negatively affected by an increase in peak temperature, whereas its effect on the exergy efficiency of the produced gas resulted to be positive. It was also found that pressurized pyrolysis favored the exergy efficiency of the process, even at relatively high pyrolysis peak temperature. For the biomass feedstock and the range of operating conditions studied here, thermodynamic irreversibilities of the pyrolysis system were considerably lowered when the process was conducted at 550 degrees C, 0.9 MPa and using a mixture of CO2 and N-2 as carrier gas at relatively short residence times.
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页数:13
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