externality analysis of the flue gas desulphurization system at

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1 1 Externality Externality Analysis Analysis of of the the Flue Flue Gas Gas Desulphurization Desulphurization System System at at Mae Mae Moh Moh Lignite Lignite - - f f ired ired Power Power Plant Plant i i n n Thailand Thailand from from LCA LCA - - NETS NETS Point Point of of View View Sate Sampattagul, Prof. Seizo Kato Prof. Tanongkiat Kiatsiriroat, Anugerah Widiyanto Energy System Design Laboratory, Mechanical Engineering Department, Faculty of Engineering, Mie University

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Page 1: Externality Analysis of the Flue Gas Desulphurization System at

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ExternalityExternality AnalysisAnalysis ofof thethe FlueFlue GasGas DesulphurizationDesulphurization SystemSystematat MaeMae MohMoh LigniteLignite--ffiredired PowerPower PlantPlant iin n ThailandThailand

fromfrom LCALCA--NETSNETS PointPoint ofof ViewView

Sate Sampattagul, Prof. Seizo KatoProf. Tanongkiat Kiatsiriroat, Anugerah Widiyanto

Energy System Design Laboratory, Mechanical Engineering Department, Faculty of Engineering, Mie University

Page 2: Externality Analysis of the Flue Gas Desulphurization System at

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Underlying CausesUnderlying CausesUnderlying CausesUnderlying CausesUnderlying CausesUnderlying CausesUnderlying CausesUnderlying Causes Energy, Environment and EconomicEnergy, Environment and Economic

Energy

Economic

Environment

3E tri-lemma3E3E tritri--lemmalemma“Top-runner" approach ““TopTop--runner" approach runner" approach

Green procurement policyGreen procurement policyGreen procurement policy

Eco labeling and green taxationEco labeling and green taxationEco labeling and green taxation

SolutionSolution

LCA and LCC LCA and LCC LCA and LCC

Page 3: Externality Analysis of the Flue Gas Desulphurization System at

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Overview of Mae Overview of Mae MohMoh Power PlantPower Plant

!! Overall capacity 2,625 MW of 13 unitsOverall capacity 2,625 MW of 13 units!! Largest open mining of Lignite site Largest open mining of Lignite site

nearby the power plantnearby the power plant!! Lignite proved reserve approximately Lignite proved reserve approximately

about 1,332 [Millionabout 1,332 [Million--ton] could be use ton] could be use more 118 yearsmore 118 years

!! High High sulphursulphur content of lignite 2content of lignite 2--3% and 3% and low calorific heating value 2,750 low calorific heating value 2,750 kcal/kcal/kgCoalkgCoal

!! There were serious impacts to the There were serious impacts to the villagers due to SOvillagers due to SO22 over emission in over emission in 1992 and more than 1,000 people were 1992 and more than 1,000 people were suffered from the respiratory symptomsuffered from the respiratory symptom

!! FGD systems have been installed to FGD systems have been installed to solve the problem since 1993solve the problem since 1993

Page 4: Externality Analysis of the Flue Gas Desulphurization System at

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FGD: Flue Gas Desulphurization SystemFGD: Flue Gas Desulphurization System

!! Limestone wet scrubbing systems have Limestone wet scrubbing systems have been installed for the power generating been installed for the power generating stations unit 4 to unit 13stations unit 4 to unit 13

!! The efficiency of SOThe efficiency of SO22 demolition are demolition are approximately 92 approximately 92 –– 97%97%

!! SO2 produced = 0.68 [SO2 produced = 0.68 [MtonMton/year]/year]!! Limestone consumption = 1.20 [Limestone consumption = 1.20 [MtonMton/year]/year]!! SO2 Emission = 0.03 [SO2 Emission = 0.03 [MtonMton/year]/year]!! Byproduct Gypsum = 1.92 [Byproduct Gypsum = 1.92 [MtonMton/year]/year]

Page 5: Externality Analysis of the Flue Gas Desulphurization System at

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SULFUR DIOXIDE FROMMAE-MOH POWER PLANT FISCAL YEAR 1988 - 2001

0

100,000

200,000

300,000

400,000

500,000

600,000

700,000

800,000

1988 1989 1990 1991 1992 1993 1994 1995 1996 1997 1998 1999 2000 2001

SULF

UR

DIO

XID

E (T

ON

S/Y

EAR)

$0

$5,000

$10,000

$15,000

$20,000

GEN

ERA

TIO

N (G

Wh/

YEA

R)

SO2 PRODUCED SO2 EMISSION GENERATION GWh

Page 6: Externality Analysis of the Flue Gas Desulphurization System at

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NETS NETS NETS NETS NETS NETS NETS NETS (NNNNNNNNumerical umerical umerical umerical EEEEEEEEcocococo----load load load load TTTTTTTTotal otal otal otal SSSSSSSStandardization)tandardization)tandardization)tandardization)

22

77

ManyMany

2424

4343

44

No.No.

Amount of residuals in disposalAmount of residuals in disposalWaste problemWaste problem

[H+] Concentration in rain[H+] Concentration in rainAcid rainAcid rainDistrictDistrict

ScaleScale

WHO regulation valuesWHO regulation valuesAir and Water pollutionAir and Water pollution

Emission of CFCs, ODPEmission of CFCs, ODPOzone layer depletionOzone layer depletion

GHG emissions, GWPGHG emissions, GWPGlobal warmingGlobal warming

Proven ReserveProven ReserveDepletion of fossil fuelDepletion of fossil fuel

GlobalGlobal

ScaleScale

Consolidated Consolidated

standardization valuesstandardization valuesEnvironmental Environmental

load factorsload factors

[NETS]kWh,...kg,

NETSkWh,...]kg,[ iii MEVELMP =

×

Loader: Giving allowable environmental load

Receiver: Received allowable environmental load

Pi [kg, kWh,m3, …, etc.] MEVi [NETS]

L-R Tolerance Balance TheoryLL--R Tolerance Balance TheoryR Tolerance Balance Theory

Page 7: Externality Analysis of the Flue Gas Desulphurization System at

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Maximum sufferable load of the biological capacity; e.g., for one person

100 [NETS] 100[NETS/person] x (6.0×109) persons

= 6.0×1011 [NETS]

(World population in 1999 = 6.0×109 persons )

MEVMEVGG

Page 8: Externality Analysis of the Flue Gas Desulphurization System at

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Example: Fossil fuel depletion (Oil)Example: Fossil fuel depletion (Oil)Example: Fossil fuel depletion (Oil)Example: Fossil fuel depletion (Oil)

[NETS/ton] 4.11 reserves) (Proved

capacity) carrying searth' (the

=

=OilELM

Consumption 1 [ton] Give impact 4.11 [NETS]

MEVG = 6.0×1011 [NETS]

Poil = 1.46 x 1011ton

Page 9: Externality Analysis of the Flue Gas Desulphurization System at

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Process Tree of FGD.Process Tree of FGD.

FGD systemsFGD systemsFGD systemsFGD systemsLimestone Limestone Limestone Limestone extractionextractionextractionextraction

Transportation to Transportation to Transportation to Transportation to FGDFGDFGDFGD

Construction of Construction of Construction of Construction of transportation transportation transportation transportation

equipmentequipmentequipmentequipment

Construction of Construction of Construction of Construction of

FGDFGDFGDFGD

Construction of Construction of Construction of Construction of mining equipmentmining equipmentmining equipmentmining equipment

MaterialMaterialMaterialMaterial EnergyEnergyEnergyEnergy

EmissionEmissionEmissionEmission to Airto Airto Airto Air Emission to WaterEmission to WaterEmission to WaterEmission to Water WasteWasteWasteWaste

Page 10: Externality Analysis of the Flue Gas Desulphurization System at

1010

0.00E+00 2.00E-05 4.00E-05 6.00E-05 8.00E-05 1.00E-04 1.20E-04 1.40E-04 1.60E-04

Limestone Extraction

Transportation

FGD Construction

Operation

Eco-Load of FGD System at LCA step

Fossil Fuel Depletion

Resources Depletion

Global Warming

Air Pollution

Acidification

NETS/kWh

3.33E-5

3.39E-5

2.30E-5

1.46E-4

Page 11: Externality Analysis of the Flue Gas Desulphurization System at

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LCC AnalysisLCC Analysis

8%8%Interest rateInterest rate

5%5%Rate of growthRate of growth

22.80 Million dollars/year22.80 Million dollars/yearOthers CostOthers Cost

1.86 Million dollars/year1.86 Million dollars/yearLimestone CostLimestone Cost

18.13 Million dollars/year18.13 Million dollars/yearOperating CostOperating Cost

2.70 Million dollars/year2.70 Million dollars/yearMaintenance CostMaintenance Cost

218.42 Million dollars/year218.42 Million dollars/yearInvestment CostInvestment Cost (8 units)(8 units)

Up to 30Up to 30Unit lifetime [Years]Unit lifetime [Years]

( )( )

+−+×= n

n

iiiLCCFGDNPV

111)(

NPVFGD (i=8%, 30 years) = 513.25 Million dollars (467.63 Million Euro)

Page 12: Externality Analysis of the Flue Gas Desulphurization System at

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LCALCA--NETS & LCCNETS & LCC

Investment Cost

FGDInput Output

Fuel + Maintenance + Others Cost

30 Years

LCA-NETS Value

LCC Value

LCC/LCA [/NETS] = Total Cost [Euro]

Total Emission [ton SO2]*Impacts per unit [NETS/ton SO2]

FGD environmental impact costing = 0.72 Euro/[NETS]

Page 13: Externality Analysis of the Flue Gas Desulphurization System at

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Calculating Externality CostsCalculating Externality Costs

!! Externality costs = Size of Insult x VEDExternality costs = Size of Insult x VED

•• Externality costs = total external cost to society Externality costs = total external cost to society [Euro, dollars, yen, baht,[Euro, dollars, yen, baht,……]]

•• Size of insult = [NETS]Size of insult = [NETS]•• VED = Value of environmental damage VED = Value of environmental damage

[Euro/NETS, dollars/NETS,[Euro/NETS, dollars/NETS,……]]

!! Pollution problems contribute to the externality costs because oPollution problems contribute to the externality costs because of it can ruin f it can ruin the society and sometime without any reflection in market systemthe society and sometime without any reflection in market system..

!! Pollution has occurred since the first step of the energy explorPollution has occurred since the first step of the energy exploration until the ation until the end user. The externality cost should be add up in each step.end user. The externality cost should be add up in each step.

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Externality Cost of FGDExternality Cost of FGD

6.48E+86.48E+8

4.86E+84.86E+8

2.03E+72.03E+7

1.01E+81.01E+8

4.08E+74.08E+7

EcLEcL [NETS] [NETS]

349.82349.82FGD OperationFGD Operation

466.42466.42Total Total

14.6014.60FGD ConstructionFGD Construction72.6472.64TransportationTransportation29.3629.36Limestone ExtractionLimestone Extraction

Life Cycle CostLife Cycle Cost[Million Euro][Million Euro]

LCA StepLCA Step

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Benefit & Cost AnalysisBenefit & Cost Analysis

B/C ratio = 4.88

B-C = 1,822.44 Million. Euro

SOSOSOSOSOSOSOSO22222222 Reduction CostReduction CostReduction CostReduction CostReduction CostReduction CostReduction CostReduction Cost

469.81 [Million. Euro]469.81 [Million. Euro]469.81 [Million. Euro]469.81 [Million. Euro]469.81 [Million. Euro]469.81 [Million. Euro]469.81 [Million. Euro]469.81 [Million. Euro]Saving from taxSaving from taxSaving from taxSaving from taxSaving from taxSaving from taxSaving from taxSaving from tax

2,292.25 [Million. Euro]2,292.25 [Million. Euro]2,292.25 [Million. Euro]2,292.25 [Million. Euro]2,292.25 [Million. Euro]2,292.25 [Million. Euro]2,292.25 [Million. Euro]2,292.25 [Million. Euro]

SOSOSOSOSOSOSOSO22222222 ProductionProductionProductionProductionProductionProductionProductionProduction

680,877.67 [ton]680,877.67 [ton]680,877.67 [ton]680,877.67 [ton]680,877.67 [ton]680,877.67 [ton]680,877.67 [ton]680,877.67 [ton]SOSOSOSOSOSOSOSO22222222 demolitiondemolitiondemolitiondemolitiondemolitiondemolitiondemolitiondemolition

654,929.88 [ton]654,929.88 [ton]654,929.88 [ton]654,929.88 [ton]654,929.88 [ton]654,929.88 [ton]654,929.88 [ton]654,929.88 [ton]

Cost of SOCost of SOCost of SOCost of SOCost of SOCost of SOCost of SOCost of SO22222222 Reduction Reduction Reduction Reduction Reduction Reduction Reduction Reduction

0.69 [Euro/kgSO2]0.69 [Euro/kgSO2]0.69 [Euro/kgSO2]0.69 [Euro/kgSO2]0.69 [Euro/kgSO2]0.69 [Euro/kgSO2]0.69 [Euro/kgSO2]0.69 [Euro/kgSO2]Taxation of SOTaxation of SOTaxation of SOTaxation of SOTaxation of SOTaxation of SOTaxation of SOTaxation of SO22222222

3.50 [Euro/kgSO3.50 [Euro/kgSO3.50 [Euro/kgSO3.50 [Euro/kgSO3.50 [Euro/kgSO3.50 [Euro/kgSO3.50 [Euro/kgSO3.50 [Euro/kgSO22222222]]]]]]]]

COSTCOSTCOSTCOSTCOSTCOSTCOSTCOSTBENEFITBENEFITBENEFITBENEFITBENEFITBENEFITBENEFITBENEFIT

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ConclusionConclusion

2. LCA-NETS�results indicated that the most serious problem of FGD has occurred when operating than others LCA step.

5. For further development, the high efficiency of SO2 control equipment or new technology of FGD system should be emphasized to minimize the emission and to maximize the efficiency of FGD.

1. LCA-NETS�has high potential to diagnose the environmental problems and find the suitable method to improve the power plantsystem

3. Externality analysis could support to convert the impacts value in [NETS] to be the monetary value [Euro, Dollars, Baht,…]

4. Mae Moh FGD has potential to get the benefit from taxation, this mean that the taxation should be the tool to encourage the powerplant and Industries to think more about environmental improvement.

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ThAnKThAnK yOuyOu FoRFoR yOuRyOuR aTtEnTiOnaTtEnTiOn