The Fuel and Energy Research Forum SCAPE PRESENTATION · The Fuel and Energy Research Forum SCAPE...
Transcript of The Fuel and Energy Research Forum SCAPE PRESENTATION · The Fuel and Energy Research Forum SCAPE...
Slide of 19 1
SCAPEThe Fuel and Energy Research Forum
Ignition Risk from Biomass Dust Layers
PRESENTATIONThe Fuel and Energy Research Forum SCAPE
Ignition Risk of Biomass
Dust Layers
- Washing Pre-treatment on Low
Temperature Ignition of Biomass
Yee Sing ChinJenny M Jones
Slide of 19 2
SCAPEThe Fuel and Energy Research Forum
Ignition Risk from Biomass Dust Layers
Background/Introduction
• Biomass
– with increase usage of renewables, UK power sector reduced carbon emissions by 13% between 2014-2015*
– a promising renewable energy source for power generation
– a reactive solid fuel
– capable of self-heating, eventually self-ignition, leading to catastrophic fire
* REF: Energy in the UK 2016 – Delivering jobs, growth and choice through sustainable investment in 2015
Slide of 19 3
SCAPEThe Fuel and Energy Research Forum
Ignition Risk from Biomass Dust Layers
Background/Introduction
• History of biomass fires…
Fire Incidents
2011
- Pinnacle Pellet in
Armstrong, British
Columbia 2011
- Shur Fire Energy
Norwich
2011
- Port of Tyne2012
- Laurinburg Nature’
Earth Plant, North
Carolina
2012
- RWE npower , Tilbury
2013
- Port of Tyne South
Shields
Motivation:
~ fires related to biomass self-combustion and ignition of
combustible biomass dust had led to growing interest in this
research area
Slide of 19 4
SCAPEThe Fuel and Energy Research Forum
Ignition Risk from Biomass Dust Layers
Methodology
• Experiments & Analyses are in accordance with:– BS 50281-2-1 Electrical Apparatus for Use in the Presence
of Combustible Dust – Part 2-1: Test Methods – Methods of Determining Minimum Ignition Temperature
– BS 50281-1-2 Electrical apparatus for use in the presence of combustible dust — Part 1-2: Electrical apparatus protected by enclosures — Selection, installation and maintenance
Procedure of determining TLIT
* TLIT (minimum layer ignition temperature)
Relating TLIT with MPST* MPST (maximum permissible surface temperature)
Slide of 19 5
SCAPEThe Fuel and Energy Research Forum
Ignition Risk from Biomass Dust Layers
– Water-washing pre-treatment
Methodology
Pre-treating Biomass
- 1g Biomass : 5 ml Distilled Water- 500 rpm agitation speed- 60 minutes
Slide of 19 6
SCAPEThe Fuel and Energy Research Forum
Ignition Risk from Biomass Dust Layers
Methodology
Hot Plate Temperature Uniformity Check
Hot plate
Dust Layer Experiment
Free from draught
↑ 16 points temp. check – hot plate temperature is uniform
Adhering to BS EN 50281-2-1 ……
Slide of 19 7
SCAPEThe Fuel and Energy Research Forum
Ignition Risk from Biomass Dust Layers
Methodology
Ring A, 5 mm height
Ring B, 12.5 mm height
Dust Layer TC
Inconel Shielded
TC
Adjustment
Nut
Adhering to BS EN 50281-2-1 ……
Slide of 19 8
SCAPEThe Fuel and Energy Research Forum
Ignition Risk from Biomass Dust Layers
Methodology
• Dust Layer Ignition Experiment*
Materials Preparation
Equipment Placement &
Setup
• BS: Materials pass through 200 µm aperture• This study: materials milled & sieved using 180µm sieve
Dust Layer Rig
Fume Extraction
* BS EN 50281-2-1. Electrical Apparatus for Use in the Presence of Combustible Dust – Part 2-1: Test Methods – Methods of Determining Minimum Ignition Temperature.
Slide of 19 9
SCAPEThe Fuel and Energy Research Forum
Ignition Risk from Biomass Dust Layers
Methodology
• Dust Layer Ignition Experiment
Experimental Procedure
•Hot plate set at estimated ignition temperature• Fill ring cavity & level off (all within 2 minutes)• Timer & recorder started once dust is levelled off• Ignition – lowest temperature when visible glow is seen ~ TLIT
• Experiments in multiples of 10oC, fresh dust each time• Ignition delay time – time recorder is started to time glow is
observed ~tig
!!! If no ignition observed, wait for
minimum 30 minutes, repeat another 2
times as confirmation
Slide of 19 10
SCAPEThe Fuel and Energy Research Forum
Ignition Risk from Biomass Dust Layers
Results & Discussion - Washing
• TLIT & tig of 8 Water-Washed Materials vs Parent Materials
Washing effects:
Increased the TLIT
by 10-20˚C
- 20˚C for parent materials- 10˚C for blended materials
Parent materials, Pine & Miscanthus
Washed Parent material
Washed 90wt%Pine:10wt%Miscanthus
Washed 50wt%Pine:50wt%Miscanthus
90wt%Pine:10wt%Miscanthus
50wt%Pine:50wt%Miscanthus
Slide of 19 11
SCAPEThe Fuel and Energy Research Forum
Ignition Risk from Biomass Dust Layers
Results & Discussion - Washing
• Acid Digestion – dissolving an untreated sample into its constituent elements with acid & heat reactions
↑ H2SO4 & HNO3 acid digest miscanthus & pine
Focus: Potassium & Calcium elements that are well known for causing fouling at heat convective boiler regions.
Slide of 19 12
SCAPEThe Fuel and Energy Research Forum
Ignition Risk from Biomass Dust Layers
Results & Discussion - Washing
• Atomic Absorption Spectroscopy (AAS) – quantification
of constituent elements
Acid digestates – determine concentrations of two major problematic metal elements, K and Ca that occurred naturally in biomass
Slide of 19 13
SCAPEThe Fuel and Energy Research Forum
Ignition Risk from Biomass Dust Layers
Results & Discussion - Washing
• Distilled Water Washing
- Solid residue taken dust layer test after drying
- Leachates taken for Ion Chromatography (IC)
Slide of 19 14
SCAPEThe Fuel and Energy Research Forum
Ignition Risk from Biomass Dust Layers
Results & Discussion - Washing
• Ion Chromatography
↑ IC on leachates – check elements washed out (removed) from biomass washing
Slide of 19 15
SCAPEThe Fuel and Energy Research Forum
Ignition Risk from Biomass Dust Layers
Results & Discussion - Washing
- decrease of reactivity in washed biomass (increased TLIT) was due to catalytic potassium and calcium elements being washed out of the biomass
In Fuel (mg/kg of Dry Fuel)
Removal (mg/kg of Dry Fuel)
K Ca K+ % K Ca2+ % Ca Cl-
PineC 342 584 130 38 19 3 31
Misc(1) 2998 5409 2709 90 1017 18 2781
Concentration (mg/kg of Dry Fuel) in Untreated Fuels (AAS Analysis) and K, Ca, and Cl Removed (mg/kg of Dry Fuel) during Water Washing (IC Analysis of Leachates)
Slide of 19 16
SCAPEThe Fuel and Energy Research Forum
Ignition Risk from Biomass Dust Layers
Results & Discussions – Risk Ranking
• Thermogravimetric Analysis (TGA) – self-ignition risk ranking (Ea, TMWL)
* Ramírez, A. et al. 2010. Experimental Determination of Self-Heating and Self-Ignition Risks Associated with the Dusts of Agricultural Materials Commonly Stored in Silos. Journal of Hazardous Materials. 175, pp.920-927
4 Risk Categories:
Low risk
Medium risk
High risk
Very high risk
Slide of 19 17
SCAPEThe Fuel and Energy Research Forum
Ignition Risk from Biomass Dust Layers
Results & Discussions – Risk Ranking
• Self-Ignition Propensity Risk Ranking
* Jones, J.M. et al. 2015. Low temperature ignition of biomass. Fuel Processing Technology. 134, pp.372-377
- by TGA slow combustion
Slide of 19 18
SCAPEThe Fuel and Energy Research Forum
Ignition Risk from Biomass Dust Layers
Results & Discussions – MPST
• Industrial Application – Maximum permissible surface temperature (MPST) of an equipment
* BS EN 50281-1-2. Electrical apparatus for use in the presence of combustible dust — Part 1-2: Electrical apparatus protected by enclosures — Selection, installation and maintenance
MPST Estimation with Three Different Methods:
• Points – TLIT less 75K• Curves – BS*, 5 mm TLIT
• Constant at 150°C – Power Station Practice
~ prediction for 12.5 mm thick dust deposits
Slide of 19 19
SCAPEThe Fuel and Energy Research Forum
Ignition Risk from Biomass Dust Layers
Conclusion
• Solid fuel biomass dust deposited on hot surfaces …– TLIT of different species is confined within a narrow range
– Removal of potassium element that is catalytic to combustion upon washing pre-treatment did make the fuel slightly safer with TLIT increase but still showed high self-ignition risk after washing pre-treatment
– Treating the MPST as 75K less than TLIT was the most lenient for thin deposits and 150˚C was most conservative for thin deposits; as dust thickness increases, the 150˚C became the most lenient, opposite to when deposits are thin
– MPST strongly depends on the situation, but regardless of this, thicker dust layers are more hazardous in terms of ignition risk