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WORKPACKAGE 3 Economic aspects AWASTWP 3
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Participants Cemagref (France) Water and environmental engineering department Research Unit : Livestock and municipal wastes Management – Rennes Universitaet Stuttgart (Germany) Institute for Sanitary Engineering, Water Quality and Waste Management : ISWA AWASTWP 3
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Objectives Providing the economic aspects of the decision support system which will help decision makers to know which kind of system should be developed, respective of the local conditions. A more accurate undestanding and control of municipal waste management service costs will be available and proposed to decision- makers. Help waste management authorities maximize long term efficiency of MSW management system by minimizing its costs. AWASTWP 3
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Work description Task 1 : state of the art and data acquisition (Month 3 to 24) Task 2 : definition of production cost models (Month 6 to 14) Task 3 : calibration and validation of the models (Month 13 to 19) AWASTWP 3
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Production costs by facility Thematic approach by facility - MSW Operations Data acquisition (production factors : Quantity, Unit costs) Collection Sorting Landfill WP 4 Biological Treatment WP 5 Thermal Treatment WP 6
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Economic modelling Facility Direct costs InputsOutputs MSW Production factors Operating : - Labour - Energy - Supplies Maintenance Revenues (compost, energy, sale materials) Residus treatment Diagram of economics models
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Methodology Identify and inventory of the types of costs to take into account within a process standardisation between facilities to allow the global approach Definition of parameter models by facility Data acquisition on site in order to test each model of facility Processing of available and newly acquired data (data standardisation according to the matter description defined) Calibration and validation of the models (models for each activity and for the global system) AWASTWP 3
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Cases studies Mathematical modelling (writing) Bibliography Mathematical equations estimated Questionnaire survey Definition of components costs Methodology of modelling costs Phase 1
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Treatment plant C N Nominal capacity (tph, tpd, tpy) Operating costs Co Residues disposal : D Q : Flow waste Capital cost C K Product sales revenue : S - Labour : L - Energy : E - Reagents : R - Maintenance : M 1 6 4 2 5 3 Flowsheet of economic evaluation
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Direct plant costs (DPC) Indirect plant costs (IPC) (Equipment costs) (Land, start- up, supervision) (Building and civil works costs) Total capital cost = C I = DPC + IPC C I = Fonction (C N, process) Existing models costs Model cost Data acquisition on plants and actualisation Annual capital cost = Ck = C I /T T : life plant / Estimation of capital costs
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Capital cost of incineration plant C I = 275,7 x C N + 18 277 000 C N : tpy C I : in euros h t Source data : France : 15 plants Norway : Trondheim Austria : Vienna
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Factor method : relation between component costs and basic variables Co = fonction (C N, Q, process) Co = aL + bE + cR + d.I E L : direct labour costs L, E, R, I E : basic variables E : energy costs R : reagent costs I E : equipment costs a, b, c, d, : processing factors are summed d. I E : maintenance costs Estimation of operating costs
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Incineration : decomposition of the operating costs (Dry scrubber) Operating cost model Co = F + P + M – S or Co = (1,36 x L + 0,005 x I E ) + 1,10 x R + (0,023 x IE + 20 x Q) – 620 x P U x Q
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Incineration : symbols explanation
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Standards et variables locales
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TYPES OF MRFs (1) Design capacity is determined for 3 000 hours per year running (2) Type 4 is particular to american regions Trondheim - 20/21 June 2002 - Cemagref - ISWA
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MRF CAPITAL COSTS Methods for fixed-capital cost estimation 1st method : C FC = k. IEC 2nd method : C FC = h. C N,, h is a cost in € / 1000 t/y IEC, the installed equipment cost, can be: calculated as a sum of equipment items costs, IEC = Σ i IEC i estimated as IEC = f. C N, f is a cost in € / 1000 t C N is the design capacity. Trondheim - 20/21 June 2002 - Cemagref - ISWA
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MRF OPERATING COSTS Methods for operating costs estimation: 1st method : C O = k (α. L + β. C FC ) 2nd method : C O =λ L k is > 1, it accounts for overhead expenses α. L represents Direct Cost, that includes Labour, utilities and repairs β. C FC represents Maintenance This method is used when no sufficient data are available (types 3,4) L is labour cost, it depends on type of MRF and number of shifts per day. L= Σ k w k l k where k= sorters, conductors, foreman, etc. l = number of k workers w = unit cost of a k worker Trondheim - 20/21 June 2002 - Cemagref - ISWA
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Flowsheet to calculate the collection cost Flowsheet to calculate the collection cost Trondheim - 20/21 June 2002 - Cemagref - ISWA AWASTWP 3 Waste collection on area Requirements : vehicles crews containers Waste quantity Qs COST ANALYSISLOCAL AUTHORITIESTECHNICAL ANALYSISWASTE STREAM Collection data by collection system Components costs by data processing Collection cost model Cp = Cc + Co Collection data France / Germany Crew efficiency Rc = f (CL) Vehicle efficiency Residual waste Dry recyclables Biowaste TOTAL PRODUCTION COST UNIT PRODUCTION COST (per waste stream) 1
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Cost determining factors Trondheim - 20/21 June 2002 - Cemagref - ISWA AWASTWP 3 2
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Work time and number of trips to facility assessments 1. Definition of the work time per day : Tc : collection available time Tj = Tc + (Nt x Th) + Tb Th : haul time Tb : break time 2. Definition of the work per week and per year : T = Tj = j x Tj(France : T = 5 x 7 = 35) 3. Number of trips per day determination : Nt = Tc / Tv Tv : vehicle loading time Trondheim - 20/21 June 2002 - Cemagref - ISWA AWASTWP3 3
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The different collection systems 4 WP3AWAST Trondheim - 20/21 June 2002 - Cemagref - ISWA
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Crew efficiency graphs Trondheim - 20/21 June 2002 - Cemagref - ISWA AWASTWP 3 5 Rc = f (CL) BRING COLLECTION Emptying rate : t = emptying time / container (2 - 6 min) Qj = Re x Tc KERBSIDE COLLECTION
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Model of waste collection cost Capital cost : C C = I v / d Operating cost : C O Production cost : C P = C C + C O Wages : L = Σ l k w k Energy : E = Ce Dy Collection follow-ups : determination of , , Trondheim - 20-21 June 2002 - Cemagref - ISWA AWASTWP 3 6
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PRODUCTION COSTS COLLECTION : C P = 1.7572 L + 1.287 E + (0.0805+1/d) I v Take into account the utilization rates for : - the vehicle : d = (35 7) / (Tj j) - the crew :full-time :L share-time :L 1, L 2 L 1 + L 2 = L under-time :L [ T / (Tj j)] PRECOLLECTION : C’ P = N w I’ r ( 2 ’ + 1/n’) required containers / week / crew:Nw = (Nj j) / f = (Nr Nt j) / f Trondheim - 20/21 June 2002 - Cemagref - ISWA AWASTWP 3 7
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Example of collection costs calculation Hypothesis :- vehicle : Vv ; n = 7 ; Nt = 1 - crew : full-time work ; Rc - one waste stream of annual quantity : Qs - number of vehicles = number of crews = Ns Collection data : Equipment / crews required :- collection time : Ts = Qs / (52 x j x Rc) - number of crews : Ns >= Ts / Tc Annual production cost : Cp = .Ns.L + .Ce.Dy + .Ns.I v Trondheim - 20/21 June 2002 - Cemagref - ISWA AWASTWP 3 8
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AWASTWP 3 Full cost of MSW Service Global approach – Integrated MSW management Collections Sorting Composting Incineration Landfill General administration Executive oversight Indirect costsDirect costs Local Authority +
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OMR 79 347,4 DEM 1 500,53 JM 7 718,9 OM 93 568,07 OM tri 5 001,24 Déchetteries 51 252,61 DAS 2 161,98 DIB 3 942,72 Verre 6 083,89 Graisse 669,28 Compostage 5 001,24 Incinération Centre de tri sélectif Compost 2 000,5 REFIOM 1 414,08 Mâchefers 20 289,52 Acier 2 824,82 Al 47,82 Energie 35 254 MWh Papier 4 628,48 Carton et Tetra-pack 2 168,1 Flaconnages plastics 578,76 Acier 526,42 Al 17,46 CET1 Verre 6 083,89 Eaux traitées 495,41 ? 40 ? 1 300,21 Evaporation 1 101,08 Maturation 20 289,52 Verre 849,379 Tout venant 14 961,65 Végétaux 14 175,01 Gravats 16 186,49 Papiers 874,56 Cartons 1 313,6 Ferrailles 2 503,46 Plastiques 23,8 Huiles 120,07 D.M.S 154,33 Pneus 55,6 Batteries 34,66 2 824 val. 47,82 val. 28 944 à EDF 6 310 MWh auto-consommation -3 192,48stocks 23 482 val. 4 356,44 val. 272,04 stocks 1 908,93 val. 259,16 stocks 477,75 val. 101,01 stocks 494,04 val. 32,38 stocks 14,24 val. 3,52 stocks Refus = 1 899,66 Refus = 261,45 2 161,98 + 3 942,72 +133,87 = 7 238,57 79 347,4 AWASTWP3 Materials flow’s synoptic : the case of Orléans Trondheim -20/21 June 2002 - Cemagref
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AWASTWP3 Method of knowledge costs Trondheim -20/21 June 2002 - Cemagref Waste collection Incineration plant Q1+Q2 Q1 Q2 Other authorities Local authority A Stream Activity Bottom Ash Fly AshLandfill 1 Landfill 2 Illustration with the thermal path Level Boundaries Costs A Plant Production cost by activity B Stream Production cost by stream C Local authority Providing cost of local authority B C
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AWASTWP3 Production cost per activity (Level A) : the case of Orléans, year 2000 Trondheim -20/21 June 2002 - Cemagref
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AWASTWP3 Cost per path or stream (level B) : the case of Orléans (France), year 2000 Trondheim -20/21 June 2002 - Cemagref
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AWASTWP3 Full cost providing for local authority (level C) : the case of Orléans, year 2000 Trondheim -20/21 June 2002 - Cemagref
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SCIENTIFIC ACHIEVEMENTS AWASTWP 3 Trondheim - 20 - 21 June 2002 - Cemagref
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PROBLEMS ENCOUTERED Requirements : available actual data, updated data, updatable data Modelling waste collection : limited to main waste stream( residual, packaging, biowaste) Sorting, composting : necessary to define a typology of the technologies Landfill, anaerobic digestion : available data from only litterature review Full cost : identification of indirect costs components on case studies Difficulty to obtain data : in spite of the achievement of questionnaire of collection data ( operating plant by private firms ) Deliverable D6 ( Methodology ) : we have a delay on the deliverable D6 ( provisional draft) Full cost of the service : will be achieved in year 3 ( with the analysis of case studies) Trondheim - 20 - 21 June 2002 - Cemagref AWASTWP 3 7
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ECONOMIC ASPECTS - FOR THE NEXT 6 MONTHS Collection : validation of the model of waste collection with data of Stuttgart ( urban area) Composting : data costs collection in France, Portugal, Germany ( in waiting ) : Modelling production cost Landfill and transfer station : modelling production cost ( with litterature review ) Deliverable D6 : achievement the writing « Methodology of production cost models and the full cost providing by local authority » Beginning the transfer of models for WP7 ( integration simulator) Beginning the determination of the full cost on case studies : ( Orleans with BRGM, Lisbon with LQARS, Stuttgart with USTUTT ) Trondheim - 20 - 21 June 2002 - Cemagref AWASTWP 3 7
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