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BIOS BIOENERGIESYSTEME GmbHBIOS BIOENERGIESYSTEME GmbHInstitute for Process and Particle EngineeringInstitute for Process and Particle Engineering
Graz University of TechnologyGraz University of Technology
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E N E R G Y B I O M A S S
A S H
Prof. Dr. Ingwald Obernberger
Biomass combustion Biomass combustion ––current status and future developmentscurrent status and future developments
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BIOENERGIESYSTEME GmbHInffeldgasse 21b, A-8010 Graz ContentsContents
Thermal biomass utilisation in Europe
Biomass combustion technologies
Relevant characteristics of biomass fuels andadvanced fuel characterisation
Ash related problems
Gaseous emissions under special consideration of NOx
CFD as an efficient tool to design and optimise biomass combustion systems
Intelligent process control systems
Relevant future R&D trends
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BIOENERGIESYSTEME GmbHInffeldgasse 21b, A-8010 Graz
Primary energy consumption and total Primary energy consumption and total turnover of biomass combustion plants turnover of biomass combustion plants in the EU for 2008 and outlook for 2020in the EU for 2008 and outlook for 2020
Explanations: small-, medium-, and large-scale plant considered; calculations based on present market and achievement of EU 2020 targets
0
2000
4000
6000
8000
10000
12000
14000
16000
18000
prim
ary
ener
gy c
onsu
mpt
ion
[PJ/
a]tu
rnov
er [M
io. €
/a]
turnover medium- & large-scale plants [Mio. €/a]
turnover - small-scale plants [Mio. €/a]
primary energy consumption [PJ/a]
261%
203%
expected average annual market growth rate: 8.3% p.a.
2008 2020
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BIOENERGIESYSTEME GmbHInffeldgasse 21b, A-8010 Graz
Biomass combustion technologies Biomass combustion technologies ––classification by capacityclassification by capacity
Small-scale biomass combustion systemscapacity range: <100 kWth
Medium-scale combustion systemscapacity range: 100 kWth to 20 MWth
Large-scale combustion systemscapacity range: >20 MWth
Co-firing of biomass in coal fired power stationscapacity range: some 100 MWth
Biomass Combustion• most advanced conversion technology• market proven applications for a broad range of fuels and plant
capacities
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BIOENERGIESYSTEME GmbHInffeldgasse 21b, A-8010 Graz
Biomass combustion technologies Biomass combustion technologies ––overviewoverview
secondaryair
ash
fuel
ash
primary air
fixed bed combustion(grate furnace)
fuel
bubbling fluidisedbed combustion
circulating fluidisedbed combustion
fuel
fuel +
ash
bedmaterial
bedmaterial
ashash
pulverised fuelcombustion
bed materialfuel
primary air primary air
secondaryair
secondaryair
freeboard
secondaryair
primary air
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BIOENERGIESYSTEME GmbHInffeldgasse 21b, A-8010 Graz
SmallSmall--scale biomassscale biomasscombustion systemscombustion systems
Application:residential heating
Technologies:wood stoves
wood chip boilerswood pellet boilerswood log boilersheat storing stovesfire-place inserts
Fuels used:log woodwood chipspellets
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BIOENERGIESYSTEME GmbHInffeldgasse 21b, A-8010 Graz
MediumMedium--scale biomassscale biomasscombustion systemscombustion systems
Technologies:underfeed stokers
dust burnersgrate-fired systems
Fuels used:wood chipsbarkforest residueswaste woodstraw
flue gas
secondaryair
fuel
primary air
Application:district heatingprocess heating and coolingCHP production
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BIOENERGIESYSTEME GmbHInffeldgasse 21b, A-8010 Graz
LargeLarge--scale biomassscale biomasscombustion systemscombustion systems
Application:CHP productionpower production
Technologies:
fluidised bedsgrate-fired systems
Fuels used:barkforest residueswaste woodstraw, cerealsfruit stones, kernels, husks, shells
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BIOENERGIESYSTEME GmbHInffeldgasse 21b, A-8010 Graz
Biomass coBiomass co--firing in coal firing in coal fired power stationsfired power stations
Application:power productionCHP
Technologies:co-firing of finely milled biomass mingled with coal
Fuels used:forest residuessawdust, wood chipspelletsstrawfruit stones, kernels, husks, shells
biomass co-firing in fluidised bed combustion systemsco-firing in separate combustion units and junction of steambiomass gasification and utilisation of the product gas as fuel in acoal combustion system
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BIOENERGIESYSTEME GmbHInffeldgasse 21b, A-8010 Graz
Chemical compositions ofChemical compositions ofdifferent different ““conventionalconventional”” solid biomass solid biomass
fuels fuels –– ash, S, Cl, Kash, S, Cl, K
mean values and standard deviations; d.b. … dry basis
ash content wt% (d.b.)
0
2
4
6
8
Woodchips
Bark Straw Wastewood
S mg/kg (d.b.)
0
400
800
1,200
1,600
Woodchips
Bark Straw Wastewood
Cl mg/kg (d.b.)
0
2,000
4,000
6,000
8,000
Woodchips
Bark Straw Wastewood
K mg/kg (d.b.)
0
4,000
8,000
12,000
Woodchips
Bark Straw Wastewood
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BIOENERGIESYSTEME GmbHInffeldgasse 21b, A-8010 Graz
Chemical compositions ofChemical compositions ofdifferent different ““newnew”” solid biomass fuels solid biomass fuels ––
ash, S, Cl, Kash, S, Cl, K
mean values and standard deviations; d.b. … dry basis; SRC ... short rotation coppice
ash content wt% (d.b.)
0
1
2
3
4
Woodchips
Miscan-thus
Poplar(SRC)
Maizecobs
S mg/kg (d.b.)
0100200300400500600
Woodchips
Miscan-thus
Poplar(SRC)
Maizecobs
Cl mg/kg (d.b.)
0500
1,0001,5002,0002,500
Woodchips
Miscan-thus
Poplar(SRC)
Maizecobs
K mg/kg (d.b.)
01,0002,0003,0004,0005,000
Woodchips
Miscan-thus
Poplar(SRC)
Maizecobs
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BIOENERGIESYSTEME GmbHInffeldgasse 21b, A-8010 Graz
Chemical compositions ofChemical compositions ofdifferent different ““conventionalconventional”” solid biomass solid biomass
fuels fuels –– relevant guiding parametersrelevant guiding parameters
Indicator for corrosion risk Indicator for embedding of S+Cl in the ashes and SO2/HCl emissions
Indicator for slagging behaviour Indicator for aerosol formation
2S/Cl mol/mol
05
10152025
Woodchips
Bark Straw Wastewood
(K+Na)/(2S+Cl) mol/mol
0
1
2
3
4
Woodchips
Bark Straw Wastewood
Si/(Ca+Mg) mol/mol
02468
10
Woodchips
Bark Straw Wastewood
mean values and standard deviations; d.b. … dry basis
K+Na+Zn+Pb mg/kg (d.b.)
02,0004,0006,0008,000
10,000
Woodchips
Bark Straw Wastewood
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BIOENERGIESYSTEME GmbHInffeldgasse 21b, A-8010 Graz
Chemical compositions ofChemical compositions ofdifferent different ““newnew”” solid biomass fuels solid biomass fuels ––
relevant guiding parametersrelevant guiding parameters
Indicator for corrosion risk Indicator for embedding of S+Cl in the ashes and SO2/HCl emissions
Indicator for slagging behaviour Indicator for aerosol formation
mean values and standard deviations; d.b. … dry basis;SRC ... short rotation coppice
2S/Cl mol/mol
05
10152025
Woodchips
Miscan-thus
Poplar(SRC)
Maizecobs
(K+Na)/(2S+Cl) mol/mol
0
1
2
3
4
Woodchips
Miscan-thus
Poplar(SRC)
Maizecobs
Si/(Ca+Mg) mol/mol
012345
Woodchips
Miscan-thus
Poplar(SRC)
Maizecobs
K+Na+Zn+Pb mg/kg (d.b.)
01,0002,0003,0004,0005,0006,000
Woodchips
Miscan-thus
Poplar(SRC)
Maizecobs
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BIOENERGIESYSTEME GmbHInffeldgasse 21b, A-8010 Graz
Ash related problems in biomass Ash related problems in biomass combustion processescombustion processes
Fine particulate emissions
Ash melting / slagging and fouling
Corrosion
Additives to reduce ash related problems
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BIOENERGIESYSTEME GmbHInffeldgasse 21b, A-8010 Graz
Influence of the fuel usedInfluence of the fuel usedon the mass of aerosols formedon the mass of aerosols formed
• Emissions at boiler outlet• Summary of the data gained during the test runs mentioned in the previous slides
grey regions: experiences from other projects• Particle emissions related to dry flue gas and 13 vol% O2
10
100
1.000
100 1.000 10.000 100.000concentration of aerosol forming elements in the fuel (K+Na+Zn+Pb)
[mg/kg (d.b.)]
parti
cles
<1
µm (a
e.d.
) [m
g/N
m³]
softwoodhardwoodbarkwaste woodstraw
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BIOENERGIESYSTEME GmbHInffeldgasse 21b, A-8010 Graz
Average chemical compositions of aerosolsAverage chemical compositions of aerosolsfrom smallfrom small--scale biomass boilers and stoves scale biomass boilers and stoves
Appropriate fuel selection relevantPrimary measures of great relevance(complete combustion, reduction of the release of ash vapours)Aerosols with high non-carbonate carbon contents are of health relevance
0%
20%
40%
60%
80%
100%
full load 50%load
full load 50%load
full load 50%load
full load full load
modern pellet boilers modern wood chip boilers modern logwoodboilers
oldstoves
modernstoves
wt%
(d.b
.)
alkalimetal sulfate alkalimetal chloride alkalimetal carbonate oxides non-carbonate carbon
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0
5
10
15
20
25
30
35
40
0 200 400 600 800 1.000
organic gaseous carbon (OGC) content in the flue gas [mg/MJ (NCV)]
orga
nic
carb
on (O
C) c
onte
nt in
aer
osol
s [m
g/M
J (N
CV)
]
0
1
10
100
1.000
10.000
1 10 100 1.000 10.000
organic gaseous carbon content (OGC) in the flue gas [mg/MJ (NCV)]
PAH
con
tent
in a
eros
ols
[µg/
MJ]
(NC
V)
OC and PAH content in aerosols versus OC and PAH content in aerosols versus OGC content in the flue gas for small scale OGC content in the flue gas for small scale
combustion of wood fuelscombustion of wood fuels
Explanations: PAH … polycyclic aromatic hydrocarbons defined according to EU directive 2004/107/EC
r2=0.98statistically significant correlation (p<0.05)
r2=0.88statistic trend(p<0.10)
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BIOENERGIESYSTEME GmbHInffeldgasse 21b, A-8010 Graz
Prediction of ash melting Prediction of ash melting ––results from TGAresults from TGA--DSC analyses and DSC analyses and
thermodynamic equilibrium analysesthermodynamic equilibrium analyses
Formation of molten phases – results from thermodynamic equilibrium analyses (left) and the influence of heavy metals on the melting temperatures of Cl-containing ash mixtures (right)
Appropriate fuel selective design and process control relevantUtilisation of new prediction tools importantFurnace cooling relevant (flue gas recirculation, grate, walls)
K2SO4
+ carbonate
+ chlorideK, Na, SO4, Cl
+ Pb
+ Zn196oC
609oC
1068oC
643oC
Tem
pera
ture
[o C]
K2SO4
+ carbonate
+ chlorideK, Na, SO4, Cl
+ Pb
+ Zn196oC
609oC
1068oC
643oC
Tem
pera
ture
[o C]
0%
20%
40%
60%
80%
100%
200 400 600 800 1,000 1,200 1,400 1,600temperature [°C]
mol
ten
phas
es [w
t%]
straw combustionbark combustion
15 wt% molten phase
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thickness of ash layer[mm]
Measurement and CFD modeling of ash Measurement and CFD modeling of ash deposit formationdeposit formation
Surface temperature[°C]
Ash deposit layer on a water-cooled deposition probe (left) compared with CFD simulations performed (middle) and influence of ash depositions on the surface temperatures (right); explanations: bulk flue gas temperature: 1,050 °C, clean probe surface temperature: 590 °C; figures at the top ... top view; figures at the bottom ... side view
4.03.83.63.43.23.02.82.62.42.22.01.81.61.41.21.00.80.60.40.20.0
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Ash related problems in biomass Ash related problems in biomass combustion processes combustion processes ––
corrosioncorrosionSolid phase reactions involving alkali metal and heavy metal chlorides2 KCl(s) + SO2(g) + 1/2 O2(g) + H2O(g) → K2SO4(s) + 2 HCl(g)
highly relevant (active oxidation)
Reactions involving molten alkali metal and other chloridesrelevant
Fuel selection relevantHighest allowable temperatures on boiler tube surfaces and inlet temperatures of flue gas in convective boiler section relevantBoiler cleaning relevantUtilisation of additives interestingDevelopment towards increased steam parameters as a driving force
straw: 540 °Cwood chips: higher than 540°C
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BIOENERGIESYSTEME GmbHInffeldgasse 21b, A-8010 Graz
Ash related problems Ash related problems ––case study for appropriate case study for appropriate
technological solutionstechnological solutions
Source:
CHP plant MariboCHP plant Maribo--SakskSakskøøbing (Denmark)bing (Denmark)Main fuel: Wheat strawSteam pressure: 92 barSteam temperature: 542 °CPower output (gross): 10.6 MWThermal output: 20 MWElectric efficiency (gross): 31.7 %Thermal plant efficiency: 60 %Total plant efficiency: 91.7 %
Superheaters operated in slagging mode
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Gaseous emissions Gaseous emissions --NONOxx
Fuel selection relevant
Primary measures especially relevant
Combination of primary and secondary measures if needed
0
100
200
300
400
500
600
0.01 0.10 1.00 10.00
Fuel N [wt% (d.b.)]
NO
X em
issi
on
[mg/
Nm
³, dr
y flu
e ga
s, 1
3 vo
l% O
2 ] woodSRC (poplar, miscanthus)waste wood and chipboardnut shellswheat strawwhole crops (triticale)grasses (arundo, cynara)
0%
10%
20%
30%
40%
50%
60%
70%
80%
0.01 0.10 1.00 10.00
Fuel N [wt% (d.b.)]w
t% o
f fue
l-N c
onve
rted
to
N in
NO X
em
issi
on
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0
100
200
300
400
500
600
700
800
0.3 0.5 0.7 0.9 1.1 1.3 1.5 air ratio in the PCC
NO
x em
issi
ons
[mg/
Nm
3 (dry
flue
gas
; 13%
O2)
]
NONOxx emissions versus air ratio in the emissions versus air ratio in the primary combustion chamberprimary combustion chamber
Explanations: results of test runs performed at a 180 kW moving grate pilot plant; fuel used: chipboard (N content: 3.6 wt% d.b.); average boiler load: 150 kW; Rec. … flue gas recirculation; PCC … primary combustion chamber; T prim … temperature at outlet of the primary combustion chamber; d.b. … dry base; the air ratio in the PCC is calculated from fuel and oxidizing agents supplied (air, recirculated flue gas)
blue: Rec. above grate; T prim=1,000 °Cgreen: Rec. below grate; T prim=1,000 °C
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NO [ppmv] N2 net production rate [kg/m3s]
Measurement UnitCO 7.5 ± 10.2 4.5 ppmV d.b.NO 391.5 ± 68.0 417.4 ppmV d.b.NO2 - 8.4 ppmV d.b.NH3 - 1.6 E-07 ppmV d.b.HCN - 3.5 E-05 ppmV d.b.
Simulation Profiles of NO and N2 net production rate (indicator for NOx reduction) in a biomass grate furnace and comparison measurement/simulation Explanations: nominal thermal load 440 kWth; fuel fibre board, fuel nitrogen content 6.5 [wt.% d.b.]
CFD simulation of NOCFD simulation of NOxx formation formation ––grate furnacegrate furnace
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CFD simulation of CFD simulation of biomass combustion plants biomass combustion plants ––
model overviewmodel overview
Models for solid biomass conversionSingle particle conversion and volatiles releaseMultiphase modelling for particle-particle and particle-gas interactions in packed beds (and entrained flows)
Finite cell model for convective heat exchangers
For fire tube boilers, water tube and steam boilers, thermal oil boilersConsideration of flow, heat transfer, pressure distribution; calculation of tube surface temperaturesLink with ash deposit model (in progress)
Models for gas phase combustion and NOx formationTurbulence modelsTurbulence-chemistry interaction modelsReaction mechanisms
Models for ash deposit and aerosol formation
Direct wall condensation, deposition of fly ash particlesAerosol formation and depositionErosionDeposit growth and influence on heat transfer
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Intelligent process control systems for Intelligent process control systems for biomass combustion plantsbiomass combustion plants
Still a high potential for optimisation is given.
Currently applied control strategies• mostly a decentralised structure
(one input variable is coupled with one output and controlled separately)• they do not consider the coupled and non-linear nature of control
loops in biomass furnaces• do not utilise the full potential of well engineered plants
Most promising future approach: model based control strategies
+ consideration of essential physical characteristics of biomass furnaces
+ well established theory for the controller design
+ state-of-the-art control methods for nonlinear systems can be applied
- labour-intensive if no applicable mathematical model is available
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Comparison of conventional and model Comparison of conventional and model based control strategies based control strategies -- feed temperature feed temperature
at a stepwise increase of the set pointat a stepwise increase of the set point
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Ongoing research and Ongoing research and future R&D topicsfuture R&D topics
State of science Future R&D
conventional biomass fuels(wood fuels, straw)
new biomass fuelsshort rotation crops, agricultural residues, torrefied materials, hydrolytic lignin, pyrolysis char
modern biomass combustion technologies
next generation biomass combustion systemstowards zero emission technologiestowards new process control systems
conventional CHP technologies
advanced highly efficient systemstowards increased steam parameterstowards higher availability
single model development virtual biomass conversion plant
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BIOENERGIESYSTEME GmbHInffeldgasse 21b, A-8010 Graz
Thank you for your attentionProf. Dr. Ingwald Obernberger
Inffeldgasse 21b, A-8010 Graz, AustriaTEL.: +43 (316) 481300; FAX: +43 (316) 4813004
Email: [email protected]: http://www.bios-bioenergy.at
Please visit our stand outside the
auditorium!