Title of article :
Gas evolution kinetics of two coal samples during rapid pyrolysis
Author/Authors :
Chen، نويسنده , , L. and Zeng، نويسنده , , C. and Guo، نويسنده , , X. and Mao، نويسنده , , Y. and Zhang، نويسنده , , Y. and Zhang، نويسنده , , X. and Li، نويسنده , , W. and Long، نويسنده , , Y. and Zhu، نويسنده , , H. and Eiteneer، نويسنده , , B. and Zamansky، نويسنده , , V.، نويسنده ,
Issue Information :
روزنامه با شماره پیاپی سال 2010
Pages :
5
From page :
848
To page :
852
Abstract :
Quantitative gas evolution kinetics of coal primary pyrolysis at high heating rates is critical for developing predictive coal pyrolysis models. This study aims to investigate the gaseous species evolution kinetics of a low rank coal and a subbituminous coal during pyrolysis at a heating rate of 1000 °C s− 1 and pressures up to 50 bar using a wire mesh reactor. The main gaseous species, including H2, CO, CO2, and light hydrocarbons CH4, C2H2, C2H4, C2H6, C3H6, C3H8, were quantified using high sensitivity gas chromatography. It was found that the yields of gaseous species increased with increasing pyrolysis temperature up to 1100 °C. The low rank coal generated more CO and CO2 than the subbituminous coal under similar pyrolysis conditions. Pyrolysis of the low rank coal at 50 bar produced more gas than at atmospheric pressure, especially CO2, indicating that the tar precursor had undergone thermal cracking during pyrolysis at the elevated pressure.
Keywords :
Coal , Pyrolysis , Wire mesh reactor , Gaseous species , Tar
Journal title :
Fuel Processing Technology
Serial Year :
2010
Journal title :
Fuel Processing Technology
Record number :
1509230
Link To Document :
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