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Kinetic combustion experiments in a pressurized fluidized bed

Conference ·
OSTI ID:6089996
 [1];  [2]
  1. Chalmers Univ. of Tech., Goeteborg (Sweden). Dept. of Energy Conversion Lawrence Livermore National Lab., CA (USA)
  2. Chalmers Univ. of Tech., Goeteborg (Sweden). Dept. of Energy Conversion

Batch combustion experiments have been performed in a bench-scale pressurized fluidized bed with the objective of establishing combustion rates under typical pressurized fluidized bed conditions. Resulting combustion conversion vs. time relationships show that pressure has no significant effect on the combustion rates of a medium-volatile bituminous coal over a wide range of practically important combustion conditions: fluidized bed temperature 700-800 C, coal particle size 0.3-4.8mm, and O{sub 2} concentration 3-7%. Pressures of 0.2, 1 and 2 MPa are studied. The explanation of the lack of a pressure effect on the overall combustion kinetics derives from mass-transfer controlled kinetics: pressure increases the driving force for O{sub 2} mass transfer by increasing O{sub 2} partial pressure but reduces diffusivity at the same time. Pressure-insensitive combustion kinetics are predicted to lead to relatively high char concentrations in pressurized beds. This in turn can lead to low combustion efficiency (by excessive loss of attrited char) but also to low emissions of NO{sub x} (high char concentrations favor NO{sub x} reduction). Measured burning particle temperatures are also relatively low, further promoting low levels of NO{sub x}. 15 refs., 7 figs., 1 tab.

Research Organization:
Lawrence Livermore National Lab., CA (USA)
Sponsoring Organization:
DOE; SENEA; USDOE, Washington, DC (USA); Statens Energiverk, Stockholm (Sweden)
DOE Contract Number:
W-7405-ENG-48
OSTI ID:
6089996
Report Number(s):
UCRL-JC-106115; CONF-9103145--1; ON: DE91009734; CNN: 276 398-1
Country of Publication:
United States
Language:
English