development of fuel flexible heat and power production based on fluidized … · 2011-01-20 ·...
TRANSCRIPT
Development of fuel flexible heat and power
production based on fluidized bed technology
Jouni Hämäläinen, Technology manager, VTT
E-mail: [email protected]
Pre-Conference for Baltic Sea Region Conference 2010
Jyväskylä, Finland, 30th of November 2010
Jyväskylän Paviljonki
214/12/2010
VTT Technical Research Centre of Finland
VTT IS
the largest multitechnological applied research
organisation in Northern Europe
VTT HAS
polytechnic R&D covering different fields of
technology from electronics to building
technology
clients and partners: industrial and business
enterprises, organisations, universities and
research institutes
VTT CREATES
new technology and science-based innovations in
co-operation with domestic and foreign partners
Turnover 280 M€ (budget for 2010)
Personnel 2,900 (1.1.2010)
78% with higher academic
degree
6,500 customers
Established 1942
VTT has been granted
ISO9001:2000 certificate.
314/12/2010
VTT - Diverse and sustainable energy research
Provides almost 400 energy experts
Provides modern experimental facilities, pilot plants and calculation tools
Synergy with other VTT competencies
Networks - national & international
Key focus of technology developments: Cost-effective and zero-emission heat and power production
Bioenergy - especially combined heat and power (CHP) Wind power – especially for cold climate conditions Nuclear energy – safety, plant life management, nuclear
waste management and geological disposal, Generation IV nuclear technologies
Efficient and optimized use of biomass resources Focus on forest residues and waste
Clean fossil fuels Carbon Capture and Storage (CCS) in Fluidized Bed
Combustion (FBC) Synthetic fuels for transportation, energy savings through
use of electricity in hybrid cars
VTT pursues versatile energy research, from nuclear to renewables. Energy economy, energy
systems and reduction of emissions also form a crucial part of our energy research.
414/12/2010
World primary energy demand until 2030. Ref. Coal in the
IEA World Energy Outlook 2006 - The Importance of Clean
Coal Technologies in China, Brian Ricketts Coal Energy
Analyst, IEA.
~ 40% increase
between 2005 and 2030
Total primary energy supply (2006)
Totally 67%
Total electricity generation (2006)
Totally 81%
World energy today and
forecast
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CO2 reduction in energy production
The approaches to CO2 emission
reduction in the energy production are
as follows:
Use of CO2 neutral energy sources:
biomass, nuclear power, wind, solar etc.
Use of fuels with lower CO2 impact:
shift from coal to natural gas
Biomass for power or Co-firing of
fossil fuels with CO2-neutral fuels
provides a technically and economically
feasible solution for CO2 reduction up to
certain degree.
Increase of efficiency provides emission cuts proportional to the rise in efficiency
CCS, Carbon Capture and Storage technologies, potential for near zero emission
power production from fossil fuels.
614/12/2010
Content of the presentation
G
ALKALISILICATES,SULPHATES
ALKALICHLORIDES
O
SULPHUR DIOXIDE, Al-SILICATES
C
FOREST RESIDUE PEAT
Co-combustion
Heat transfersurface
Lack of protecting
compounds
Low ash content
ALKALICHLORIDES
BARK/FOREST RESIDUE
By M. Aho, VTT
1. Shortlly about fluidized bed combustion (FBC) technology and VTT’s activities in
FBC related research and development especially in biomass fuel combustion
2. Some recent results achieved and new innovation based on our expertise
3. New applications and tools for improving power plant performance in biomass
combustion
4. Conclusions
Research activities and developing
technologies for biomass combustion
is more or less understanding high
temperature chemistry of ash behaviour
The understanding of that will lead to
solutions for plant designs and power
plant operators. Target of this presentation
is to give a view that interaction of fuel
mixture (or use additives) really has an
effect of combustion and ash behaviour
process
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Source: Metso Power
Fluidised Bed Combustion (FBC) technology has advantage to burn simultaneously various kind of fuels from coal to biomass and mixtures of different fuels
Variations in fuel particle size or in moisture content does not have a large effect on combustion process because of stability of fluid bed behaviour (huge amount of bed material in process = stabilize combustion)
However, the fuels spectrum has come and will come more wider in the future. Challenge is to optimise fuel mixture to prevent unwanted fuel ash behaviour (deposition and corrosion) during combustion or to find another ways to control combustion chemistry.
The fuel flexibility of the technology will give great advantage in the markets
Fluidized bed combustion technology
Targets of development in FBC technology
scaling up and increasing efficiency
improving environmental performance
widening (still) the fuel flexibility, agrobiomass, short
rotation energy crops
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1. Fluidized bed combustion characterisation test services
High-class, unique experimental pilot and bench scale FB testing environment
Well-established procedures for testing, analysing and reporting
2. Challenging fuels and ash chemistry in multifuel operation
Advanced sampling techniques, control, manipulation and modelling tools for ash chemistry
Effects of fuel quality and combustion conditions on ash related problems
Novel tools for fouling and high temperature corrosion monitoring, boiler economy evaluation and process simulations
Boiler availability and diagnostics at different operation conditions
3. In-furnace phenomena in air and oxyfuel fluidized bed combustion
World-class oxyfuel FB combustion research facilities
Combining of experimental results and process knowledge into rigorous combustion modelling tools
Fluidized bed combustion reseach at VTT
On this R&D&I field we have
turnover about 5 milj.€ at VTT
in Jyväskylä
- Direct industrial funding 30%
- Funding from public sources 45%
- VTT’s own funding 25%
914/12/2010
Fuel capacity ~50 kW
Riser height 8 m, diameter 17 cm
Option for fuel feed with two separate feeding lines
Option for fuel additive feed with a separate feeding line
Option for gas and solid matter sampling as a function of riser height
Fly ash sampling after both cyclones
Deposit probe measurements
Particle size analyses
Combustion conditions fully controlled
Several lab or pilot scale combustion
units: example CFB reactor
R&D topics in combustion
Understanding in furnace phenomena under FB combustion
Combustion profiles
Gas, solids, temperature
Heat transfer inside combustor
Emission formation
Ash behaviour characteristics
Aerosol sampling inside furnace
Formation and analysis of deposition
Combustion control studies
1014/12/2010
Major challenges in biomass combustionThere already exists lot of experience and knowledge about forest fuel
combustion (Scandinavian fuels). The trend today is, however, towards
agrobiomass fuels, fast growing, short rotation biomass fuels like
Miscanthus sinensis
Eucalyptus, bagasse
Rice husk, willow and other energy wood feedstocks
Industrial by-products, etc…
In general the major challenges with biomass
fuels are in fuel feeding and burning properties
Stability of fuel mass flow
Ash behaviour due to high alkalines,
chlorine etc.
However, the “new” biomass fuel fractions
has specific characteristics due to higher
alkaline, chlorine, potassium and some
heavy metal content → boiler design for
those fuel will be the future challenge –
but very feasible
In cooperation with industry VTT is developing and demonstrating new designs for boilers andnew concepts for energy markets
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To stack
Sampling port
Sampling port
Sampling port
Gas cooling
Bagfilter
Gas probe
Observationport
Cyclone
Gas sample
Temperature control
Tertiary air optional
Tertiary air optional
Tertiary air (preheated)
Fuel container 2Fuel container 1
Secondary air(preheated)
Nitrogen
Air
Additivecontainer
Primary gas heating
Heating zone 2/Cooling zone 2
Heating zone 3
Heating zone 4
Heating zone 1/Cooling zone 1
BEDmade of quarz
PC control and data logging system
Obervation port
Obervation port
Obervation port
Obervation port/Deposit probe
Deposit probe
VTT’s expertise on this field Offering pilot scale R&D devices to study combustion phenomena
- Stable combustion conditions achievable
- In furnace sampling of gas, solid, aerosols. Measurement of temperature
and pressure profiles – able to go inside the process
- High-level sampling technologies for fine particulates at high temperature
- Development of modelling tools for ash behaviour chemistry
CorroStop®: Method for preventing chlorine deposition
on the heat-transferring surfaces of a boiler. Aho, Martti Pat.
WO2006134227
CorroStop – water soluble liquids
- Aluminium sulphate Al2(SO4)3 and ferric sulphate
Fe2(SO4)3 as 25 % water solutions
0
100
200
300
400
500
600
0.01 0.1 1 10
Particle Diameter Dp [µm]
dm
/dlo
g(D
p)
[mg
/Nm
³]
0
100
200
300
400
500
600
700
0.01 0.1 1 10
Particle Diameter Dp [µm]
dm
/dlo
g(D
p)
[mg
/Nm
³]
AEROSOLS FROM ALKALINE CHLORIDES CAN
BE BIND IN NON-HARMFUL PHASE USING ADDITIVES
Before After
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Based on understanding of ash chemistry VTT has got a trademark for CINDY CFBC®-Chemically active (coal) minerals are able to effect on biomass or waste derived aerosols
Biomass or waste Coal CINDY CFBC®
Chemically reactive mostly inert alkalines cocombustion process
alkalines etc. → no corrosive FUEL INTERACTION!
0
100
200
300
400
500
600
0.01 0.1 1 10
Particle Diameter Dp [µm]
dm
/dlo
g(D
p)
[mg
/Nm
³]
0
1000
2000
3000
4000
5000
6000
0.01 0.1 1 10
Particle Diameter Dp [µm]d
m/d
log
(Dp
) [m
g/N
m³]
0
500
1000
1500
2000
2500
0.01 0.1 1 10
Particle Diameter Dp [µm]
dm
/dlo
g(D
p)
[mg
/Nm
³]
Corrosive
alkaline salts
@ 780°C
Sorption + chemical reaction:
Al2Si2O5(OH)4 …
2KCl + Al2Si2O7 + H2O K2O·Al2Si2O7 + 2HCl
1314/12/2010
15 %
20 %
25 %
30 %
35 %
40 %
45 %
50 %
350 400 450 500 550 600 650 700
Steam temperature, °C
Ele
ctr
ic e
ffic
ien
cy,
%
Grate fired CHP waste incinerator
420°C, 60bar
Fluidised bed CHP plant for waste
470°C, 65bar
Ultra super critical pulverised coal fired condensing
power plant, 700°C, 330bar
Super critical coal fired condencing power plant, fluidised bed
580°C, 275bar
Grate firing for MSW
Fluidised bed for SRF
Biomass
combustion
Coal fired condencing mode
power plants
Grate fired CHP plant for biomass
500°C, 70bar
ADCOF TARGET AREA:
Fluidised bed CHP plant for biomass,
520°C, 120bar
15 %
20 %
25 %
30 %
35 %
40 %
45 %
50 %
350 400 450 500 550 600 650 700
Steam temperature, °C
Ele
ctr
ic e
ffic
ien
cy,
%
Grate fired CHP waste incinerator
420°C, 60bar
Fluidised bed CHP plant for waste
470°C, 65bar
Ultra super critical pulverised coal fired condensing
power plant, 700°C, 330bar
Super critical coal fired condencing power plant, fluidised bed
580°C, 275bar
Grate firing for MSW
Fluidised bed for SRF
Biomass
combustion
Coal fired condencing mode
power plants
Grate fired CHP plant for biomass
500°C, 70bar
ADCOF TARGET AREA:
Fluidised bed CHP plant for biomass,
520°C, 120bar
®DOUBLING THE ELECTRIC EFFICIENCY IN WASTE-TO-
ENERGY by utilising the capability of coal ash to adsorb:
and chemically react with the waste-originated salts ending to a complete absence
of halogen salts in the combustion gases wherefrom the energy can be recovered with
electric efficiency of 40%.
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Development of monitoring tools for power plant operators to
improve plant performance
Development of on line-monitoring, diagnostic and calculation methods to optimize multifuel operation at power plants
On-line monitoring of ash deposition
Long-term measurements of corrosion characteristics
Methods for process analysis to improve plant operation (availability and reliability)
Currently in semicommercial application, installed on several power plants by VTT
New innovations and patents on analysis of fluid bed behaviour and on-line measurement of heat transfer inside the furnace
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Information to customer:
• On-line deposition monitoring
• Monthly reporting system
• HelpDesk-service
Technical concept for power plant monitoring toolbox
On-line monitoring probe
Probe cooling unit
Measurement system Monitoring toolboxMultifuel boiler
• On-line deposition data
• Process data from customers
automation system
• Connection to combustion
process and plant automation
and control system
1614/12/2010
Conclusions
Ten years ago we did not have lot of experience about burning of forest
residues – the first experience revealed problems with fouling of heating
surfaces and risk of high temperature corrosion.
The next step was new designs for biomass boilers (external superheates
into loop seal ie. not to direct contact to flue gas path etc).
Nowadays the use of more challenging biomass sources is increasing –
eucalyptus, agrobiomass fuels, fast growing energy wood etc. These new
fuels have lot of new challenges due to ash related understanding.
Lot of new understanding is however available and hopefully after 10
years we are able to say that agrobiomass fuels and fas growing energ
wood was a challenge in 2010 but now we have …..
1714/12/2010
Thank You for your attentionFurther questions or contact
Jouni Hämäläinen tel. +358 40 5211066 or
VTT creates business from technology