TY - RPRT
T1 - Straw Combustion in a Grate Furnace
T2 - Fixed-Bed Experiments
AU - Lans, Robert Pieter Van Der
PY - 1998
Y1 - 1998
N2 - Fixed-bed combustion of straw has been conducted in a 15 cm
diameter and 137 cm long cylindrical reactor. Air, which could be
preheated, was introduced through the bottom plate. The straw was
ignited at the top with a radiation heater. After ignition, when a
self-sustaining reaction front was attained, the radiation source
was removed. Temperatures were measured at 8 locations inside the
bed, and the concentrations of O2, CO2, CO, H2O, CxHy, NOx, and
NH3 were measured at the location of the upper thermocouple, i.e.
30 cm under the top of the bed. Air velocities of 6, 10 and 15
cm/s (Standard Temperature and Pressure) were used, air
temperatures of 20, 150 and 200°C, and as bed material finely cut
straw (dp
AB - Fixed-bed combustion of straw has been conducted in a 15 cm
diameter and 137 cm long cylindrical reactor. Air, which could be
preheated, was introduced through the bottom plate. The straw was
ignited at the top with a radiation heater. After ignition, when a
self-sustaining reaction front was attained, the radiation source
was removed. Temperatures were measured at 8 locations inside the
bed, and the concentrations of O2, CO2, CO, H2O, CxHy, NOx, and
NH3 were measured at the location of the upper thermocouple, i.e.
30 cm under the top of the bed. Air velocities of 6, 10 and 15
cm/s (Standard Temperature and Pressure) were used, air
temperatures of 20, 150 and 200°C, and as bed material finely cut
straw (dp
M3 - Report
BT - Straw Combustion in a Grate Furnace
ER -