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MILENA – OLGA - IGCC Most Efficient Energy from Waste Technology
Jan-Willem Könemann
Washington October 27th 2014
Royal Dahlman
• Technology company, established in 1886
• Serving the Oil & Gas and Power market worldwide
• Developing gasification and syngas purification
systems in cooperation with ECN since 2001.
• License Holder of MILENA and OLGA technology
• Developing complete biomass and waste fuelled
IGCCs in cooperation with Synova since 2012
Royal Dahlman & partners
FCC Slurry Oil Filtration Package on transport
2
ETI: Searching the best EfW technology
Worlds most robust and efficient energy from waste technology contest
• The British ETI selected Royal Dahlman and two British companies to compete
in this challenge. These three competitors, selected out many applicants from
all over the world, received funds to support waste gasification tests, a FEED
study and project development work.
• In the coming months the winner will be announced, which will receive an ETI
investment for the commercial demonstration plant.
• Primary goals:
- Commercial deployment scale 5-20 MWe,
- Overall net energy form waste efficiency > 25%
- Availability > 80%
3
MILENA-OLGA-IGCC net efficiency
RDF/SRF to electricity net efficiency
5
Note: The total Energy from waste efficiency, as defined by the ETI, including MRF parasitic and energy content of the fine wet fraction (to digester is approximately 2% lower than the RDF/DRF to energy efficiency
The Grimsby Renewable Power facility
Project Statistics
Project location Moody Lane, Grimsby, Lincolnshire, UK
Plant design capacity (flexibility) 70 to 110% of nominal capacity
Plant commercial feedstock Flexible, designed for RDF - SRF - Biomass
Waste input (at MRF) 60,000 to 80,000 tpa (based on typical MRF operation)
Plant RDF/SRF input 37,000 tpa SRF or 47,000 tpa RDF
Plant input energy 22-23 MW (LHV) at nominal capacity
Plant gross electricity generation 9,4 MW
Plant net electricity sales 7.6 MW
7
Grimsby site
GRP facility MILENA-OLGA-Taurus-60 7 MWe IGCC plant
GRP facility Red outline is lease for 7 MWe plant
GRP facility RDF receipt & storage building
8
Plant layout impression
RDF/SRF receipt building Visitor Centre Existing RWE - NPower plant 7MWe MILENA-OLGA IGCC
9
MILENA – OLGA Most Efficient EFW
MRF The GRP facility receives
RDF/SRF bales from Transwaste, but also has
MRF functionality for flexibility and robustness.
Two shredders, a sieve and magnet belts
MILENA The MILENA scope includes flue gas treatment, coolers
and the cyclones
OLGA - AQUA OLGA (green) captures tars and dust and recycles these
to the MILENA. Downstream OLGA (blue)
water is condensed out and components like HCL and
NH3 are removed
Power Block A Solar/Caterpillar Taurus60 gas turbine, heat recovery
steam generator and a steam turbine that also receives steam from the
MILENA coolers
11
The MILENA gasifier
MILENA an indirect gasifier
• Both reactors in one refractory lined reactor vessel
• 100% carbon to gas ratio
o Resulting in carbon free ash
o Resulting in a 5 - 15% higher cold gas efficiency
typically 75 - 85% excluding tars and NH3
• Separate flue gas exhaust, no or minimized nitrogen
dilution of the product gas
o Compared to air blown gasification a 3 to 4
times higher heating value.
o Compared to oxygen/steam blown gasification
a much higher efficiency (no ASU parasitic),
while still having 60% more heating value
o Very suitable for gas turbines
12
Typical gas compositions
Improved gas quality
Typical applicability Engine: Wobbe > 4, Gas Turbine: Wobbe > 12
Product gas composition
downstream water condensation
(saturated at 30-35 °C)
Specification Sand bed Sand bed Sand bed Sand bed
CO 12.5 28.0 22.0 24.7
H2 11.3 21.6 14.2 15.9
CO2 13.1 29.7 15.8 17.7
O2 0.0 0.0 0.0 0.0
H2O 6.0 6.0 6.0 6.0
CH4 2.9 8.6 15.3 17.2
N2 51.2 0.6 10.9 1.0
CxHy (>CH4 & < toluene) 1.7 3.7 13.9 15.6
Wobbe (LHV, MJ/Nm3) 5.1 12.0 21.8 24.5
Clean Product GasCFB
Air fluidisation
MILENA
Air fluidisation (riser)
MILENA
Steam fluidisation (riser)
CFB
oxygen/steam fluidisation
13
OLGA tar removal
Portugal: CFB gasifier, OLGA gas cleaning,
Caterpillar 3516A+ gas engine
OLGA, a tar/oil based gas scrubber
• OLGA captures tars with high efficiencies, well within specification for gas engines, gas turbines, fuel cells and catalytic processes (SNG, FT-diesel)
• OLGA has low pressure drop and only consumes some electricity for pumps and tracing < 100 kW for a 9000 kW gross plant (<1%)
• OLGA does not change the main gas composition: high energy carriers like methane, ethene and the bulk of the benzene and toluene stay in the product gas
• OLGA is able to handle very high tar loads, up to 50 g/Nm3, allowing us to optimize the MILENA towards CH4 production and efficiency
14
OLGA Experience & Performance
Lab scale pilot ECN Industrial Pilot ECN France
Caterpillar 3516 A+ engines
Portugal
15
Tar analyses
Parameter Unit CFB gasifier
Raw Gas Downstream
OLGA Efficiency
Total tar mg/Nm³ 17,106 171 99.0%
Total tar excl. BTX mg/Nm³ 16,040 63 99.6%
Total tar excl. BTX & unknowns mg/Nm³ 10,349 9 99.9%
Naphthalene (key-component) mg/Nm³ 2,822 < 2.5 > 99.9%
Phenol (key-component) mg/Nm³ 386 < 2.5 > 99.9%
Tar dewpoint ° C > 350 < 15
° F > 660 < 59
Tar aerosols (incl. dust) mg/Nm³ -- 10
16
Tests on refuse derived fuel so far Clean Gas flare
(downstream OLGA) Raw Gas flare
(downstream gasifier)
17
Energy Balance
23,6 MW RDF
3,7 MW electricity
18,1 MW Clean Product Gas
13,3 MW steam
TOTAL NET (RDF to electricity): efficiency 32%,
5,7 MW electricity
Parasitic 1,8 MW
7,6 MW
28%
32%
20
Grimsby development opportunities
The Grimsby facility is the ideal basis
for development of future applications.
Clean product gas is available at
pressure for slipstream tests
21
SNG, green gas, overall efficiency 70%
FT liquid fuels