Cost Functions for Controlling SO2 Emissions in Europe Amann, M. and Kornai, G. IIASA Working Paper WP-87-065 May 1987 Amann, M. and Kornai, G. (1987) Cost Functions for Controlling SO2 Emissions in Europe. IIASA Working Paper. IIASA, Laxenburg, Austria, WP-87-065 Copyright © 1987 by the author(s). http://pure.iiasa.ac.at/2987/ Working Papers on work of the International Institute for Applied Systems Analysis receive only limited review. Views or opinions expressed herein do not necessarily represent those of the Institute, its National Member Organizations, or other organizations supporting the work. All rights reserved. Permission to make digital or hard copies of all or part of this work for personal or classroom use is granted without fee provided that copies are not made or distributed for profit or commercial advantage. All copies must bear this notice and the full citation on the first page. For other purposes, to republish, to post on servers or to redistribute to lists, permission must be sought by contacting [email protected] COST FUNCXXONS FOR CONTROLLING SO2 EMISSIONS IN EUROPE Markus Amann Gabor Kornai May 1987 W-87-065 Working Papers are interim reports on work of the International Institute for Applied Systems Analysis and have received only limited review. Views or opinions expressed herein do not necessarily represent those of the Institute or of its National Member Organizations. INTERNATIONAL INSTITUTE FOR APPLIED SYSTEMS ANALYSIS A-2361 Laxenburg, Austria Preface This p a p e r marks a n important s t e p in t h e development of the Regional Acidification INformation and Simulation (RAINS) model. One of t h e major goals of t h e project since i t s beginning f o u r y e a r s ago, has been t o get RAINS used in policy analysis. To t h a t end t h e model should include variables t h a t a r e v e r y crucial in t h e eyes of t h e decision makers. The cost of reducing a i r pollutant emissions c e r tainly is such a n important policy relevant variable. The a u t h o r s have successfully developed a uniform approach f o r establishing cost-of-control functions f o r emissions of sulfur dioxide in virtually all European countries. This uniformity is particularly important f o r comparing t h e costeffectiveness of various scenarios f o r controlling acid deposition in Europe. Currently t h e assumptions and t h e numbers in this p a p e r a r e under review by e x p e r t s in many of t h e European countries. I would like t o thank t h e members of t h e Working P a r t y f o r Air Pollution Problems of t h e Senior Advisers t o ECE Governments on Environmental Problems and t h e Group of E x p e r t s on Cost and Benefit Analysis of t h e Executive Body f o r t h e Convention on Long-Range Transboundary Air Pollution f o r providing t h e f o r a f o r discussing t h e work contained in this paper. The cost-of-control functions allow t h e evaluation of t a r g e t t e d deposition levels at a variety of locations in Europe. This will b e t h e topic of a subsequent pap e r . In t h e n e a r f u t u r e w e will also develop similar control function f o r t h e emissions of nitrogen oxides and will eventually combine t h e functions into one cost-ofcontrol function f o r acidifying emissions. Finally I would like t o acknowledge contributions both financially and in kind made by t h e Federal Environmental Agency of t h e Federal Republic of Germany, t h e Department of Energy of t h e United S t a t e s of America, t h e Air Pollution Group of t h e Nordic Council of Ministers and t h e Dutch P r i o r i t y Programme on Acidification. Naturally t h e responsibility f o r t h e use and interpretation of t h e materials provided by these institutions remains solely with t h e authors of t h e paper. Leen Hordijk Leader, Acid Rain P r o j e c t Acknowledgment The a u t h o r s are grateful t o B. S c h a r e r (Umweltbundesamt, FRG), D. S t r e e t s (Argonne National Laboratory, USA), and B. Tangena and R. Swart (National Instit u t e f o r Public Health and Environmental Hygiene, t h e Netherlands) who were involved in discussions about t h e cost of control submodel. W e are also indebted to t h e many individuals who worked and have been working in t h e Acid Rain Project. Table of Contents 1. Introduction 2. Goals and limitations of t h e Approach 3. Principles of cost calculation 4. Abatement Options 5. P r o c e s s Emission's Removal 6. National Cost Curve References Appendix A: Cost calculation routine f o r desulfurization options during or after combustion Appendix B: Data used for t h e cost calculation Appendix C: National cost c u r v e s - vii - COST FUNCTIONS MIR CONTROLLING SO2 W S S I O N S IN EUROPE Markus Amann and Gabor Kornai 1. INTRODUCTION The RAINS (Regional Acidification Information and Simulation) model is a set of interactive computer based models developed at IIASA to assess long-term acidification in Europe on a regional scale. The available submodels a r e grouped into t h r e e compartments: the energy, emissions and cost of pollution control submodels, t h e atmospheric t r a n s p o r t submodel, and t h e impact compartment covering submodels f o r effects on lakes, groundwater, f o r e s t soils and d i r e c t impact of SO2 on forests. Special emphasis i s put on flexible use of t h e computer model both by advanced interactive software and graphical representation of t h e model r e s u l t s (Alcam0 et al., 1987). This p a p e r gives a description of t h e cost of control submodel, which is linked with t h e energy pathways and emission calculations within t h e f i r s t compartment. 2. GOALS AND LIMJTATIONS OF THE APPROACH The cost submodel of RAINS should s e r v e as framework f o r a consistent assessment of pollution control costs f o r all 27 European countries in o r d e r t o enable - a cost evaluation of different abatement strategies, based on different energy scenarios and - a comparison of pollution control costs between countries. The international comparability of t h e resulting cost d a t a is t h e basis f o r t h e development of optimized European wide emission reduction strategies, where targeted sulfur deposition levels are achieved in a cost optimal way (Batterman et al., 1986). The requirement t o assess abatement costs f o r all countries of Europe limits necessarily t h e level of detail, which can b e maintained. Data availability and computational constraints r e q u i r e simplifications, which might a p p e a r too rough f o r studies focused on one country only. Therefore t h e r e s u l t s of t h e cost submodel should b e considered much more as indicative than as absolute cost estimates: t h e main emphasis is put on international consistency and comparability. Keeping in mind t h e broad scope of RAINS - t o provide a tool f o r integrated assessment of acidification from pollutant's r e l e a s e t o ecological impacts - only d i r e c t pollution control costs are considered by t h e cost submodel. All indirect costs of emission reduction (effects on energy prices, t r a d e balance, employment, etc.) as w e l l as t h e benefits are excluded from t h e evaluation. 3. PRINCIPLES OF COST CALCULATION A basic assumption of t h e RAINSmcost submodel is t h e existence of ' f r e e t r a d e and exchange of technology0, o r - in o t h e r words - of a competitive market f o r desulfurization equipment, accessible f o r all countries throughout Europe. Based on this assumption one can specify country independent capital costs f o r a l l abatement technologies, which are determined only by t h e type of t h e equipment. The actual abatement costs ( p e r ton of removed S O z ) of each abatement technology are defined by national circumstances. These costs differ considerably among count r i e s even f o r t h e same technology mainly. due t o sulfur content of fuels, capacity utilization and boiler sizes of installations. The RAINS' cost submodel provides a n algorithm, which takes into account the technology dependent cost parameters as well as t h e country specific situations of t h e i r application. 4. ABATEMENT OPTIONS Basically seven options t o reduce sulfur emissions from energy combustion exist: energy conservation, fuel substitution, use of low sulfur fuels, fuel desulfurization, combustion modification, 'conventional' flue gas desulfurization and advanced, high efficient flue gas cleaning methods (regenerative processes). This c h a p t e r will discuss t h e s e options in some detail. Although RAINS is able t o evaluate ecological impacts of energy conserva- tion s t r a t e g i e s and provides t h e u s e r t h e possibility t o input his own energy scenario, i t seems not reasonable t o r e l a t e all costs of such policies only to emission reduction benefits, as t h e r e a r e a lot of o t h e r economic benefits (effects to t h e t r a d e balance, employment, etc.). Therefore t h e cost submodel excludes t h e cost assessment of energy conservation explicitly. Fuel sabstitution f o r reasons of emission reduction comprises t h e exchange of sulfur containing fuels (coal, oil) by sulfur f r e e fuels (natural gas, hydropower, nuclear energy). A precise evaluation of costs involved would b e very tedious and would r e q u i r e more detailed energy models. A s this,-would enlarge t h e size of \ RAINS too much, t h e cost submodel contains only a rough cost estimation p r e c e d u r e f o r such strategies, assuming t h a t t h e differences between t h e fuel prices in each country could b e i n t e r p r e t e d as opportunity costs and r e f l e c t somehow t h e more complex underlying cost s t r u c t u r e of t h e energy system (Inaba, 1985). The fuel p r i c e s of OECD countries a r e taken from IEA statistics (OECD, 1986). In o r d e r t o avoid problems of evaluating non-convertible currencies versus hard currencies, f o r CMEA countries t h e e x p o r t prices of energy t o Western Europe (as r e p o r t e d by OECD) are assumed t o r e p r e s e n t opportunity costs of fuel substitution f o r t h e national economies of those countries. A special algorithm p r e s e r v e s t h e consistency of t h e energy balance, keeping t r a c k of different combustion efficiencies of fuels and satisfying t h e basic demand/supply balances. The potentials f o r fuel substitution are derived f o r each country separately based on differences of extreme, but still on a n European level consistent, energy scenarios. According t o one of t h e main assumptions of t h e cost submodel this approach is able t o assess cost differences between scenarios, but i t does not provide absolute cost figures. The use of low sulfur fuels in o r d e r t o reduce sulfur emissions is only implemented f o r h a r d coal, where low sulfur coal is defined as coal with 1p e r c e n t sulfur content. Although in some countries coal with lower sulfur content is available, it cannot be expected t h a t t h e r e are enough coal r e s e r v e s of this type t o establish a long-term t r a d e of coal of this quality. The costs r e l a t e d t o this option are derived from analysis of t h e long-term p r i c e differences on t h e world coal market f o r low sulfur coal and are assumed t o b e equal f o r all countries. Because of t h e competitive market f o r low sulfur coal qualities, also t h e costs of physical coal cleaning have t o decline t o t h e market p r i c e differential f o r naturally occurring low sulfur coal, if this desulfurization method is t o b e applied. Due t o high transportation costs only a negligible international t r a d e of brown coal and lignite exists in Europe. I t is, t h e r e f o r e , unlikely t h a t domestic resources of those fuels will b e substituted by imports with eventually lower sulfur content. The deaulfnrization of oil products affects different product qualities. The database of RAINS contains t h e consumption of light fraction products (gasoline, jet fuel), gasoil (diesel and light fuel oil) and heavy fraction products (heavy fuel oil). The light fraction products contain a negligible amount of sulfur. Gas oil can b e desulfurized down to 0.3 percent, and at higher costs down to 0.15 percent. Heavy fuel oil will b e available with 1 p e r c e n t sulfur content e i t h e r by use of naturally occurring low sulfur c r u d e oils (e.g. from t h e North Sea) as refinery input or by desulfurization during t h e refinery process. Because of t h e vivid t r a d e with refined oil products in Europe, t h e cost submodel r e s t r i c t s t h e cost calculation of fuel desulfurization to t h e fuel p r i c e differences, but performs no bookkeeping of refinery capacities and desulfurization investments. The p r i c e increments f o r l o w sulfur oil qualities are valid f o r all count r i e s . The cost d a t a f o r fuel desulfurization are based on t h e experience of t h e Federal Environmental Agency in t h e Federal Republic of Germany. D e s u l f u r i z a t i o n during or a f t e r combustion, in c o n t r a s t to t h e already discussed emission reduction options, r e q u i r e s d i r e c t investments at t h e plant site. Therefore t h e t h r e e methods within t h i s category: combustion modification, flue gas desulfurization and high efficient regenerative processes are modeled in a diff e r e n t way. An algorithm w a s developed to derive country specific unit costs of abatement ( p e r ton of removed S O 2 ) f o r t h e s e technologies, taking into account investment eff o r t s as w e l l as fixed and variable operating costs. The investment costs are described by a function, involving t h e t y p e of technology, t h e flue g a s volume of t h e fuel and t h e boiler size as well as t h e additional expenses caused by retrofitting installations. In o r d e r to convert t h e one-time payments of t h e investment expenses to costs p e r removed ton of SO2, t h e country specific real i n t e r e s t rate and t h e a v e r a g e lifetime of plants (depending on t h e s e c t o r ) are used to annualize t h e costs by t h e p r e s e n t value method. The capacity utilization (operating hours p e r y e a r ) and t h e sulfur removal efficiency relate those annualized costs to t h e actual amount of removed sulfur. The operating expenses a r e divided into two categories: fixed costs, which a r e independent on t h e use of t h e technology (maintenance, taxes, administrational overhead, etc.) and variable costs, which are directly related t o t h e operation (labour costs, additional energy demand, costs f o r sorbents and waste disposal, etc.). Together with t h e annualized investment costs they add up t o unit costs p e r ton of removed SOz. Appendix A gives a n overview of t h e cost calculations f o r desulfurization options during o r a f t e r combustion. The technology related input data f o r t h e cost calculation routine a r e different f o r each of t h e t h r e e abatement methods mentioned above. These t h r e e basic processes represent several different technological solutions, which have in each group - - similar overall technical and economical characteristics. For methodological reasons for each group t h e most common process w a s used t o derive those significant properties, but one can assume t h a t these data represent also o t h e r competitive methods of t h e same group. Desulfurization technologies with low investment efforts, but high operating costs (due t o large amounts of produced waste material), which are applied mostly for medium efficiency removals, are represented within t h e combustion modifica- tion group by t h e limestone injection method. A s advanced. but not yet fully commercially available process t h e fluidized bed combustion would also be covered by this abatement option. The most common desulfurization technology throughout Europe is t h e flue gas desulfurization. represented by t h e w e t limestone scrubbing process. Removal efficiencies of 90 percent a r e typical. Advanced, very high efficient desulfurization proaesses are grouped into t h e regenerative process methods, which achieve efficiencies in t h e range of 98 percent, but require higher costs. A s example f o r t h e cost calculation t h e already fully commercial Wellman-Lord method i s taken. For t h e future, e.g. t h e integrated gasification - combined-cycle plants, which are presently under development in t h e USA would also fit into this technology group. The cost d a t a f o r t h e s e methods were estimated in cooperation with t h e Federal Environmental Agency of t h e Federal Republic of Germany, using t h e specific West German experience ( S c h a r e r et aL.,1987). Appendix B contains t h e data used f o r cost calculations. 5. PROCESS EMISSION'S REMOVAL Compared t o emissions caused by energy combustion, man-made sulfur emissions originating from industrial processes not r e l a t e d t o energy consumption, are badly documented. For purposes of a consistent assessment of emission reduction potentials and costs, d a t a are only available f o r few countries. These few published d a t a d o not allow t o derive even rough estimates f o r o t h e r countries. In o r d e r t o avoid inequalities between countries reporting process emissions and those, who do not d o so, i t i s necessary t o use some generic assumptions about potentials and costs of reducing those pollutants. In absence of any data, which could b e generalized, t h r e e reduction levels at different (generic) costs are assumed f o r those countries, who specify p r o c e s s emissions. Even if t h e r e would exist more precise d a t a about t h e origin of t h e emissions, i t would b e extremely difficult t o estimate reduction costs, as emission reduction of those processes is mostly connected with a change of t h e production technology. Such a change is neither necessarily induced by environmental interests, n o r should t h e resulting changes of productivity and efficiency b e ignored. 6. NATIONAL COST CURYE The national abatement costs are defined f o r each country by t h e unit costs and t h e actual potential f o r sulfur removal, which is mainly connected with t h e en- ergy consumption. In o r d e r t o allow comparisons of abatement costs between count r i e s , RAINS contains a procedure t o derive t h e least cost combination of available abatement options f o r each emission reduction level from z e r o reduction up t o t h e technically feasible limit. For a selected energy pathway a compilation of those least cost solutions will result in t h e 'National Cost Curve'. The cost efficiency serves a s common criterion to select a set of pollution control policies out of t h e infinite number of possible combinations within each country and enables therefore a consistent international comparison and evaluation of abatement efforts. The cost submodel performs in t h e f i r s t step f o r all implemented reduction possibilities (see Table 2 of Appendix A) t h e calculation of t h e country specific unit abatement costs, as long as they are technical feasible, irrespective whether they a r e cost efficient o r not. In t h e second phase of t h e model run, these sets of theoretical options are used to form cost efficient combinations. It should be mentioned, t h a t this process does not take care of introduced environmental legislation of individual countries, as otherwise difficult evaluation problems between countries would arise. It is assumed t h a t limitations t o some abatement methods, f o r example due t o waste disposal problems, are reflected by t h e related (country specific) cost f a c t o r (e.g. disposal costs), which prohibits a cost efficient application of this process in a country. However, t h e r e are some other underlying assumptions, influencing t h e construction of t h e cost curves. To evaluate t h e abatement costs f o r future years, one should also know t h e potential of new and old power plants, as t h e investment costs t o r e t r o f i t old plants are much higher. The cost submodel is based on t h e generic assumption, t h a t t h e power plants of t h e y e a r 1985 are phased out in a linear way within t h e i r lifetime of 30 years. The resulting gap in electricity production depending on t h e selected energy pathway - - has t o b e filled with new installations. For reasons of internal consistency i t should b e assured t h a t desulfurization equipment, which h a s been constructed once, h a s t o o p e r a t e until t h e end of i t s calculated lifetime, otherwise t h e c o s t calculation, which i s based on a n annualization procedure, would fail. A s result of this condition only those old power plants are allowed t o b e r e t r o f i t t e d with desulfurization equipment, which will b e still in operation at t h e end of t h e time horizon of t h e c o s t of control submodel (in t h e y e a r 2000). For those plants, which are to b e closed down e a r l i e r , only t h e use of l o w sulfur fuels i s applicable. Appendix C contains t h e abatement cost c u r v e s f o r all 27 European countries. They are based on t h e official energy pathways as they were r e p o r t e d from individual governments to IEA and ECE and r e l a t e to t h e y e a r 2000 (IEA coal information, ECE energy database). A s they should r e f l e c t t h e original energy scenario, f o r t h e purpose of t h i s p a p e r , no fuel substitution i s included although t h e cost submodel i s a b l e t o handle also this option (as described above). The c u r v e s show t h e least costs t o r e d u c e emissions f o r increasing reduction levels, starting from t h e amount of unabated emissions, which would result from t h e forecasted fuel consumption without any abatement measures. The level of t h e 30% reduction (compared to 1980 emissions), t o which m o s t countries a g r e e d in t h e Convention on Long-Range Transboundary Air Pollution, i s indicated by a star. The g r a p h s contain t h e c u r v e s f o r t h e total annual abatement costs and marginal costs curves. REFERENCES Alcamo, J., Amann, M., Hettelingh, J.-P., Holmberg, M., Hordijk, L., Kamari, J., Kauppi, L., Kauppi, P., Kornai, G. and Makela, A. (1987). Acidification in Europe: a simulation model f o r evaluating control strategies. Ambio (forthcoming). Batterman, S., Amann, M., Hettelingh, J.-P., Hordijk, L. and Kornai, G. (1986). Optimal SO2 abatement policies in Europe: some examples. IIASA Working Paper WP-86-42,IIASA, Laxenburg, Austria. ECE Energy Data Base (1987) (on tape), Geneva. Inaba, S. (1985). Costs of Meeting Stricter Environmental S t a n d a r d s for Stat i o n a t y Sources of Emissions - The Electricity Sector. International Energy Agency, Paris. International Energy Agency, Coal Information 1986, OECD, Paris. OECD (1986). Energy Prices a n d Tarzes, Second Quarter 1986,No. 4 , International Energy Agency, OECD, Paris. S c h a r e r , B., and Haug, N. (1987). The cost of flue gas desulfurization and dentrification in t h e Federal Republic of Germany. Economic B u l l e t i n for Europe, 39 (1).Pergamon Press. APPENDIX k an overview of the cost calculations f o r desulfurization options during or after combustion. Table 1: Parameters used for cost calculation. Country specific data sc hv ST bs Pf q c e ,c l , c ,c sulfur content h e a t value sulfur retained in ash a v e r a g e boiler size capacity utilization r e a l i n t e r e s t rate p r i c e s f o r electricity ,labour, s o r b e n t s and waste disposal Technology specific data I c if ciV v It x Pi Ae , A 1 , A S , Ad investment function intercept slope r e l a t i v e flue gas volume lifetime of plant sulfur removal efficiency maintenance costs and administrational overheads specific demand f o r energy,labour, s o r b e n t s and waste disposal Investment Function ciV I =(cif +-)v bs / bs Annualized investments Fixed operating costs: 0hf-1~ =I Pi Variable operating coats: SC OMvaT=(A1cl+Aece+(-(1-sr))z(AscS hv Unit Costa per PJ Unit Costs per ton S O 2 removed c ~ 0 =, C P J / ( SC ( hv 1- s r ) z ) + A d c d )) Table 2: Pollution control options (excluding fuel switching). Low sulfur Conversion Power plants Hard coal Heavy fuel oil Brown coa1,old Brown coa1,new Hard coa1,old Hard coal.new Heavy fuel oi1,old Heavy fuel oi1,new x x x x x Hard coal Coke,Briquettes Gas oil Heavy fuel oil x x Transport Gas oil x Industry Hard coal Coke Gas oil Heavy fuel oil x Domestic Combustion modification Flue g a s desulfuriz. Regener. process x x x x x x x x x x x x x x x x x x x x x x x APPENDIX B: Data used for the cost calculation. Technology Specific Cost Data Table 3: Technology specific data Combustion Modlficatlon Investment Cost Functions Intercept cif Slope ci" Resulting Specific Investments for a 210 MWeL plant: Operating Costs: Annual Maintenance Costs Other Overheads Labour Demand Additional Energy Demand Pi Flue Gas Desulfurlzation Regenerative Processes new retrofit new retrofit 52.0 22500.0 67.6 29250.0 167.0 20000.0 217.0 26000.0 275.0 22500.0 159.1 207.2 262.2 340.9 382.1 DM / kWeL X of total investments/year % of total investments/year Manyear/100 MW he 4.0 2.0 5.0 1.0 4.0 2.0 10.0 1.0 4.0 2.0 10.0 5.0 Sorbents Sorbents Demand AS Limestone 4.68 Limestone 1.56 NaOH 0.06 t Sorbents/t SO2 removed By-product Amount of By-product hd Waste material 7.80 Gypsium 2.60 Sulfur 0.50 t Product/t SO2 removed 50.0 90.0 98.0 Sulfur removal efficiency *Ih z The notation of the parameters refers t o the equations on page 12. % X - 16 Country Specific Parameters Table 4: Average Boiler Size (bs )- Powerplants (in MW el) Albania Austria Belgium Bulgaria CSSR Denmark Finland France FRG GDR Greece Hungary Ireland Italy Brown Coal Hard Coal Heavy Fuel Oil 210 139 210 210 210 210 210 202 235 210 243 210 210 153 210 220 160 210 210 178 134 252 206 210 210 210 300 335 210 128 158 210 210 201 82 306 190 210 155 210 106 227 Luxembourg Netherlands Norway Poland Portugal Romania Spain Sweden Switzerland Turkey UK USSR Yugoslavia Brown Coal Hard Coal Heavy Fuel Oil 210 210 210 210 210 210 257 210 210 195 210 210 99 210 328 210 210 300 210 254 502 210 150 245 210 370 210 193 210 210 150 210 195 203 150 126 291 210 149 Note: In case a fuel is not used in a country as powerplant input, f o r computational reasons a default boiler size of 210 MW i s used. Table 5: Capacity Utilization (pf)- Powerplants (in hours per year) Albania Austria Belgium Bulgaria CSSR Denmark Finland France FRG GDR Greece Hungary Ireland Italy Brown Coal Hard Coal Heavy Fuel Oil 4000 3504 4000 4818 4818 4000 4000 3767 6745 4818 6132 4292 4000 3679 4000 3504 3416 4818 4818 3592 2365 3767 4205 4818 4000 4292 3592 4030 4000 3066 3679 4380 3153 526 3854 1489 1226 2716 3504 4292 3416 4030 Luxembourg Netherlands Norway Poland Portugal Romania Spain Sweden Switzerland Turkey UK USSR Yugoslavia Brown Coal Hard Coal Heavy Fuel Oil 4000 4000 4000 4380 4000 4380 4730 4000 4000 4993 4000 5168 4380 3504 3154 4000 4468 4117 4380 4468 4000 4000 2978 4468 5168 1927 3504 3942 964 4468 4117 4380 4468 1314 1401 2978 876 5168 1927 Note: In case a fuel i s not used in a country as powerplant input, f o r computational reasons a default capacity utilization of 4000 hours p e r y e a r i s used. / Table 6: Electricity Prices. labour Costs and Real Interest Rata - 1 - ElePrice [10**6DM p e r PJ] Labour Costs [lOOO DM/ Manyear] Real Interest Rate c l3 cl P Albania Austria Belgium Bulgaria CSSR Denmark Finland France FRG GDR Greece Hungary Ireland I talv [XI Luxembourg Netherlands Norway Poland Portugal Romania Spain Sweden Switzerland Turkey UK USSR Yugoslavia 4.0 4.0 7.0 4.0 4.0 5.7 7.0 7.1 4.5 4.0 4.0 4.0 7.8 5.6 ElePrice [10**6DM p e r PJ] Labour Costs [lOOO DM/ Manyear] Real Interest Rate c l3 c1 Q 115.0 126.0 41.0 88.0 153.0 88.0 135.0 88.0 141.0 88.0 135.0 88.0 88.0 28.1 24.8 39.8 10.8 5.9 8.8 12.8 34.9 41.4 3.2 22.8 13.2 10.9 4.0 5.3 8.0 4.0 4.O 4.0 8.0 6.9 2.2 8.0 4.4 4.0 4.0 Note: The d a t a f o r electricity p r i c e s r e p r e s e n t t a r i f s f o r industrial consumers (without taxes). The differences in labour costs between countries are assumed to be reflected by t h e GDP (NMP) p e r capita. 1 Table 7: Default values assumed for all countries: 1 Average Boiler Size bs Industry Capacity Utilization ~f Industry Costs of Sorbents Material cS Limestone NaOH Costs of By-products Waste Disposal f o r Limestone Injection Gypsum Sulfur c [XI General Parameters valid for all Technologies Table 8: General Parameter valid for all Technologies Lifetime of Pollution Control Equipment It (in years) Conversion Powerplants Industry 20 30 20 Flue G a s Volume relative t o Hard Coal Combustion u Brown Coal Hard Coal Heavy Fuel Oil 1.2 1.0 0.9 I Table 9: Process Emissions Control Costs: Reduction from 0 % t o 30 % : Reduction from 30 % t o 60 % : Reduction from 60 % t o 80 % : 5000 10000 20000 DM/t SO2 DM/t SO2 DM/t SO2 I APPENDIX C: The following cost c u r v e s a r e based o n t h e official e n e r g y pathways, as t h e y w e r e r e p o r t e d from t h e individual governments to IEA and ECE and r e l a t e to t h e y e a r 2000 (IEA Coal information, 1986; ECE E n e r g y d a t a b a s e , 1986). A s t h e y should r e f l e c t t h e original e n e r g y s c e n a r i o s , f o r t h e p u r p o s e of t h i s p a p e r n o fuel substitution is included, although t h e cost submodel is a b l e t o handle a l s o t h i s option ( a s d e s c r i b e d above). The c u r v e s show t h e l e a s t costs to r e d u c e emissions f o r increasing r e d u c t i o n levels. Displayed a r e t h e c u r v e s of t o t a l annual and marginal c o s t s , v e r s u s t h e remaining emissions f o r t h e y e a r 2000. NATIONAL COST FUNCTIONS, y e a r 2000, OFFICIAL ENERGY PATHWAY (*) 30% reduction of 1980 emissions 25/05/1987 (c) IlASA 500: II I ~ - 5 0 Albania \ ----- \ I \ I \ n 6 400: r40 - < z --- Q, --- \ \ ..-5-- 300 E v, A 4 3 2 loo! se 0 -- \ -,20 --- \ 5200;-0 -- \ -- V z I30 - \\! \ \ --- \ --:lo ----- \ \ \ \ ---- \ \ \ \ \ 1 \ I I I I I 1 I I I I I I I I I I I l I I I I I I I I I I I , I I I t I I I I f , I I I ; J I I I I I 0 50 150 100 200 0 250 EMISSIONS (kt of S 0 2 ) NATIONAL COST FUNCTIONS, y e a r 2000, OFFICIAL ENERGY PATHWAY (*) 30% reduction of 1980 emissions 25/05/1987 (c) IlASA I I 1600- r50 ----- ---- I I I -- n L 0 '-%1200. i3 - --E " 800-E0 --0 -4 3 z 400-Z < -< -+ \ \ \ + 0 -- \ \ -120 \ \ A 0 *- \ - \ k \ \ \ \ --- \ \ -- ,,,, l l l . l l l l l l l l l l l l l l l l l l l l - l 0 100 0 -0 -C -2i i30 0 --0 -0 \ 0 ..-- N ~ - 4 0 v, . Austria \ C /4 200 300 EMISSIONS (kt of S 0 2 ) --!lo ------ 0 400 - w V) 6 0 U a $ Z NATIONAL COST FUNCTIONS, yeor 2000, OFFICIAL ENERGY PATHWAY 25/05/1987 (c) IlASA (*) 30% reduction of 1 9 8 0 emissions I 3000: -I -1 -1 ,2500 <-baJ .2 z 2000 ;! i --..-E --1500: -I ~ - 5 0 ---- Belgium \ \ \ -- ---i30 --- \ \ \ \ \ -- \ \ - 81 0 0 0 : -20 \ ---- \ s \ --500,-F P \ Z Z 4 rt \ ----- \ % 8 rC 0 < Z 0 0 0 V E az 0 U f10 \ A 0- N F40 \ E A o % Z 0 I I I I I I I I I , I I I I I I I I I I I I I I I I l 7 L I - ~ I I I I I I I I ~ 0 200 400 800 600 EMISSIONS (kt of S 0 2 ) NATIONAL COST FLINCTIONS, yeor 2000, OFFICIAL ENERGY PATHWAY (*) 30% reduction of 1 9 8 0 emissions 25/05/1987 (c) IlASA , Bulgaria \ ---------. ------- \ \ \ \I - ,20 ---F \ \ - \ y o ----- \ \ \ \ \ '+. 1 0 --- 1 1 1 1 1 1 1 1 l 1 1 1 1 1 1 \ \ \ \ 1 1 1 ~ 1000 EMISSIONS (kt of S02) 500 1 1 1 1 1 1 1 Y1 0 1500 NATIONAL COST FUNCTIONS, year 2000, OFFICIAL ENERGY PATHWAY (c) IlASA 25/05/1987 (a) 30w reduction of 1980 emissions I 4000I I I I 7 - 50 --- - L 0 '. %. 3000 8 -8-..0 -- r40 --- \ -- \ \ -E -- 2000 -- \ -- \ -- r Czechoslov. \ - n --- 1.30 ----- \ \ \ \ \ 120 \ \ 5z 1 0 0 0 --- \ --- -- Z u se --- 0 1 1 1 1 , 1 1 1 r , l l 0 500 10 0 0 1 500 2000 EMISSIONS (kt of S02) 2500 NATIONAL COST FUNCTIONS, year 2000, OFFICIAL ENERGY PATHWAY (a) 30w reduction of 1980 emissions 25/05/1987 (c) IlASA EMISSIONS (kt of S02) NATIONAL COST FUNCTIONS, year 2000, OFFICIAL ENERGY PATHWAY (*) 3095 reduction of 1980 emissions 25/05/1987 (c) IlASA EMISSIONS (kt of S02) NATIONAL COST FLINCTIONS, year 2 0 0 0 , OFFICIAL ENERGY PATHWAY (*) 30% reduction of 1980 emissions 25/05/1987 (c) IIASA I I I 8000- y50 - ---- I I n x 6000 -B -b , ------:40 ---- France \ ---- C -.-0E -4000 P f30 l \ - L -- I/) 0 0 \ \ -- a \ \ 1 2000 1 z - u J u + P 0 -----20 ---- \ I0 --- hl 0 v, rC 0 C Z 0 0 0 w g0 U g d I i 11 111 11 I I 1 111 11 0 n I I1711 1 I I I I I H I 1000 15CO EMISSIONS (kt of S02) 900 1 IIlill" l IIIIIII I 0 2800 NATIONAL COST FUNCTIONS, yeor 2 0 0 0 , OFFICIAL ENERGY PATHWAY (*) 30% reduction of 1 9 8 0 emissions 25/05/1987 (c) IlASA , F.R. Germany \ \ \ \ \ EMISSIONS (kt of S02) NATIONAL COST FUNCTIONS, yeor 2000, OFFICIAL ENERGY PATHWAY I I I (*) 30% reduction of 1 9 8 0 emissions 6000- -- I I 0 4 -E -P v, 0 0 2000 -a3 z z Q aI-e -- \ \ 0 ----- 1 \ \ --- f30 \ \ \ V \ \ \ . --20 ----- \ \ \ \ \ :lo -- \ \ \ \ ~ n hl F40 \ 8 ..-- 0 ---- \ if 4 0 0 0 - (c) IlASA ~ 5 0 German D.R. \ -- I 25/05/1987 zob'd ~ I I I I I iz6d ~ 4bb; I I I IJ EMISSIONS (kt of S02) 1 I - 1 >bbo 0 ~ v- 0 < Zi 0 0 0 C w g 0 U az ? Zi ~ NATIONAL COST FUNCTIONS, year 2000, OFFICIAL ENERGY PATHWAY (*) 30% reduction of 1 9 8 0 emissions 25/05/1987 (c) IlASA EMISSIONS (kt of S02) NATIONAL COST FUNCTIONS, y e a r 2000, OFFICIAL ENERGY PATHWAY (*) 30% reduction of 1 9 8 0 emissions 25/05/1987 (c) IlASA Hungary \ - ---800 ----400 ----- \ -- L \ ---- 30 --- \ \ \ \ --- 20 ---- \ \ \ \ \ \ \ \ \ t \ :lo - --- \ \ \ \ 0 l , , l l l l l l I l l l I I I I l I l ~ - l l l l l l l l l 0 500 1000 1500 EMISSIONS (kt of S02) -- 0 2000 EMISSIONS (kt of S 0 2 ) NATIONAL CO!3 FUNCTIONS, year 2000, OFFICIAL ENERGY PATHWAY (*) 3095 reduction of 1980 emissions 25/05/1987 (c) IlASA .\\\> 2000/ \ 4 olllllllll,,lllll,llllll,l --- , , , , , , , , 1 1 , 1 1 1 , , , 1 : 0 500 1000 1500 * 2000 EMISSIONS (kt of S 0 2 ) 1 , , 1 , , 1 , -:lo -- L --;;,;~,,, 2500 -- 0 3000 NATIONAL COST FUNCTIONS, year 2000, OFFICIAL ENERGY PATHWAY (a) 3056 reduction of 1980 emissions 25/05/1987 (c) IlASA EMISSIONS (kt of S02) NATIONAL COST FUNCTIONS, year 2000, OFFICIAL ENERGY PATHWAY 3056 reduction of 1980 emissions 2500: 25/05/1987 (8) I I I --- -- I I 2000 Q, -? , : - 3 -6 r 5 o o i..-E --- Netherlands \ \ \ \ 500: 3 P 0 ----- -- -- \ \ \ \ J\ [ I- a z lo \ ?I \ lllllllll,lllllll,l,llll,llll,l,lllll,l,lsllllll \ \ 0 . 0 U \ \ 2* V) \ \ 0 7 -- \ (V v, + 0 w 1.20 \ n g -- \ g 1000: 0 3z ---J I.30 \ - P ----1.40 ----- \ V (c) IlASA 50 100 200 300 EMISSIONS (kt of S02) 400 0 500 NATIONAL COST FUNCTIONS, y e o r 2000, OFFICIAL ENERGY PATHWAY (*) 30% reduction of 1980 emissions 1000: 1 I I I I 800: .= Q, 2 0 ..-S- ----- P ~ 5 0 -- ---: -- 40 ---- \ \ \ ---- \ \ \ \ ---- E \ 130 - \ \ \ \ -d 3 -z f 200: a ---+ -P 0 J \ \ , \ -,20 ---- 1 til 0 \ ------ \ \ I 0 --- \ 400: 0 (c) IlASA Norway 6004 w 25/05/1987 I I I I I I I I I I I 40 I I I I I l I [ I I I 1 I I I I I , I l I I I I I 80 120 EMISSIONS (kt of S02) 1 0 160 I NATIONAL COST FUNCTIONS, y e o r 2000, OFFICIAL ENERGY PATHWAY (*) 30% reduction of 1980 emissions I 8000 1 I I I -- -o % 6000 I \ -i3 0 0 a ---- \ \ \ \ F30 ----- \ \ \ \ 120 ---- \ _I \ 1 2000 f z -< $ -P -0 L40 \ --- E ---- \ --- -4000 750 - Poland L E (c) IlASA , n ..-S- 25/05/1987 - \ -- \ 1000 C'J % %- 0 C 2 a 0 0 0 C V m 0 U a z 2 :lo Z \ \ \ \ -. 2000 3000 4000 EMISSIONS (kt of S02) -- 0 5000 I I I I I h I I I l I r l I I I l I I I 1 I ~ l 1 I I I I I I I " I ' I ' I ~ t I l I I I I I l 0 n NATIONAL COST FUNCTIONS, year 2000, OFFICIAL ENERGY PATHWAY (*) 30% reduction of 1980 emissions 25/05/1987 (c) IIASA 1200j I~ o r t u g a l 1I EMISSIONS (kt of S02) - NATIONAL COST FUNCTIONS, year 2000, OFFICIAL ENERGY PATHWAY 25/05/1987 (c) IlASA I I (*) 30% reduction of 1980 emissions 5000 1 ---- I I I n 8 50 ----- -- \ 4000 1 -- <z -C o -.-- 3000 : --E -P g 2000 .-I i40 \ \ \ \ \ \ \ --- J 4 3 \ - z 0 \ \ \ \ -- 5 I ---t20 ----- \ 2 1 0 0 0- ~ :lo -- \ \ --- \ \ \ \ -- 0 I I 1 I I I r I I r I I I I I l I I 1 I I I I I I I I I I I I I I I I I l I I I I I I I ~ ~ ~ I ~ 0 500 N % + 0 .T: I F30 \ V 0 ---- \ A 1000 1500 2000 EMISSIONS (kt of S02) 2500 0 0 0 7 w 0 U d z g I NATIONAL COST FLINCTIONS, y e a r 2000, OFFICIAL ENERGY PATHWAY (=) 30% reduction of 1980 emissions 25/05/1987 (c) IlASA EMISSIONS (kt of S02) NATIONAL COST FUNCTIONS, y e a r 2000, OFFICIAL ENERGY PATHWAY (=) 30% reduction of 1980 emissions -- (c) NASA ---140 ----:30 -- L , Sweden -- \ \ ---------------------- \ \ \ \ ---- \ - \ \ L\ --~ 2 ---:lo -- \ \ \ * \ . '.. 1 1 1 1 1 1 1 1 ~ 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 1 --- L '.. 1 0 25/05/1987 1 100 200 300 EMISSIONS (kt of S02) -. ~ 1 1 1 1 1 1 1 1 0 1 400 0 NATIONAL COST FUNCTIONS, year 2000, OFFICIAL ENERGY PATHWAY (s) 25/05/1987 30% reduction of 1980 emissions \ (c) IlASA Switzerland EMISSIONS (kt of S02) NATIONAL COST FUNCTIONS, yeor 2000, OFFICIAL ENERGY PATHWAY (s) 30% reduction of 1980 emissions \ c, ~ 0 1 1 1 1 1 ~ ~ 1000 1 1 , (c) IlASA 25/05/1987 1 1 1 1 2000 EMISSIONS (kt of S02) 1 1 1 1 0 3000 1 , 1 1 1 ~ ~ NATIONAL COST FLINCTIONS, year 2000, OFFICIAL ENERGY PATHWAY (*) 30% reduction of 1980 emissions 25/05/1987 (c) IlASA , United King. ---- -- \ -:30 --- \ \ -- \ -- ---- \ - \ ---------- 120 \ -- \ --- \ \ \ \ ~ 1 1 \ . -. -. .1 1 1 - 1 lllllll,o ~ 0 I I I l l l 0 1000 2000 3000 4000 EMISSIONS (kt of S02) 5000 NATIONAL COST FUNCTIONS, year 2000, OFFICIAL ENERGY PATHWAY (*) 30% reduction of 1980 emissions 25/05/1987 (c) IlASA I I 40000 - --- I I I -- n L O %30000 \ 1---- B C .-0 - ! USSR i40 \ z u A u I- 10000 e 0 \ < 0 0 0 --- \ \ \ \ ----- \ \ \ I ---- I I I I I I I I I \ \ I I I I I I I I I . I I t : , I I I I I sob0 Iodoo 15doo EMISSIONS (kt of S02) 0 U -:lo ---- \ k 7 V 3 - 0 \ \ o a o --- \ I , I I I I I I I tw ~ 3 05 \ A A '4- -- \ I/) s -- i -E -- 20000 -Li0 -0 -.- -- 50 --- 0 20000 az ?!i Z NATIONAL COST FUNCTIONS. veor 2000. OFFICIAL ENERGY PATHWAY (r) 3035 reduction of 1980 'emissions \ \ ' 25/05/1987 (c) IlASA Yugoslavia \ 0 l 1000 l l l ~ , 2000 3000 EMISSIONS (kt of S 0 2 ) l l ~ 4000 l ~ o
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