Fixed Bed Gasification of Steam Treated Food Waste
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Fixed Bed Gasification of Steam
Treated Food Waste (FW) and
Municipal Solid Wastes (MSW)
Abdullah Malik
University of Northumbria at Newcastle UK
Simon Carves Ltd UK
What is Discussed
Today?
Development of R&D Gasification Set-
up at UET Lahore
STRAP Schematics
Hybrid Gasification Process
Key Test Results
Future Work
Objectives of Gasification
Project at UET, Lahore
To construct a gasification research and
development pilot plant facility – 100 kg/h
To demonstrate the utility of various fuels and
their performance for energy conversion
To demonstrate power generation using
synthesis gas
Major Stages of Project
1. Process Design
2. Fabrication & Procurement of Pilot Plant
Accessories
3. Testing & Operation
4. Experimentation to Establishing performance
5. Demonstration of Electrical Power Generation
6. Development of Fuel Testing Facilities
7. Design & Fabrication of Desktop Gasifier to Study
the Effect of Design Innovations and Various
Fuels
Simplified Process Flow
Scheme
Synthesis gas generation and clean up
Gasifier Scrubber Flare
Wood
Water Clean
Syngas
Air
Water
Filtration
Ash
Facility Developed at Chemical
Engineering
Downdraft
Gasifier
Wet Blower
Scrubber
Water Recycle
Recirculation Pump
Tank
Gasifier Reactor
Manual Ash Agitating
Device
Intensified Spray
Scrubber
Water Re-circulation Tank
Induced Draft Fan
3. Testing & Operation
Cold testing
Hot testing
Instrument Calibration
Test runs
4. Experimentation to establish
performance
Wood.
Coal (Charcoal).
Shredded Tires.
Poultry Waste + Rubber
crumbs.
Palletized Agriculture
Residue.
Rice Husk
Lignite
Steam Treated FW and
MSW
Steam Treatment Recycling and
Power (STRAP) Process
Steam Boiler Operates Heat Recovery
Using Heat Recoverd and Exhaust
8
Power Generation
Gasification System
System
Waste Fed Directly 1
Air
to Autoclave
Power to export
Steam 4
Autoclave 2 3
Clean Water
Bio Effluent recovered
Recyclable Materials Treatment
Recovered Air
Via Separation 6
Trommel
7 Ash Sent to Form Part
of Aggregate Post Conditioning
Hybrid Gasification
Process
HGL Gasifier Key
Features
• Offers uniform airflow through the fuel bed when fuel
is allowed to flow under gravity without any
constriction.
• Hybrid gasification design has accommodated all the
features required for a perfect gasification unit to treat
difficult residues with variable ash composition.
• This makes it suitable for a wide variety of solid
biomass feed stocks.
Gasifier Zones
The gasification process can be divided
into three main zones
Fuel feeding zone – Top one third
Fuel gasification zone – Middle one
third
Ash discharge zone – Bottom one third
Syngas using FW
Square Briquettes
Density Measurements
Absolute density Bulk density
(kg/m3) (kg/m3)
MSW* 816 452
FW* 822 535
Wood chips 836 250
Proximate Analysis
As received* Dry basis* Dry ash free basis*
MSW FW Wood MSW FW Wood MSW FW Wood
Moisture (%) 50.9 29.3 16.66 - - - - - -
Volatile matter (%) 18.8 68.33
51.1 38.2 72.4 82 71 77.8 83.67
Fixed carbon (%) 7.6 13.33
14.6 15.5 20.7 16 29 22.2 16.33
Ash (%) 22.7 1.66 - - -
4.9 46.3 6.9 2
Ultimate Analysis
MSW FW* Wood Anthracite
Carbon (%) 36.35 56.65 43.43 88.9
Hydrogen 4.96 8.76 6.08 3.4
(%)
Oxygen (%) 10.13 23.54 46.29 2.3
Nitrogen 1.43 3.95 0.67 1.55
(%)
Sulfur (%) 0.83 0.19 0.43 0.81
Ash 46.3 6.9 3.11 3.04
CV (MJ/kg) 9.35 26.33 15.15 34.37
Heavy Metal
Concentration
Elements Concentration in FW Concentration in MSW
(µg/g)* (µg//g)*
Mercury <2 2.3
Cadmium < 0.7 1.2
Arsenic <1 <1
Chromium < 15 < 15
Titanium 344.1 2874
Lead 15.4 755.7
Ash Softening
Temperature
Food Waste – 1357 oC
MSW – 1297 oC
Typical Syn-gas
Composition from Air
Gasifiers
Component Vol%
CO 12 to 16
H2 10 to 12
CH4 1 to 3
CO2 10 to 12
N2 40 to 50
O2 <1
H/C ~1 to 2
Average Gas
Composition
FW MSW
CO2, vol % 7.50 8.95
H2O, vol % 1.72 2.05
CO, vol % 12.11 4.49
CH4, vol % 3.27 2.24
C2H2, vol % 1.63 1.12
C2H4, vol % 3.27 2.24
H2, vol % 13.9 6.21
N2, vol % 56.6 72.7
CV, MJ/m3 7.61 4.31
Temperature Monitoring
Gasification zone
Ash Zone
Syngas
Demonstration of Electrical Power
Generation
Conclusions & Way
Ahead
A R&D facility is developed and being used
for various MSc and PhD studies
STRAP concept is expected to be a
successful way forward – further work is
continuing
A novel gasifier to treat difficult solid residue
is developed and patent application is in
progress.
Development of commercial scale STRAP
facility is currently being pursued in UK
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