TY - GEN
T1 - CFB gasification of biomass residues for co-combustion in large utility boilers
T2 - Power Production from Biomass III
AU - Kurkela, Esa
AU - Moilanen, Antero
AU - Nieminen, Matti
PY - 1999
Y1 - 1999
N2 - Atmospheric-pressure gasification of biomass and waste
fuels and co-firing of pro-duced gas in large utility
boilers is a promising and cost-effective method for
re-ducing the CO2 emissions of coal-based energy
production in short and medium time scale. The
commercialisation of this co-utilisation technology will
also pro-mote the development and commercialisation of
advanced biomass-based power production systems, such as
IGCC, which in the longer run have a key role in the
global renewable intensive energy scenarios.
The woody residues of mechanical and chemical wood
industry as well as other high-grade woody biofuels can
be co-combusted with coal in existing fluidised-bed
boilers or even in pulverised combustors (1, 2) without
major problems. On the other hand, extensive full-scale
test programmes carried out with straw in Denmark (3) and
with various agrobiofuels in the United States (4) have
clearly shown the limitations of this type of
co-combustion methods. Many potential biomass
feed-stocks, such as straw, have a problematic ash
melting behaviour, which causes sintering and fouling
problems in combustors. Straw and many fast-growing
energy crops as well as industrial and municipal waste
fuels often contain high amounts of chlorine and alkali
metals, which have a tendency to cause severe corrosion
prob-lems in coal-fired boilers. This problem can be
assumed to be more severe in the modern plants where
supercritical steam values are utilised.
Perhaps the most critical factor controlling
possibilities for direct co-firing of these problematic
biofuels in large PC boilers is the usability of coal ash
for cement in-dustry and construction purposes.
Demolition wood waste is another example of a locally
important renewable feedstock, which is difficult to be
introduced into ordi-nary coal-based combustion plants
due to the relatively high content of heavy met-als (Zn,
Pb, Cd) and chlorine.
In principle, there are three main technical solutions to
avoid sintering, corrosion and ash problems in
co-utilisation of problematic biofuels in large
coal-fired power plants:
· Construction of a smaller separate boiler with low
steam values for the biofu-els and superheating the steam
of the biomass boiler in the coal-fired boiler.
· Production of pyrolysis oils from the biomass, and
· Gasification of biomass and combustion of cleaned
product gas in the boiler.
The concept based on gasification has several advantages
over the other alterna-tives. First of all the
gasification reactor, bubbling or circulating
fluidised-bed, is simpler and much cheaper than the
complete fluidised-bed boilers with steam cy-cles or
complete pyrolysis oil production plants. Secondly, the
product gas can be cleaned from trace metals, chlorine
and other harmful contaminants prior to leading into the
coal-fired boiler. Depending on the feedstock quality and
on the require-ments for contaminant control different
gas cleaning methods from simple hot cy-clones to
effective low-temperature filtration can be used.
Thirdly, the separation of gasification and gas
combustion makes it possible to maintain stable
high-temperature combustion in order to minimise risks
for the formation of dioxins and other chlorinated
organic compounds. Finally, the biomass-derived gas may
even have positive effects also on the NOx emissions if
it is introduced to the coal-fired boiler as a reburning
feedstock (5).
At present, there are a lot of on-going activities in
Europe aiming at the demon-stration and commercialisation
of this promising co-utilisation concept (6). Al-most all
activities are based on Circulating Fluidised-Bed
gasifiers. Series of studies on the critical technical
questions of this co-utilisation concept are car-ried out
by VTT Energy in the PROGAS R&D programme. The results
obtained with wheat straw, demolition wood and fresh wood
are outlined in this paper.
AB - Atmospheric-pressure gasification of biomass and waste
fuels and co-firing of pro-duced gas in large utility
boilers is a promising and cost-effective method for
re-ducing the CO2 emissions of coal-based energy
production in short and medium time scale. The
commercialisation of this co-utilisation technology will
also pro-mote the development and commercialisation of
advanced biomass-based power production systems, such as
IGCC, which in the longer run have a key role in the
global renewable intensive energy scenarios.
The woody residues of mechanical and chemical wood
industry as well as other high-grade woody biofuels can
be co-combusted with coal in existing fluidised-bed
boilers or even in pulverised combustors (1, 2) without
major problems. On the other hand, extensive full-scale
test programmes carried out with straw in Denmark (3) and
with various agrobiofuels in the United States (4) have
clearly shown the limitations of this type of
co-combustion methods. Many potential biomass
feed-stocks, such as straw, have a problematic ash
melting behaviour, which causes sintering and fouling
problems in combustors. Straw and many fast-growing
energy crops as well as industrial and municipal waste
fuels often contain high amounts of chlorine and alkali
metals, which have a tendency to cause severe corrosion
prob-lems in coal-fired boilers. This problem can be
assumed to be more severe in the modern plants where
supercritical steam values are utilised.
Perhaps the most critical factor controlling
possibilities for direct co-firing of these problematic
biofuels in large PC boilers is the usability of coal ash
for cement in-dustry and construction purposes.
Demolition wood waste is another example of a locally
important renewable feedstock, which is difficult to be
introduced into ordi-nary coal-based combustion plants
due to the relatively high content of heavy met-als (Zn,
Pb, Cd) and chlorine.
In principle, there are three main technical solutions to
avoid sintering, corrosion and ash problems in
co-utilisation of problematic biofuels in large
coal-fired power plants:
· Construction of a smaller separate boiler with low
steam values for the biofu-els and superheating the steam
of the biomass boiler in the coal-fired boiler.
· Production of pyrolysis oils from the biomass, and
· Gasification of biomass and combustion of cleaned
product gas in the boiler.
The concept based on gasification has several advantages
over the other alterna-tives. First of all the
gasification reactor, bubbling or circulating
fluidised-bed, is simpler and much cheaper than the
complete fluidised-bed boilers with steam cy-cles or
complete pyrolysis oil production plants. Secondly, the
product gas can be cleaned from trace metals, chlorine
and other harmful contaminants prior to leading into the
coal-fired boiler. Depending on the feedstock quality and
on the require-ments for contaminant control different
gas cleaning methods from simple hot cy-clones to
effective low-temperature filtration can be used.
Thirdly, the separation of gasification and gas
combustion makes it possible to maintain stable
high-temperature combustion in order to minimise risks
for the formation of dioxins and other chlorinated
organic compounds. Finally, the biomass-derived gas may
even have positive effects also on the NOx emissions if
it is introduced to the coal-fired boiler as a reburning
feedstock (5).
At present, there are a lot of on-going activities in
Europe aiming at the demon-stration and commercialisation
of this promising co-utilisation concept (6). Al-most all
activities are based on Circulating Fluidised-Bed
gasifiers. Series of studies on the critical technical
questions of this co-utilisation concept are car-ried out
by VTT Energy in the PROGAS R&D programme. The results
obtained with wheat straw, demolition wood and fresh wood
are outlined in this paper.
KW - gasification
M3 - Conference article in proceedings
SN - 951-38-5267-9
T3 - VTT Symposium
SP - 213
EP - 228
BT - Power Production from Biomass III
PB - VTT Technical Research Centre of Finland
CY - Espoo
Y2 - 14 September 1998 through 15 September 1998
ER -