Šiaudų degimas stacionariame sluoksnyje
Behavior of combustion process in the fuel bed on the grate, is characterized by different thermochemical conversion stages, each with significantly different temperatures, and the reacting conditions. This simple analysis of combustion processes taking place on the grate is a useful information for...
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Lithuanian Academic Libraries Network (LABT)
2005
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Online Access: | http://vddb.library.lt/fedora/get/LT-eLABa-0001:E.02~2005~D_20050722_115416-43995/DS.005.0.01.ETD |
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ndltd-LABT_ETD-oai-elaba.lt-LT-eLABa-0001-E.02~2005~D_20050722_115416-439952014-01-17T03:45:50Z2005-07-22litPower and Thermal EngineeringKavaliauskas, AndriusŠiaudų degimas stacionariame sluoksnyjeStraw combustion in a packed bedLithuanian Academic Libraries Network (LABT)Behavior of combustion process in the fuel bed on the grate, is characterized by different thermochemical conversion stages, each with significantly different temperatures, and the reacting conditions. This simple analysis of combustion processes taking place on the grate is a useful information for understanding of the paths of pollutants formation and destruction as well. The large fixed bed reactor was used for obtaining the experimental results of straw combustion. The fixed bed reactor contains a column of biomass fuel that is ignited at the top and with air entering through the grate from the bottom, measurements are performed while the ignition front proceeds downwards. The influence of inlet air flow velocity and temperature, moisture content in the fuel and oxygen concentration in the inlet air on combustion parameters such as ignition front velocity (kg/(m2·s)), temperature, and gas species concentration during combustion is presented based on measurements of in-bed temperatures along the bed and different gas compounds (O2, CO2, CO and NO) over the bed. A 1-D transient heterogeneous model was used for straw combustion in a fixed bed. The processes included in the model comprise: moisture evaporation, biomass pyrolysis, heterogeneous reaction of char forming CO and CO2, homogeneous reactions of CO, H2, CH4, CxHy and tar, heat and mass transfer between the gas and solid phases. The model provided detailed structure of the ignition flame front, gas species... [to full text]CombustionStraw as fuelŠiaudaiStrawDegimasŠiaudų kurasDoctoral thesisKatinas, VladislovasČėsna, BenediktasSkrinska, Alfonsas KazysŠinkūnas, StasysKaunas University of TechnologyKaunas University of Technologyhttp://vddb.library.lt/obj/LT-eLABa-0001:E.02~2005~D_20050722_115416-43995LT-eLABa-0001:E.02~2005~D_20050722_115416-43995KTU-LABT20050722-115416-43995http://vddb.library.lt/fedora/get/LT-eLABa-0001:E.02~2005~D_20050722_115416-43995/DS.005.0.01.ETDUnrestrictedapplication/pdf |
collection |
NDLTD |
language |
Lithuanian |
format |
Doctoral Thesis |
sources |
NDLTD |
topic |
Power and Thermal Engineering Combustion Straw as fuel Šiaudai Straw Degimas Šiaudų kuras |
spellingShingle |
Power and Thermal Engineering Combustion Straw as fuel Šiaudai Straw Degimas Šiaudų kuras Kavaliauskas, Andrius Šiaudų degimas stacionariame sluoksnyje |
description |
Behavior of combustion process in the fuel bed on the grate, is
characterized by different thermochemical conversion stages, each with
significantly different temperatures, and the reacting conditions. This simple
analysis of combustion processes taking place on the grate is a useful
information for understanding of the paths of pollutants formation and
destruction as well. The large fixed bed reactor was used for obtaining the
experimental results of straw combustion. The fixed bed reactor contains a
column of biomass fuel that is ignited at the top and with air entering through
the grate from the bottom, measurements are performed while the ignition front
proceeds downwards. The influence of inlet air flow velocity and temperature,
moisture content in the fuel and oxygen concentration in the inlet air on
combustion parameters such as ignition front velocity (kg/(m2·s)), temperature,
and gas species concentration during combustion is presented based on
measurements of in-bed temperatures along the bed and different gas
compounds (O2, CO2, CO and NO) over the bed. A 1-D transient
heterogeneous model was used for straw combustion in a fixed bed. The
processes included in the model comprise: moisture evaporation, biomass
pyrolysis, heterogeneous reaction of char forming CO and CO2, homogeneous
reactions of CO, H2, CH4, CxHy and tar, heat and mass transfer between the gas
and solid phases. The model provided detailed structure of the ignition flame
front, gas species... [to full text] |
author2 |
Katinas, Vladislovas |
author_facet |
Katinas, Vladislovas Kavaliauskas, Andrius |
author |
Kavaliauskas, Andrius |
author_sort |
Kavaliauskas, Andrius |
title |
Šiaudų degimas stacionariame sluoksnyje |
title_short |
Šiaudų degimas stacionariame sluoksnyje |
title_full |
Šiaudų degimas stacionariame sluoksnyje |
title_fullStr |
Šiaudų degimas stacionariame sluoksnyje |
title_full_unstemmed |
Šiaudų degimas stacionariame sluoksnyje |
title_sort |
šiaudų degimas stacionariame sluoksnyje |
publisher |
Lithuanian Academic Libraries Network (LABT) |
publishDate |
2005 |
url |
http://vddb.library.lt/fedora/get/LT-eLABa-0001:E.02~2005~D_20050722_115416-43995/DS.005.0.01.ETD |
work_keys_str_mv |
AT kavaliauskasandrius siaududegimasstacionariamesluoksnyje AT kavaliauskasandrius strawcombustioninapackedbed |
_version_ |
1716625135115436032 |