Professor Rosemary Falcon and Dr Samson Bada DST-NRF SARChI Clean Coal Technology Research group University of the Witwatersrand
ENVIRONMENTALLY RESPONSIBLE METHODS TO MITIGATE THE USE OF COAL IN THE SUSTAINABLE ENERGY MIX. .
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ENVIRONMENTALLY RESPONSIBLE METHODS TO MITIGATE THE USE OF COAL IN - - PowerPoint PPT Presentation
ENVIRONMENTALLY RESPONSIBLE METHODS TO MITIGATE THE USE OF COAL IN THE SUSTAINABLE ENERGY MIX . . Professor Rosemary Falcon and Dr Samson Bada DST-NRF SARChI Clean Coal Technology Research group University of the Witwatersrand 1 CONTENTS 1.
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GLOBAL CONTEXT CFBC Project addresses the UN’S SDGs for a low carbon economy SOCIO-ECONOMIC CONTEXT Modern Coal Developments
economic and social benefits and quality of life for people
expertise required for the technology TECHNOLOGICAL CONTEXT Modern Coal Developments provide
alternative fuels DST CONTEXT aligns with the DST’s Programme 2 + Programme 3 + Programme 4 NATIONAL CONTEXT aligns with NDP’s 3 Phases of Innovation REGIONAL CONTEXT aligns with projects in Botswana, Zimbabwe and Mozambique
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Ref: POLICY ADJUSTED IRP 2010
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The size and mix of the South African power generation capacity pie – 2010 to 2030
Hydro carbons 57% Hydrocarbons 86%
2010 2030
Discards 51.8 Mt Electricity 120.8 Mt
Exports 64.0 Mt
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LOW CARBON ECONOMY IN SA - 1 IRP2010 - SA’S Integrated Resource Plan 2010
The Role of Coal going forward....
The role of coal (% in mix)
86%.......57%
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LOW CARBON ECONOMY IN SA - 2 IRP2010 - SA’S Integrated Resource Plan 2010
The Role of Coal going forward....
The role of coal (MW)
86%.................57 %
7th largest producer of coal in the world 7th largest exporter of coal Major supplier to the Middle East, India and Far East, with some to EU and Africa
Highest foreign exchange earnings in the country each year from 2011 (R50 Billion in 2017) Total coal sales local and export generated R120 billion 2017. Largest mining income earner, beating gold, platinum, diamonds >91% of SA energy production, 81% of the regions’ energy >100% of carbon reductants in the metallurgical industry >33% of liquid fuels - petrol, diesel and other requirements >200 major chemicals for 1000s of carbon-based products
Over 255 000 direct employees in coal mining, power generation, Sasol, metallurgical and over 6 000 coal-fired manufacturing industries. More than 4 times employed in related service industries or are
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1 000 2 000 3 000 4 000 5 000 6 000 7 000 China USA Russia India Japan Germany Canada UK Iran Korea Italy Mexico Australia Saudi Arabia Indonesia France Brazil South Africa Spain Ukraine
Million tons CO2 SA is responsible for 1.1% of total global CO2 emissions, but South Africa has committed to reducing its emissions by 35% and 42% within the next 8 years (2025)
Source IEA - Top 20 CO2 Country emitters, 2008
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6 000 INDUSTRIAL BOILERS for heat and power - Travelling grate, Shell, Water tube, Fluidised bed, Kilns, etc. 14 ESKOM POWER STATIONS for power generation – pulverised coal.
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Source IEA CCC
Efficiency gains using today’s technology can cut CO2 emissions by 33% CCS technology can produce 50% loss but leads to efficiency loss of 7-12% points
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Coal Mines do beneficiate in South Africa (beneficiated products for export) Less coal per unit heat produced = less CO2 per unit coal produced
Subcritical Pulverised Coal PC boilers e.g. Lethabo, Duvha, etc
➢ Supercritical PC Boilers – None in SA ➢ Ultra Supercritical Boilers – None in SA ➢ Advanced Supercritical Boilers – Medupi and Kusile PSs ➢ Integrated Gasification Combined Cycle - None in SA, only demonstration abroad ➢ Use of Fluidised bed power generating technologies - None in SA
* Case studies in South Africa to follow
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Implementation is on-going in South Africa
Numerous capture mechanisms and storage sites are under review South Africa has limited to negligible on land geological storage capacity
Use of CO2 streams / flue gases from coal-fired stacks for:
Research is on-going in South Africa
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4.1 - TECHNOLOGY – CIRCULATING FLUIDISED BED COMBUSTION (CFBC)
4.2 - FEEDSTOCK – COAL CO-FIRED WITH BIOMASS
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➢ Bubbling Fluidised bed (BFB) boilers – <60 MWe ➢ Circulating Fluidised bed (CFB) boilers – 60-550 MWe
many Far Eastern countries.
❖Most efficient method to address escalating environmental constraints ❖Tolerates wide fuel flexibility and quality variation
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Pilot Plant Oriental Chem General Motors Tri State Vaskalouden Nova Scotia Turow 1 JEA
100 200 300 400 500 600 700 800
1979 1981 1984 1986 1987 1990 1993 1998 2001 2009 2015
MWe Uni nit St Start-up Yea ear
Lagisza Samcheok
Lo Longest Run unnin ing Lar Largest Petcoke CFB FB
2 x 300 MW MWe
Lo Longest Run unnin ing Supe upercrit itic ical l CFB FB
1 x 460 MWe
1st
st Ul
Ultr tra Supe upercrit itic ical l CFB FB
4 x 550 MW MWe
World CFB Market Orders Over 2005-2014 Period
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70% 30% Amec FW Others
CFB over 200 MW All CFB 46% 54%
Ref: R Giglio, Amec FW, PCC 2016
Łagisza, Poland 460 MWe supercritical CFB power plant
Fuel Coal Steam flow (SH/RH), kg/s 360/313 Steam pressure (SH/RH), MPa 27.5/5.0 Steam temperature (SH/RH), ºC 565/580 Feed water temperature, ºC 290 Boiler thermal efficiency, % 94.5 Electrical output, MW gross 460.0 net 438.9 Plant thermal efficiency, % gross 45.3 net 43.3
Połaniec, Poland 205 MWe supercritical CFB power plant
Fuel: Wood residue, agro biomass LHV: 10.5 MJ/kg Moisture (AR): 35.9% Ash yield (DB) 2.8% Boiler efficiency (LHV): 91.0% Steam flow (SH/RH): 158.3/135.1 kg/s Steam pressure (SH/RH): 127.5/19.5 bar(a) Steam temperature (SH/RH): 535/535°C Feed water temperature: 242°C Reported Performance data (dry 6% O2 /50% MCR) NOx <150 mg/m3
n
SO2 <150 mg/m3
n
CO <50 mg/m3
n
Particulate matter <20 mg/m3
n
The power station meets the EU emission requirements
Emissions mg/m3n (6%)2 dry SO2 200 NOx 200 Particulates 30
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The power station meets the stringent emission values stated below
Fuel: Indonesian coal and biomass Boilers: 4 × 550 MWe CFB Net plant efficiency (LHV): 42.4% Steam flow (SH/RH): 1573/1282 t/h Steam pressure (SH/RH): 257/53 bar(g) Steam temperature (SH/RH): 603/603°C Feed water temperature: 297°C
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Particle Size 1-5cm Operating temperatures <900oC Burnout time As long as needed SOx sorbent Dolomite+& Limestone* Combustion In-bed Fuel Coal / flexible fuels Variable qualities
NB: This precludes the need for Flu Gas Desulphurisation (FGD)
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10 20 30 40 50 60 70 80 1 2 3 4 5 6 7 8 9 10 11 12 13
% Self scrubbed blue + Ash% brown
Coal samples with increasing percentages of self scrubbed SOx
% SELF SCRUBBED ASH % TOTAL S %
Source: R Taole PhD - 2018
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4.1 - TECHNOLOGY – CIRCULATING FLUIDISED BED COMBUSTION (CFBC)
4.2 - FEEDSTOCK – COAL CO-FIRED WITH BIOMASS
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PEAT
SEWAGE SLUDGE BIO & FIBER SLUDGE & S ANTRACITE
WOOD BIOMASS DEMOLITION WOOD CHIP- BOARD- POLYOLEFIN PLASTICS (PE, PP, PC..) COLORED OR PRINTED PLASTICS, CLEAN COLORED OR PRINTED MIXED PLASTICS RDF CONSUMER REF II - III MIXED PLASTICS PAPER & WOOD PETROLEUM COKE DEINKING SLUDGE SEWAGE SLUDGE REF PELLETS WOOD & PLASTICS REF I COMMERCIAL & INDUSTRIAL PEAT W/ HIGH Ca, Cl, Br BITUMINOUS COAL ANTRACITE COAL BIO & FIBER SLUDGE BROWN COAL, LIGNITE PLY- WOOD WASTE COAL OIL SHALE
PC Fuel Combustion difficulty
BARK
CFB Fuel = all fuels
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CFB provides the widest fuel flexibility in a single boiler design
Source: R Giglio, Amec FW, PCC 2016
Heating Value in MJ/kg
35 20 10 5
Renewable Fuels
COALGAE
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April 4, 2011 January 13, 2012
Source: Desa Harjobinangun, and Pakem Sleman, Yogyakarta 2014
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Ultimate analysis of different Bamboo Species and coal Physicochemical properties of Bamboo Species and coal OBSERVATIONS: Compared to coal, Bamboo species have: Calorific values (heat content)
comparable or equal to coal.
Ash contents considerably lower than
coal
Volatile matter considerably higher
than coal
Nitrogen contents considerably lower
than that of coal
Sulphur contents lower than coal (B.
balcooa has the lowest sulpur content (0.017%ad).
The firing of the bamboo (alone
expected to generate lower NOx and SOx compared to coal - as proved by the UK’s Drax full scale biomass burning power plant
Source: Samson Bada, 2018
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Raw (Unheated) Bamboo with Coal (25% Ash)
Observations:
(i) The coal combustion profile (solid black) shows peak burnout at the highest temperature (450oC ) (ii) The DTG profile presents two different peaks for the bamboo (iii) The shoulders observed within 210 – 300 0C could be attributed to the decomposition of hemicellulose & some cellulose. (iv) At temperature >300 0C, lignin is being degraded. (v) The ignition of the bamboo occurs at the lower temp region (vi) The B. bambos has the highest peak/reactivity compared to all fuels in Fig 4b
DTG curves for coal, Dendrocalamus asper, Bambusa balcooa and Bambusa bambos Peak combustion
Peak combustion of Three Bamboo spp
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Co-combustion of raw Bambusa balcooa with coal at different Wt% ratio
DTG curves for Raw BB, Coal and BB/coal at different Wt % ratios
Observations:
(i) Both the raw BB and the 90%BB+10%coal samples have virtually identical burning profiles and mass loss rates (%/min) (ii) Raw 100% BB has the lowest burnout temperature while 100% coal has the highest burnout temperature. (iii) Two peaks were noted for all coal+raw BB blended samples; coal on its own had only one peak (iv) As the coal ratio (%) in the blends increases, the combustion peaks and reactivity rates decrease; this is due to the reducing proportions of bamboo and, with that, the progressive reduction in VM and hemicellulose content in the bamboo. (v) The 75% coal/BB sample has the closest profile to coal, indicating increasing combustion compatibility between the products (vi) Varying proportions of the different fuels do affect the overall combustion behaviour of the sample
Peak combustion
Peak combustion of Increasing wt% of Bamboo balcooa DTG curves for coal and Bambusa balcooa in different wt% proportions
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Co-combustion of heat-treated Bambusa balcooa with coal at different Wt% ratio DTG curves for BB @ 280 C, Coal and BB/coal at different Wt % ratios DTG curves for BB @ 380 C, Coal and BB/coal at different Wt % ratios Observation: i. All samples are seen with one single main peaks ii. Peak combustion temperatures coincide for both heat-treated bamboo and coal
280oC 380oC
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Current 2025 UK TARGETS
Bio NG US Canada EU UK Avge DRAX
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➢ LCOE from co-firing is greater than conventional 100% coal, as the coal ratio increases ➢ Co-firing is seen to be competitive with offshore wind and solar installation ➢ There is greater certainty in the estimation of the LCOE for co-firing compared to renewable technologies
Source:: IEA Clean Coal Centre, 2018 Solar PV Offshore wind Gas CCGT 100% biomass 50% biomass Co-firing 10% biomass Co-firing Lignite Supercritical Coal Supercritical Coal Conventional
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(WITH $30 CARBON TAX)
Source: IEA Clean Coal Centre, 2018 Solar PV Offshore wind Gas CCGT 100% biomass 50% biomass Co-firing 10% biomass Co-firing Lignite Supercritical Coal Supercritical Coal Conventional
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