Coal combustion releases elevated amounts of pollutants to the atmosphere including SO X . During the pyrolysis step, sulfur present in the coal is released to the gas phase as many different chemical species such as H 2 S, COS, SO 2 , CS 2 , thiols and larger tars, also called SO X precursors, as they form SO X during combustion. Understanding the sulfur release process is crucial to the development of reliable kinetic models, which support the design of improved reactors for cleaner coal conversion processes. Sulfur release from two bituminous coals, Colombian hard coal (K1) and American high sulfur coal (U2), were studied in the present work. Low heating rate (LHR) experiments were performed in a thermogravimetric analyzer coupled with mass spectrometry (TG-MS), allowing to track the mass loss and the evolution of many volatile species (CO, CO 2 , CH 4 , SO 2 , H 2 S, COS, HCl and H 2 O). High heating rate (HHR) experiments were performed in an entrained flow reactor (drop-tube reactor - DTR), coupled with MS and nondispersive infrared sensor (NDIR). HHR experiments were complemented with CFD simulation of the multidimentional reacting flow field. A kinetic model of coal pyrolysis is employed to reproduce the experiments allowing a comprehensive assessment of the process. The suitability of this model is confirmed for LHR. The combination of HHR experiments with CFD simulations and kinetic modeling revealed the complexity of sulfur chemistry in coal combustion and allowed to better understand of the individual phenomena resulting in the formation of the different SO X precursors. LHR and HHR operating conditions lead to different distribution of sulfur species released, highly-dependent on the gas-phase temperature and residence time. Higher retention of total sulfur in char is observed at LHR (63%) when compared to HHR (37-44%), at 1273 K. These data support the development of reliable models with improved predictability.

Experimental and modeling assessment of sulfur release from coal under low and high heating rates

Faravelli T.;Hasse C.
2020-01-01

Abstract

Coal combustion releases elevated amounts of pollutants to the atmosphere including SO X . During the pyrolysis step, sulfur present in the coal is released to the gas phase as many different chemical species such as H 2 S, COS, SO 2 , CS 2 , thiols and larger tars, also called SO X precursors, as they form SO X during combustion. Understanding the sulfur release process is crucial to the development of reliable kinetic models, which support the design of improved reactors for cleaner coal conversion processes. Sulfur release from two bituminous coals, Colombian hard coal (K1) and American high sulfur coal (U2), were studied in the present work. Low heating rate (LHR) experiments were performed in a thermogravimetric analyzer coupled with mass spectrometry (TG-MS), allowing to track the mass loss and the evolution of many volatile species (CO, CO 2 , CH 4 , SO 2 , H 2 S, COS, HCl and H 2 O). High heating rate (HHR) experiments were performed in an entrained flow reactor (drop-tube reactor - DTR), coupled with MS and nondispersive infrared sensor (NDIR). HHR experiments were complemented with CFD simulation of the multidimentional reacting flow field. A kinetic model of coal pyrolysis is employed to reproduce the experiments allowing a comprehensive assessment of the process. The suitability of this model is confirmed for LHR. The combination of HHR experiments with CFD simulations and kinetic modeling revealed the complexity of sulfur chemistry in coal combustion and allowed to better understand of the individual phenomena resulting in the formation of the different SO X precursors. LHR and HHR operating conditions lead to different distribution of sulfur species released, highly-dependent on the gas-phase temperature and residence time. Higher retention of total sulfur in char is observed at LHR (63%) when compared to HHR (37-44%), at 1273 K. These data support the development of reliable models with improved predictability.
2020
Coal
Kinetic modeling
Pyrolysis
SO
X
Sulfur
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Utilizza questo identificativo per citare o creare un link a questo documento: https://hdl.handle.net/11311/1168557
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