Acessibilidade / Reportar erro

A GENERIC TACTICAL PLANNING MODEL TO SUPPLY A BIOREFINERY WITH BIOMASS * * Invited paper.

ABSTRACT

The supply chains which bring biomass to biorefineries play a critical role in biofuel production. Optimization models can help decision makers to design more efficient chains and minimize the cost of biomass delivered to the refineries. This article based on a French national research project on biomass logistics considers one refinery, able to process several crops and several parts of the same crop, over a one-year horizon divided into days or weeks. A network model and a data model are first developed to let the decision maker describe the supply chain structure and its data, without affecting the underlying mathematical model. The latter is a mixed integer linear program which combines for the first time various features, either original or tackled separately in the literature. Knowing the refinery demands, it determines the activity levels in the network (amounts harvested, baled, transported, stored, etc.) and the required equipment, in order to minimize a total cost including harvesting costs, transport costs and storage costs. Numerical evaluations based on real data show that the proposed model can optimize large supply chains in reasonable running times.

Keywords:
biomass; supply chain; modeling; optimization; mixed integer linear programming

1 INTRODUCTION

The three last decades have seen a growing interest in the potential of biofuels as a means of reducing dependence on fossil fuels and in the development of clean and renewable energy. In this context, efficient logistic chains are essential to supply biorefineries regularly, reliably, and with sufficient quantities of quality biomass at a reasonable price. This latter aspect is particularly important since a significant percentage of biomass cost at the refinery gate lies in logistic costs.

Optimization models and algorithms constitute precious tools to design a biomass supply chain, evaluate possible structures a priori, and quantify the resources required, the associated costs, the energy consumptions and the environmental impacts. Beyond a simple simulation of a future reality, design choices can be rationalized and optimized. Moreover, a good model allows to anticipate the impact of important investments and thus reduces the risk of wrong decisions.

However, such an optimization raises many theoretical and practical issues, such as the relevance of the mathematical model and the need for reliable data. In particular, the supply chain must be carefully analyzed to come to a model as close as possible to reality. Indeed, a biomass supply chain is a complex network, controlled by a huge number of parameters and decision variables. For instance, it is necessary to determine the types of biomass to mobilize, the production areas, the locations of refineries and their capacities, the associated storage sites, the required harvesting and transportation equipment, etc. This kind of chain often covers a vast territory and involves a time horizon of several months, to take into account seasonal fluctuations in supply and demand. Moreover, numerous constraints must be satisfied, such as harvesting windows, biomass degradations, resource capacities, and refinery demands.

This article presents a mixed integer linear program (MILP), developed in the frame of a French national project to optimize the biomass supply chain of one biorefinery with a typical supply radius of 50 km. This multi-biomass and multi-period tactical planning model combines several features, either original or considered separately in the literature. It determines for each period the amount processed by each activity (harvesting, packing, transportation, preprocessing...), the flows in the logistics network, the required equipment and the stock levels. The goal is to satisfy the needs of the refinery while minimizing the total cost of the system. The modeling approach is generic and flexible enough to be extended to most biomass-to-bioenergy supply chains at the tactical decision level.

This remainder of the paper is organized in four sections. Section 2 briefly recalls the principles of biomass supply chains (structures, activities), reviews the literature on tactical optimization models for biomass supply, and position our problem vis-a`-vis the existing works. Section 3 introduces the network model used to describe biomass supply chains. The data model is quickly presented in Section 4. Its aim is not only to encode the network model, but also the other required information, such that refinery demands and equipment characteristics. The mathematical model is defined in Section 5. Section 6 is devoted to case studies while concluding remarks are brought in Section 7.

2 BIOMASS SUPPLY CHAINS

This section recalls the principles of biomass supply chains, and in particular in which respect they differ from industrial supply chains, before presenting a literature review and situating our problem.

2.1 Structure and activities

A biomass supply chain includes various activities, such as cultivation, harvesting, preprocessing, transportation, handling, and storage. It usually stops at the gates of a conversion unit, in general a biorefinery, producing biofuels and chemical intermediates, or a bioenergy conversion plant, generating electricity, heat, and/or cooling. The distribution stage from conversion facilities to end-users is sometimes added but the actors involved in the upstream and downstream parts are very different, which makes a global optimization extremely difficult (for instance, reliable data are hard to find). Compared to industrial supply chains, several differences must be underlined:

  • Biomass supply chains cover a vast collection territory, with many scattered cultivation areas.

  • Long planning horizons must be considered, because most crops have a one-year cultivation cycle.

  • Inputs (biomass productions) and outputs (conversion activities) are desynchronized.

  • Because of degradations, the crops cannot wait and must be harvested quickly when ready.

Both industrial and biomass supply chains can be modeled as networks (graphs) where the nodes correspond to the locations of interest while the arcs represent product flows. However, biomass supply chains involve specific activities that require various resources:

  • Harvesting activities are possible in a limited time window at the input nodes devoted to biomass production (farms), when the crop is ready, and they compete for a limited fleet of machines like combine harvesters.

  • Storage is required in practice to synchronize the biomass production calendar with the production plan of conversion plants. It can take place in the fields or forests as simple stacks, in the farms, in centralized storage sites, or before the processes in conversion facilities.

  • Pre-processing is useful to improve preservation (drying) and handling (baling, pelletization) and to reduce transportation costs by increasing density. The simplest treatments like baling can be done on the field. Stronger compressions and other transformations like torrefaction are possible, but using heavier equipment and/or dedicated sites.

  • Transport. Like in industrial logistics, several transport modes can be used, the fleet of vehicles is often limited and the number of travels per period is restricted by vehicle range and driving time regulations. Road transport is often the only solution for biomass production areas with limited accessibility (forests), and truckload operations are systematic due to the large amounts handled.

The designers of such chains need modeling tools to cope with this complexity. Before coming to a total cost, they must understand the dynamics of the chain and determine many variables, like the amounts harvested (which crop, where, when, in which amount), the network flows (quantities transported), the advisable stock levels, and the resources consumed (harvesting equipment, vehicles, energy, manpower). Subtle tradeoffs must be found. For instance, densification can be done on the field, using balers, or in a more efficient densification plant. The second option adds a transport step to the plant, but then transport costs are reduced, due to higher density.

2.2 Literature review

The literature on biomass supply chains is exploding but covers very different topics, such as the design of new harvesting machines, densification techniques and biomass degradation issues. The papers devoted to quantitative modeling represent only a subset and involve various approaches which include simple cost calculations (spreadsheet-based), geographical information systems (GIS), performance evaluation (e.g., simulation), and mathematical optimization. As even a review restricted to optimization models would take too much space, we prefer to recommend two recent and up-to-date surveys, and then cite only a few representative examples of research works which address, like ours, tactical planning problems. The reader will find in the two surveys other examples of optimization models dealing with strategic or operational decisions.

The first recommended review (De Meyer et al., 20144 DE MEYER A, CATTRYSSE D, RASINMÄKI J & VAN ORSHOVEN J. 2014. Methods to optimise thedesign and management of biomass-for-bioenergy supply chains: A review. Renewable and Sustainable Energy Reviews, 31: 657-670.) addresses deterministic optimization models and solution methods for biomass supply chains. 99 publications from 1997 to 2012 are analyzed and classified according to the decision level at hand, the objective to optimize, and the kind of mathematical model used. A general description of biomass supply chains for bioenergy is presented, with the decisions related to their design and management. The authors underline the fact that most publications optimize an economic objective and use a commercial solver to solve the models. Very few dedicated algorithms like metaheuristics (e.g., genetic algorithms) are developed up to now.

We recently published in Renewable Energy a complementary survey (Ba et al., 20161 BA BH, PRINS C & PRODHON C. 2016. Models for optimization and performance evaluation of biomass supply chains: An operations research perspective. Renewable Energy, 87: 977-989.) which comments 124 references, including 72 after 2010. In addition to the deterministic optimization models of the previous review, it covers simple cost calculation models, GIS-based techniques, simulation models, stochastic optimization, and multi-objective approaches.

Tactical models involve medium-term decisions, typically over a one-year horizon divided into elementary periods (days, weeks or months). In biomass supply chains, the decisions in each period concern for instance the amount of each type of biomass to harvest, the stock levels, the product flows in the network and the required number of harvesting machines and transportation vehicles. The published models are designed to supply biorefineries, but also heating and power plants. Some of them include strategic decisions, like the optimal location of refineries, but the exact schedule of activities in each period is never addressed since it concerns the operational decision level.

Cundiff et al. (19973 CUNDIFF JS, DIAS N & SHERALI HD. 1997. A linear programming approach for designing a herbaceous biomass delivery system. Bioresources Technology, 59(1): 47-55.) introduced the first remarkable tactical model of biomass supply chain. The goal is to supply one biorefinery with switchgrass (an herbaceous plant) over a 12-month horizon. The model is a pure linear program (LP), i.e., without integer variables. It is tested on 20 producers, having 3 to 10 fields each, and 4 to 7 storage sites (open air or covered). It determines the optimal amounts harvested, stored and transported each month and the capacity of each storage. An extension with meteorological scenarios weighted by different probabilities is also described.Van Dyken et al. (201017 VAN DYKEN S, BAKKEN BH & SKJELBRED HI. 2010. Linear mixed-integer models for biomass supply chains with transport, storage and processing. Energy, 35(3): 1338-1350.) model as a MILP a forest supply chain for one heating plant. The changes in density, humidity and heating power of each product after each operation are tracked along the chain. These changes depend on the drying mode and vary nonlinearly with drying time but they can be linearized. The model is appraised on a simple case with 3 products, 1 dryer, 1 chipper, 1 pelletizer, 2 storages and 2 demand points, over 12 weeks. It extends an earlier model, eTransport, designed for the planning of energy systems (Bakken et al., 20072 BAKKEN BH, SKJELBRED HI & WOLFGANG O. 2007. eTransport: investment planning in energy supply systems with multiple energy carriers. Energy, 32: 1676-1689.).

Haque & Epplin (20128 HAQUE M & EPPLIN FM. 2012. Cost to produce switchgrass and cost to produce ethanol from switchgrass for several levels of biorefi y investment cost and biomass to ethanol conversion rates. Biomass and Bioenergy, 46: 517-530.) consider one year with a monthly time-step, 6 possible sites for several biorefineries processing switchgrass, and 57 counties in Oklahoma. They develop a MILP in which binary variables specify the locations and capacities of refineries and storage centers, while integer variables are defined to select the number of equipment for harvesting and handling.

EksioGlu et al. (20096 EKSIOGLU SD, ACHARYA A, LEIGHTLEY LE & ARORA S. 2009. Analyzing the design and management of biomass-to-biorefinery supply chain. Computers & Industrial Engineering, 57(4): 1342- 1352.) propose one of the rare models including the distribution phase beyond the refinery. The chain collects agricultural and woody biomass to produce ethanol. The MILP model prescribes strategic decisions such as the location, number and size of refineries and collection sites, and tactical decisions like material flows. However, the different harvesting activities and their resources are not handled. The objective is to minimize over one year a sum of costs concerning biomass (harvest, storage, transport, conversion) and the distribution of ethanol. EksioGlu et al. (20107 EKSIOGLU SD, LI S, ZHANG S, SOKHANSANJ S & PETROLIA D. 2010. Analyzing the Impact of Intermodal Facilities to the Design and Management of Biofuels Supply Chain. Transportation Research Record. Journal of the Transportation Research Board, 144-151.) extend the previous study to different transport modes. The objective is to identify locations for refineries, transport modes to use, transport planning and biofuel production scheduling, to minimize the total cost for delivering the fuels to end-customers.

Shabani & Sowlati (201313 SHABANI N & SOWLATI T. 2013. A mixed integer non-linear programming model for tactical value chain optimization of a wood biomass power plant. Applied Energy, 104: 353-361.) focus on the supply of a power plant with forest residues (bark, sawdust, pruning products), purchased from different producers. They propose a mixed integer nonlinear program, in which nonlinearities are induced by two complex constraints that bind the types of biomass consumed, their quantities, their moisture content and the amount of electricity that can be obtained. For 6 suppliers over 12 months, the model has 260 variables and 333 constraints and can be solved using the Outer Approximation (OA) algorithm.

2.3 Position of our problem and closest works

Our mathematical model, a MILP, is described in Section 5 but we can already underline its features:

  • The chain supplies a single refinery, already located and whose biomass demands are given.

  • It ranges from the fields to refinery gates but ignores cultivation systems and refinery processes.

  • The activities in the chain are planned over one year divided into periods of one day.

  • The biomass producers can be selected in a given set of farms.

  • The model can switch to larger periods (e.g., weeks) and larger production areas (e.g., counties).

  • Many oil and lignocellulosic crops can be used, e.g., rape, camelina, miscanthus (a kind of cane)...

  • Several parts of the same crops can be employed, e.g., seeds, straw and chaff for rape.

  • Several harvesting chains are possible for the same crop and the equipment can be selected for each task of these chains (for instance, one tractor among several commercial models).

  • Shared stocks (containing several products) and storages with opening periods can be dealt with.

  • A network model and a data model make the MILP independent from the supply chain structure.

No published model includes all these features simultaneously but we comment below the three closest papers, which share several characteristics with our contribution: Shastri et al. (2011a15 SHASTRI Y, HANSEN A, RODRIGUEZ L & TING KC. 2011a. Development and application of BioFeed model for optimization of herbaceous biomass feedstock production. Biomass and Bionergy, 35: 2961-2974.), Dunnett et al. (20075 DUNNETT A, ADJIMAN C & SHAH N. 2007. Biomass-to-heat supply chains: Applications of process optimization, Trans. IChemE Part B (Process Safety and Environmental Protection), 85(B5): 419-429.) and Samsatli et al. (201512 SAMSATLI S, SAMSATLI NJ & SHAH N. 2015. BVCM: A comprehensive and flexible toolkit for whole system biomass value chain analysis and optimisation - Mathematical formulation. Applied Energy, 147: 131-160.). Like in our study, the first work details several steps in the harvesting process. The two others are based on the same network model as ours, called state-task network (STN) and detailed in Section 3.

Shastri et al. (2011a16 SHASTRI Y, HANSEN A, RODRIGUEZ L & TING KC. 2011b. A novel decomposition and distributed computing approach for the solution of large scale optimization models. Computers and Electronics in Agriculture, 76: 69-79.) built a sophisticated MILP to supply one biorefinery producing bioethanol with one herbaceous plant (e.g., switchgrass or miscanthus) over one year divided into days. The refinery is already placed but several locations are possible for a centralized storage. A strong point is to detail farm activities (harvesting, raking and baling) and to determine the associated equipment. Integer variables are used to select and dimension storage areas, harvesting equipment, vehicle fleet size, and the number of vehicle rotations in each day. The model called BioFeed comes in two versions: either in pull mode (the capacity of the refinery and its demands per period are given, and these needs must be satisfied) or in push mode (the available biomass is completely collected, then the refinery is dimensioned accordingly). An online supplement lists the symbols used for data and variables, but the equations for the constraints and the objective function are not provided.

BioFeed underwent two evolutions. Lin et al. (201411 LIN T, RODRIGUEZ LF, SHASTRI YN, HANSEN AC & TING KC. 2013. GIS-enabled biomass-thanol supply chain optimization: Model development and Miscanthus application. Biofuels, Bioproducts and Biorefineries, 7: 314-333.) combine this tactical model with a strategic one developed by Lin et al. (201310 LIN T, RODRÍGUEZ LF, SHASTRI YN, HANSEN AC & TING KC. 2014. Integrated strategic and tactical biomass-biofuel supply chain optimization. Bioresource Technology, 156: 256 266.). Shastri et al. (2011b) propose a Decomposition and Distributed Computing (DDC) approach for large supply chains. The BioFeed model is split into two separate optimization sub-problems: a biomass production problem, focusing on on-farm activities, and a provisioning problem, dealing with post-production activities such as transportation logistics.

Dunnett et al. (2007) applied the state-task networks to model a supply chain delivering miscanthus to one heating plant, over a 12-month horizon. The example treated considers one farm where miscanthus is baled or chipped, and then stored in a local storage with passive drying. Both forms are trucked to the heating plant where the bales are also chipped. A forced drying is applied to achieve a minimum moisture level, then the resulting product is incinerated to produce heat. Storage capacities are virtually unlimited in this case study but all tasks have a maximum throughput. A MILP model is derived from the STN. It minimizes system costs by using continuous variables (quantity processed by each task, in each period), integer variables (numbers of harvesting and transportation resources to purchase) and binary variables (to indicate whether a resource is used or not in a given period, and to allocate resources to tasks).

More recently, Samsatli et al. (2015) proposed the BVCM (Biomass Value Chain Model) for a large number of bioenergy system pathways. This is in fact a strategic model, but we cite it as it relies, like our model, on a multi-biomass and multi-period MILP derived from an STN. More precisely, the network model called Resource-Technology Network (RTN) is an extension of the STN in which different resource modes can be selected for each technology. The BVCM is provided with a database and a user interface, allowing decision makers to configure a scenario, run the optimization and visualize results. It is illustrated by a case study over a 50-year horizon divided into 5 decades and one large territory (Great Britain) discretized in squares of 50 km.

Contrary to our work, Shastri et al. (2011a) and Dunnett et al. (2007) do not tackle multiple crops, multiple harvesting chains, different parts for each plant, shared storages and a restricted opening period for each storage. Moreover, Dunnett et al. (2007) consider one farm only and use a longer time slot (one month). Samsatli et al. (2015) can cope with various biomass types but their model with much coarser time and space granularities is not really applicable to tactical planning. In particular, it does not detail farm activities and transportation resources are not taken into account.

3 NETWORK MODEL

The network model is a graphical description of the supply chain, from which the equations of the mathematical model can be automatically generated. Its aim is to enable the user to describe a wide range of supply chains, without having to modify the underlying mathematical model. We selected as a basis a modeling framework called state-task network, which is more precise than a classical graph.

3.1 State-task networks

State-task networks (STN) were introduced by Kondili et al. (19939 KONDILI E, PANTELIDES CC & SARGENT RWH. 1993. A general algorithm for short-term scheduling of batch operations - I. MILP formulations. Computers and Chemical Engineering, 17(2): 211- 227.) and Shah et al. (199314 SHAH N, PANTELIDES CC & SARGENT RWH. 1993. A general algorithm for short-term scheduling of batch operations - II. Computational issues. Computers and Chemical Engineering, 17(2): 229- 244.) to model petrochemical processes over a time horizon divided into discrete periods. They use only three entities: two types of nodes (states and tasks), and arcs.

A state represents a feed, an intermediate, or a final product. Symbolized by a circle, it can correspond to a true storage, a work in process (WIP) or even a product in rapid transit between two manufacturing units. A task, represented by a rectangle, is a processing operation which transforms one or more input states, in fixed proportions, into one or more output states, also in fixed proportions. An arc corresponds to a flow of a single product, always from a state to a task or vice versa. A state can be produced and consumed by one or more tasks. In each period, each task pulls simultaneously the required materials from its input states and sends the resulting products to its output states. A processing time in number of periods can be specified on each outgoing arc.

Figure 1, adapted from Kondili et al. (1993), illustrates the flexibility of STN on a petrochemical process with 9 states, 5 tasks and 1-hour discrete time slots. A storage capacity, sometimes unlimited, is indicated in each state. The percentages before a task define the proportions of the recipe, while the ones after a task specify the output yields. These percentages are implicitly equal to 100% when omitted, for instance for the tasks with a single input state.

Figure 1
Example of state-task network (adapted from Kondili et al., 1993).

We can notice that the STN can model tasks with multiple inputs and outputs (Reaction 1), loops (Reaction 3 → Intermediate Y → Separation → Intermediate Z → Reaction 3), and processing times. For instance, the input products consumed by Reaction 2 in period t yield a new product available on output in period t + 2. Note that changing a single characteristic of a product (state) makes it another product, e.g., “Feed A” becomes “Hot A” after heating.

Moreover, limited resources can be added. E.g., Kondili et al. (1993) mention for Figure 1 one heater (capacity 100 kg) for the “Heating” task, two reactors (80 and 50 kg), usable for the three tasks “Reaction 1”, “Reaction 2” and “Reaction 3”, and one distillation column for the “Separation” task.

Last but not least, the same authors show that a MILP can be generated from the STN, to determine the timing of operations for each resource and the product flows through the network, so as to optimize a given objective function. All these features make the STN a powerful modeling tool for multi-period planning problems over discretized time horizons. Only simulation models can be more precise, but it is difficult to use them for optimization purposes.

3.2 Application to biomass supply chains and example

As mentioned in subsection 2.3, the STN has been already applied to biomass supply chains in two works, Dunnett et al. (2007) and Samsatli et al. (2015). The first one brought the following extensions to the original STN, designed by Kondili et al. (1993) for process industries:

  • Transportation tasks are added, the product before and after such tasks giving two distinct states.

  • The final product (heat) is also considered as a state.

  • Humidity is an additional attribute associated with the states.

  • Tasks can be period-specific, e.g., the ambient drying rate is higher in August than in January.

  • Utilities (manpower, gasoil, etc.) are defined for each processing unit to deduce CO2 emissions.

Samsatli et al. (2015) added another feature in their Resource-Technology Network (RTN). The RTN is in fact similar to the STN (the resources correspond to the STN states and the technologies to the STN tasks) but it becomes possible to select different modes for each technology.

Figure 2 shows how a more complex supply chain like the one considered in our study can be represented as an STN. We add to the basic STN an upper level, the geographical locations, to model the set of states and tasks of each important site (gray rectangles). Three locations are considered: one farm producing rape (colza), one centralized storage with one silo for seeds plus one platform for bales, and one refinery with buffer stocks. The sites are composed of states Se (stocks in a broad sense, including the rape field S 1) and tasks T i . Each state contains a single product Pk and is either a cultivated field, a work in process (like the straw on swath) or a true stock (silo for instance).

Figure 2
Example of state-task network (STN) for a simple supply chain with one farm, one centralized storage and oe biorefinery.

Only one crop is considered to keep the figure readable, but it is easy to add other crops. The whole rape (product P1) is cut by a combine harvester (task T1) which yields three products: seeds (product P2), chaff (small particles, P3) and straw (stalks, P5). Each product is defined by a crop of origin (here, rape only), a crop part (seeds, chaff, straw), a presentation (bulk or square bales) and a moisture content.

The seeds are discharged in a trailer drawn by a tractor and brought immediately to the silo. The straw, available after 3 days of drying on swath, is packed in square bales using a tractor pulling a baler. These bales temporarily placed on the ground are either kept in a shed on the farm or sent to the refinery by a semi-trailer truck. The chaff is collected by the harvester in a special compartment which is emptied on the ground, giving a loaf which is then taken over by a square baler equipped with a special feeder. Chaff bales are carried by a tractor with a flatbed trailer, to be stored with the straw in the same shed. Then the same transport mode transfers the straw and chaff bales to the platform of the storage site. Finally, semi-trailers transport the products from the on-farm shed and the centralized storage to the buffer stocks of the refinery.

The STN indicates the storage capacity in each state, the distances (often negligible inside the farm) for each transport task, and the required resources (over each task). The only separation process is here the harvesting task, while the only blending process is the refine-task. Percentages are only indicated on the outgoing arcs of the harvesting task. They are implicitly equal to 100% on the other arcs. The refine-task is particular because its inflows (biomass demands) are given period per period: the percentages are not mentioned since they depend on the period.

The only notable wait is the passive drying of the straw on the ground (3 days) on exit from the harvesting task. This drying could also be modeled by a dedicated task. For the other tasks, there is no waiting time, which means that the inputs consumed in period t are transformed into output products which can be used in the same period.

This example shows that the STN describes well the structure of the supply chain and its different activities. However, this graphical representation cannot be directly interpreted by a computer and many auxiliary data must be added, for instance the number of periods of the planning horizon, the length of a period in days, the costs and throughputs of equipment, the density of the different products to compute their transported volumes, etc. The role of the data model presented briefly in the next section is to encode the STN and all other required data as database tables.

4 DATA MODEL

The purpose of this section is to explain, without entering into details, how the STN and all auxiliary data can be structured efficiently as a set of database tables. Indeed, the data management layer is a critical component in optimization software, although it is often under-estimated in OR papers. We first present the list of tables used, the special way in which resources (equipment) are handled, and the list of data symbols from which the mathematical model of Section 5 is automatically generated.

4.1 Tables used

We selected the entity-relationship approach to analyze data. An entity is a set of things or persons sharing common properties, called attributes or fields. A relationship describes the way the entities are linked. For instance, states and tasks represent two entities while state-to-task arcs constitute a relationship, more precisely a subset of the cross product of states and arcs. A relationship may have its own attributes, for instance an arc may have a length and a transported product.

Entities and relationships can be implemented as a set of tables stored in a database. We selected Excel, which is simpler and lighter than a true database management system. Each entity gives one Excel worksheet with one column per attribute and one row for each member (record) of the entity. The identifier (ID) or key is a mandatory attribute to identify each member of an entity unambiguously. All tables for one run of the model are stored in one Excel workbook. The user can evaluate different scenarios by modifying existing workbook or creating new ones.

The proposed worksheets are listed in Table 1. They include those describing the state-task graph: STATES, TASKS, ST ARCS (state-task arcs) and TS ARCS (task-state arcs). The biomass is described by three worksheets: CROPS, CROP PARTS and PRODUCTS. What we call a product is defined by one plant of origin, one part of this plant, and one form (e.g., bulk, bales, or pellets). The other worksheets describe the resource management system, described in Section 4.2. Such a data model is very flexible and new attributes can be easily added in each entity.

Table 1
List of worksheets (type E: implementing one entity, type R: one relationship).

4.2 Resource management system

Our resource management system deserves some explanations. We call resources the motorized equipment (harvesters, tractors, trucks...) and their accessories (rakes, balers, trailers...) used by the tasks. The table RESOURCES contains various commercial models with their characteristics, e.g., the productivity in hectares per hour (for a harvester), or the average speed (for a truck).

The resource families (FAMILIES worksheet) are categories of equipment with similar functions but which do not refer to specific models. Examples of families are mowers, combine harvesters, balers, trucks, farm trailers (drawn by a tractor), truck trailers, etc. Families serve in the LOCA FAM worksheet to limit the number of equipment which can be employed on each site, for example no more than two tractors on a farm. Each tractor can be any commercial model defined in RESOURCES.

A resource combination (worksheet COMBINATIONS) is a collection of resources working together for a task. For instance, the transport task T3 in the state-task network of Figure 2 involves one tractor and one flatbed trailer. Combinations are necessary to properly calculate resource working times, because the productivity of a resource depends on the combination that uses it. In France for instance, the maximum speed allowed for a tractor on the road depends on the size of its trailer. The combinations have the same attributes as the resources but, because of special cases like our tractor example, only an expert in agricultural machinery can specify which combinations are possible and compute their attribute values, in order to fill the worksheet COMBINATIONS.

Finally, the combination groups or generic combinations (worksheet GROUPS) play for the combinations the same role as the families for the resources: the exact characteristics are not specified. For example, a 200 hp tractor with a 15-ton flatbed trailer is a resource combination belonging to the combination group “tractor + trailer”.

In fact, the state-task graph specifies one group for each task, so the optimization module is free to choose any combination of real equipment in COMBINATIONS. The resource level is mainly used to cumulate the working hours of each selected equipment (since the same machine can be used by several tasks and in several combinations) and estimate fleet size.

4.3 Data and variables used by the mathematical model

The data contained in the Excel workbook are listed below. The database contains other fields not described here, e.g., to format the results (full site names) or prepare the distance matrix (GPS coordinates). The general parameters listed in Table 2, like the number of periods, are loaded from worksheet PARAMETERS. As refinery demands are often specified per week or half-month, we introduce a longer period Re f Per for the refinery. Its use is explained in subsection 5.3.

Table 2
Data from worksheet PARAMETERS.

Table 3 gives the indexing sets. MILP solvers can read Excel files with one row per record and one column per attribute, including one for the identifier (key) of each record. These keys which may be integers or character strings are gathered in a set used to allocate dynamic arrays. We used character strings to improve model readability. For instance, if the solver finds 8 products in worksheet PRODUCTS, it stores their keys in a set PI D and creates arrays of 8 elements, indexed over PI D, for product attributes like density. A model generated in this way is said data-driven: data and model equations are completely separated, and even set cardinalities are discovered by the solver when loading the worksheets. Figure 2 contains examples of location, product, state and task identifiers.

Table 3
Indexing sets.

Note that a few indexing sets do not correspond to worksheets listed in Table 1. RCRPairs is required to define the different resources involved in each resource combination, while the last sets as from Z are introduced to improve model readability.

5 MATHEMATICAL MODEL

This section introduces the equations of our mixed integer linear program in this order: declarations of variables, inventory and flow constraints, satisfaction of refinery demands, resource constraints, objective function, computation of energy consumptions and CO2 emissions.

5.1 Declaration of variables

A general principle is to restrict the indexing of variables listed in Table 5, to reduce model size. Inventory levels (S e,t ), flows on state-task arcs (X e,i,t ), and task-state arcs (Y i,e,t ) are defined only in the time windows when state e is open, see constraints (1)-(3).

e , i S T A , t S B e g e , S E n d e : X e , i , t 0 (1)

i , e T S A , t S B e g e , S E n d e : X i , e , t 0 (2)

e S I D , t S B e g e , S E n d e : X e , t 0 (3)

Table 4
Data arrays indexed over the sets of Table 3.

Table 5
List of variables.

For each task i and each period t, the variables Amp (amount processed) are defined only for the resource combinations c which may be used by the task, see constraints (4). The Ref ine task of the refinery is not concerned since its amounts processed are fixed and equal to the demands.

i T I D | T T y p e i " R e f i n e " , c R C I D | R C G r o u p c = T G r o u p i , t H : A m p i , c , t 0 (4)

In constraints (5), the integer variables for the number of vehicle rotations are generated only for transport tasks and resource combinations usable by each task.

i T I D | T T y p e i = " T r a n s p o r t " , c R C I D | R C G r o u p c = T G r o u p i , t H : R T i , c , t (5)

Finally, the integer number of units of resource r to purchase for geographical site (location) l is defined only for the resource families allowed on the site.

l L I D , r R I D | l , R F a m r L F P a i r s : F S l , r (6)

5.2 Inventory and flow constraints

Storage capacity. We added an attribute SRep e to model a group of states as one shared storage, for instance a platform storing bales of different products. In the data, one representative r is defined for the group and all members e of the group (even r) are such that SRep e = r. A nonshared storage e has no representative: SRep e = N A. Storage capacity constraints are generated only if a limited capacity is specified. Constraints (7) concern non-shared stocks. Constraints (8) for shared stocks are generated only for representatives, i.e., states e such that SRep e = e.

e S I D | S C a p a e < H u g e a n d S R e p e = N A , t S B e g e , S E n d e : S e , t S C a p a e (7)

e S I D | S C a p a e < H u g e a n d S R e p e = e , t S B e g e , S E n d e : u S I D | S R e p u = e = S u , t S C a p a e (8)

Inventory balance equations. They take degradations into account. Constraints (9) concern the first period of the opening window and the initial inventory. Constraints (10) are for the other periods.

e S I D : S e , S B e g e = S Q B e g e · S D e g e + i , e T S A Y i , e , S B e g e - e , i S T A X e , i , S B e g e (9)

e S I D , t ] S B e g e , S E n d e ] : S e , t = S e , t - 1 · S D e g e + e , j S T A X e , j , t (10)

Definition of flows on task outgoing arcs. Constraints (11) translate one property of STN networks: the flow on a task outgoing arc (i, e) is equal in each period t to a fraction TSFrac i, e of the total input flow consumed TSDura ie periods before.

i , e T S A , t S B e g e , S E n d e | t - T S A D u r a i e 1 : Y i , e , t = T S F r a c i , e · u , i S T A X u , i , t - T S D u r a i e (11)

Definition of flows on task incoming arcs. Constraints (12) specify the fraction of the total input flow taken on each incoming arc. For the Ref ine task, they are replaced by demand constraints, see 5.3.

e , i S T A | T T y p e i " R e f i n e " , t S B e g e , S E n d e : X e , i , t = S T F r a c e , i · e , j S T A | j = i X e , j , t (12)

Flow conservation for each task. In constraints (13), the left sum is the total flow consumed by task i, taken in parallel on all incoming arcs (e, i). It is multiplied by the sum of TSFrac, which can be less than 1 if the yield is not perfect. The resulting flow appears on outgoing arcs (i, u), TSDurai,u periods later. For the refinery, these constraints have a different form explained in 5.3.

i T I D T T y p e i " R e f i n e " , t H : e , i S T A | t S B e g e , S E n d e X e , i , t · i , u T S A T S F r a c i , u = i , u T S A | t S B e g u , S E n d u - T S D u r a i , u Y i , u , t + T S D u r a i , u (13)

Final inventory constraints. They are generated for the last period of the opening period of each stock e if a final stock is specified. Constraints (14) for minimum final inventories are mainly used for the input stocks of the refinery, to chain successive years without having to stop activities. Constraints (15) deal with maximum final inventories. For instance, SQEnd Maxe = 0 is used to empty a stock after the last period SEnd e of its window.

e S I D | S Q E n d M i n e > 0 : S e , S E n d e S Q E n d M i n e (14)

e S I D | S Q E n d M a x e < H u g e : S e , S E n d e S Q E n d M a x e (15)

Maximum reception capacity of storage states. Constraints (16) deal with storage states like silos. They have a maximum reception capacity SThrue , in metric tons per hour, to be multiplied by the number of opening hours per period of the geographical site containing the state.

e S I D | S T y p e e = S t o c k , t S B e g e , S E n d e : i , e T S A Y i , e , t S T h r u e · L H o u r s S L o c a e (16)

5.3 Demand satisfaction constraints

The supply chain is analyzed over base-periods of 1 or 7 days. Refinery demands use a longer period, in general 1 or 2 weeks, equal to Ref Per base-periods. Moreover, they are expressed in dry tons of some crop parts. The exact products are not imposed, e.g., a demand of 185 dry tons of rape straw can be satisfied using 100 tons of bales with 10% humidity and 100 tons of pellets with 5%.

As refinery production variations are unknown, we assume that the need in dry tons for crop part k in refinery period w is consumed at a constant rate in each base-period. For instance, a demand of 70 tons in week w is consumed at a rate of 10 tons/day. Note that this does not imply to receive the same amounts daily, since the refinery has input stocks for 2 weeks of production, on average.

i T I D | T T y p e i = " R e f i n e " , w , k D P a i r s , t w - 1 · R e f P e r + 1 , w · R e f P e r : e , i S T A P P a r t S P r o d e = k P D r y S P r o d e · X e , i , t = D N e e d w , k / R e f P e r (17)

In constraints (17), the demand DNeed w,k for refinery period w and crop part k covers baseperiods (w − 1) Ref Per + 1 to w Ref Per. It is defined only for the pairs (w, k) contained in set DPairs. This set was introduced to reduce memory requirements: indeed, most products are requested a few weeks or months per year. The sum cumulates the flows of products X e,i,t (converted in dry tons) for crop part k, from the input stocks in each base-period of the refinery period. It must be equal to the uniform consumption DNeed w,k /Ref Per in the refinery period.

5.4 Resource management constraints

The principles of our resource management system were introduced in subsection 4.2. Recall that in worksheet TASKS a group of resource combinations is specified for each task i, e.g., “one tractor + one trailer”. The task may use several combinations in the same group, e.g., one 200-hp tractor with a 6-meter trailer, plus one 240-hp tractor with a 8-meter trailer.

Constraints (18) mean that the total input flow of each task i in each period t must be processed by the resource combinations c allowed for this task.

i T I D | T T y p e i " R e f i n e " , t H : c R C I D | R C G r o u p c = T G r o u p i A m p i , c , t = e , i S T A X e , i , t (18)

The next step is to convert the amounts processed in resource combination working times. For farm tasks Harvest, Rake and Bale (set of task types ZHRB), constraints (19) compute the variables TCH RB i,c,t (working time of combination c for farm task i en période t), which are necessary to count the operational costs of farm equipment (Farm OpCosts) in the objective function. We have two cases because the productivities RT hru are in hectares per hour for Harvest and Rake (set ZH R) tasks but in bales per hour for Bale tasks. We get metric tons per hour using the crop yield for Harvest and Rake tasks, and the volume of a bale and product density for Bale tasks.

i T I D | T T y p e i Z H R B , c R C I D | R C G r o u p c = T G r o u p i , t H : I f T T y p e i Z H R t h e n : T C H R B i , c , t = A m p i , c , t e , i S T A R C T h r u c · S T Y i e l d e , i e l s e : T C H R B i , c , t = A m p i , c , t e , i S T A R C T h r u c · R C V o l u m e c · P D e n s S P r o d e (19)

In constraints (20), the working time TCT i,c,t for a transport task is based on the number of vehicle rotations RT i,c,t , the distance travelled Dist i and the average speed of the combination RCSpeed c .

i T I D | T T y p e i = " T r a n s p o r t " , c R C I D | R C G r o u p c = T G r o u p i , t H : T C T i , c , t = 2 · T D i s t i · R T i , c , t R C S p e e d c (20)

In constraints (21), the working time T R l,r,t of resource r on site l in period t is deduced from the working times of combinations in which the resource intervenes. Here we do separate constraints for Harvest, Rake and Bale tasks from the ones for Transport tasks, because a tractor (for instance) can be used by all these tasks.

l L I D , r R I D | l , R F a m r L F P a i r s , t H : T R l , r , t = c R C I D | c , r R C R P a i r s ( i T I D | T T y p e i Z H R B a n d R C G r o u p c = T G r o u p i a n d T L o c a i = l T C H R B i , c , t + i T I D | T T y p e i = " T r a n s p o r t " a n d R C G r o u p c = T G r o u p i a n d T L o c a i = l T C H R B i , c , t ) (21)

To help the solver, simple bounds are applied to the integer variables RT i,c,t , the number of rotations in period t for the resource combination c used by task i, e.g., a semi-truck with a road trailer. In the lower bounds of constraints (22), Amp i,c,t is divided by the minimum of vehicle capacity and maximum weight (resulting from vehicle volume and product density). As the product is defined for states but not for tasks, the sum is used to get the state e of origin, which is unique for a transport task. The quotient cannot be rounded up to the closest integer if we wish to keep the model linear.

i T I D | T T y p e i Z T , c R C I D | R C G r o u p c = T G r o u p i , t H : R T i , c , t A m p i , c , t m i n R C W e i g h t c , e , i S T A R C V o l u m e c · P D e n s S P r o d e (22)

RTi,c,t cannot exceed the previous lower bound plus 1. For instance, if the quotient in (22) is 6.3, the integer variable RT i,c,t must be greater than 6.3 and less than 7.3: the solver has no choice and sets it to 7.3. If the quotient is integer, say 6, the solver has the choice, but only among two values, 6 and 7.

i T I D | T T y p e i Z T , c R C I D | R C G r o u p c = T G r o u p i , t H : R T i , c , t A m p i , c , t m i n R C W e i g h t c , e , i S T A R C V o l u m e c · P D e n s S P r o d e + 1 (23)

In constraints (24)-(25), the number of units of resource r required on site l, FS l,r , can be bounded using the maximum resource working time and the number of opening hours of the site (per period).

l L I D , r R I D | l , R F a m r L F P a i r s , t H : F S l , r T R l , r , t m i n R W T i m e r , L H o u r s l (24)

l L I D , r R I D | l , R F a m r L F P a i r s , t H : F S l , r T R l , r , t m i n R W T i m e r , L H o u r s l + 1 (25)

Finally, the total number of resource units per family is limited via constraints (26). These constraints were introduced after preliminary tests where all fields were harvested in too few periods, implying an unrealistic number of combine harvesters.

l , f L F P a i r s : r R I D | l , R F a m r L F P a i r s F S l , r L F N M a x l , f (26)

5.5 Objective function

Over the planning horizon, the objective function defined by Equation (27) includes operational costs of farm equipment (FarmCosts), transport costs (TranCosts), fixed costs (capital costs) of resources (FixedCosts), inventory costs (InvCosts), and handling costs (HandCosts).

M i n Z = F a r m C o s t s + T r a n C o s t s + F i x e d C o s t s + I n v C o s t s + H a n d C o s t s (27)

In Equation (28), FarmCosts concerns resource combinations for Harvest, Rake and Bale tasks (set ZHRB), the transports in the farms being counted with other transports in Trans OpCosts. It is derived from working times TCH RB i,c,t computed in constraints (19). The first sum includes each task i with a type TType i is in ZHRB. The second considers only the combinations c of the resource combination set (RCI D) which have the group recommended for the task (RCGroup c = T Group i ).

F a r m C o s t s = i T I D | T T y p e i Z H R B c R C I D R C G r o u p c = T G r o u p i × t H T C H R B i , c , t · R C O C o s t c (28)

TransCosts is deduced in Equation (29) from working times TCT i,c,t computed in constraints (20).

F a r m C o s t s = i T I D | T T y p e i Z H R B c R C I D R C G r o u p c = T G r o u p i × t H T C H R B i , c , t · R C O C o s t c (29)

FixedCosts is computed in equation (30) from variables FS l,r computed in constraints (24)-(26).

F i x e d C o s t s = l L I D r R I D | l , R F a m r L F P a i r s F S l , r · R C C o s t r (30)

A storage cost is applied to the amount contained in each state e at the end of each period t . In general, Field and WI P states have no storage cost. Some true storages like silos can be used only a few weeks or months per year for the biorefinery. The rest of the time, they are reserved to other activities like cereal production. Hence, the storage costs in equation (31) are counted only in the opening window [SBeg e , SEnd e ].

I n v C o s t s = e S I D t S B e g e , S E n d e S I n v C o s t e · S e , t (31)

Finally, the handling costs (32) are applied to the amounts of products entering or leaving a storage. They avoid detailing the numerous little resources involved: band conveyors and aspirators of grain silos, forklifts used to stack bales, etc.

H a n d C o s t s = i , e T S A t S B e g e , S E n d e S I n p C o s t e · Y i , e , t + e , i S T A t S B e g e , S E n d e S O u t C o s t e · X e , i , t (32)

5.6 Derivation of energy consumptions and CO 2 emissions

Environmental criteria are important to appraise a biomass supply chain. The following equations are used to derive the energy consumption and the CO2 emissions from the optimal solution to the mathematical model. They can also be included with adequate weights in the objective function (27).

For each resource combination is given a power RCPower in kW. In general it corresponds to the motorized component of the combination, e.g., the tractor for a “tractor + baler” combination. It can be also the power of electric equipment such as an oven or a press in a pretreatment/densification site. In Equation (33), the total energy consumption in kW×h is simply deduced from the powers RC Power of resource combinations and their working times, i.e., TCH RB i,c,t for harvesting equipment and TCT i,c,t for transport vehicles.

E n e r g y = i T I D c R C I D | R C G r o u p c = T G r o u p i × t H T C T i , c , t + T C H R B i , c , t · R C P o w e r (33)

Equation (34) for CO2 emissions is almost as simple. Indeed, we know for each resource combination the gasoil consumption RFuel in liters per hour, while table PARAMETERS indicates the number of kilograms of carbon dioxide emitted per liter of gasoil, KgCO2 (nearly 2.6 kg/l).

C O 2 = i T I D c R C I D | R C G r o u p c = T G r o u p i × t H T C T i , c , t + T C H R B i , c , t · R C F u e l · K g C O 2 (34)

6 NUMERICAL EVALUATIONS ON REAL DATA

The effectiveness of our MILP model based on extensions and adaptations of state-task networks is demonstrated on a few numerical examples based on real data. Only the first example can be described completely, due to the large amount of data involved in the other tests.

6.1First example

This case involves 10 production zones (“farms” in a broad sense) which cultivate rape (colza) and/or miscanthus and 3 centralized storage sites, at 50 km maximum from one local refinery close to the city of Compie`gne (60 km at the north of Paris). These sites are listed in Table 6.

Table 6
Data for locations and their attributes.

The three first columns respectively give the location (geographical sites) identifiers, the site types and the municipalities. We selected a total demand of 50,730 metric tons/year of dry matter, a typical value for a local biorefinery. Rape yields three products (bulk seeds, straw bales, chaff bales) while miscanthus provides straw bales only.

The planning horizon is one year divided into 52 weeks of seven days each, giving 364 elementary time periods. The annual demands in metric tons for each product are given in Table 7, in reality they are specified for each refinery-period of one week.

Table 7
Annual demands for each crop part.

Each farm grows rape and/or miscanthus. The harvesting chain and harvesting windows applied to each farm are given in the two last columns of Table 6. Chain 1, used by farms 5 and 10 which produce rape only, is identical to the chain already depicted in Figure 2. Chain 2 (see Fig. 3 for an example) is employed in farms 6 and 11 which cultivate miscanthus only. The other farms produce both crops using chain 3, a combination of chains 1 and 2 with a shared on-farm storage for all baled products (rape straw, rape chaff and miscanthus). The earliest windows, ending at period 144 or before, are related with miscanthus, harvested in March-April. Those beginning as from period 189 (beginning of July) concern rape. The windows vary slightly depending on soils but all end beg-October. The refinery and centralized storages (sites L1-L4) are open all over the year.

Figure 3
Harvesting chain number 2 for miscanthus.

It is assumed that each farm may ship biomass to the closest storage site and to the refinery. Real distances by road were calculated using the MapPoint software from Microsoft. Data for the equipment were found in agricultural databases, see for instance (18).

The mathematical model has been implemented under the OPL-STUDIO version 12.6 modeling environment from IBM (which calls the CPLEX solver in version 12.6 too) and solved on a portable PC with a 2.7 GHz Intel Core i7-3740 QM processor, 16 GB of RAM, and Windows 7 Professional.

Although the number of farms (10) looks modest, the model is already huge, due to the number of periods and the number of states and tasks in the STN. For instance, even a farm growing rape only requires 8 states and 11 tasks, with associated decision variables (flows and stocks) indexed over 364 periods. The whole model has in fact 588,304 constraints and 500,094 variables, including 91,437 integer variables. The pre-solver of CPLEX reduces it to 87,445 constraints and 94,883 variables, including 31,575 general integer variables and 9,826 binary variables. The binary variables are visibly used to replace the number of vehicle rotations and the number of resource units when they have small upper bounds. The overall running time is reasonable: an optimal solution costing 4,829,586 euros is obtained in less than 3 minutes (164 seconds).

Figure 4 shows the breakdown of the expenses. The fixed costs of equipment are included in the harvesting part. Storage costs represent 59%, while they are often under-estimated in the literature. In fact, this percentage is normal because the harvest periods are short (about 15 days for each of the two crops), while the refinery consumes biomass throughout the year: it is therefore necessary to build up important stocks. In particular, initial stocks must be sufficient to supply the refinery before the harvesting periods for miscanthus and (later) rape, to avoid infeasibility.

Figure 4
Logistic costs breakdown.

6.2 Simplifications for large instances

The model can be solved up to 80 farms and 20 centralized storage sites, over one year divided into 52 weeks. Such a size is already respectable but we found one example with 100 farms/25 storages which cannot be solved over 52 weeks: the branch-and-bound of CPLEX reports an “out of memory” error. The problem clearly comes from the large number of integer variables, F S l,r and RT i,c,t .

The model computes the number of machines FS l,r to buy for each site. This leads to a total cost where equipment investments are predominant. In reality, a farmer uses also his machines for other crops not asked by the refinery and may help other farmers or be helped. So, it is difficult to isolate the equipment cost fraction related to the refinery supply chain. The French Chambers of Agriculture regularly publish tariffs to invoice such exchanges (18). The main interest is to provide costs which include everything, even maintenance and equipment amortization. It becomes possible to optimize a total cost, composed of the resource working times of constraints (19)-(20), multiplied by the hourly tariffs. The modification of the objective function is straightforward and variables FS l,r can be suppressed. However, if the user wishes so, it is still possible to derive the equipment required on each site from the optimal solution, using constraints (24)-(26).

The numbers of vehicle rotations RT i,c,t used to compute transport costs can also be avoided using a simpler system in tons × km, often applied when a refinery subcontracts its transports.

The French Federation of Road Transport (FNTR) (http://www.fntr.fr) gives formulas for various trucks.

We have solved again the 10-farm case with 364 days to evaluate the impact of these simplifications. The numbers of variables and constraints are roughly divided by 2 and, obviously, there are no more integer variables. Before the pre-solve, the model has 265,245 variables and 212,760 constraints. The pre-solver goes down to 26,580 variables and 9,791 constraints. The running time drops from 164 seconds to less than one second. The solution obtained is very similar to the one of the complete model, with an important cost difference equal to the equipment fixed costs since they are no longer counted. Looking at the other costs, a marginal difference of only 0.53% can be observed.

These simplifications also allowed to solve the case with 100 farms, 25 storages and 52 weeks which raised an “out of memory” error for the complete model. The simplified MILP has 162,074 variables and 203,721 constraints. Once pre-solved, only 8,339 variables and 5,839 constraints remain. The running time reaches 8,158 seconds (2 hours 1/4) but this duration is acceptable for strategic studies. By dichotomy, we were able to solve instances with 150 production zones, but not more.

To go further, it is important to notice that model size mainly results from the states and tasks of harvesting chains, which are applied to hundreds of farms. In comparison, the states and tasks for the refinery and centralized storage represent around 10% of the STN nodes. Hence, we tried a formulation where all the tasks and states of a harvesting chain, between the Field state and the farm storage, are aggregated to give a “macro-task” Harvest. An example is given in Figure 5 . The stock-states before leaving the farm must be kept, otherwise the macro-task would be connected to transport tasks (remember that two tasks cannot be directly connected in an STN).

Figure 5
State-task network of Figure 2 after the introduction of the macro-task.

Macro-tasks are similar to the tasks considered before, with three important differences.

  • A classical task may use one resource combination only, while a macro-task may involve several combinations, in fact, all resource combinations required by the aggregated tasks.

  • In a classical task, the resource combination used processes 100% of the total input flow, while in a macro-task it can be applied to sub-products. For instance, Figure 2 shows that rape yields 18% of chaff, which explains that the combination “tractor + square baler” used to bale chaff in Figure 5 treats only 18% of the total amount of rape harvested on input.

  • Waiting times are still possible for some outputs, see the straw released after 3 days of passive drying in Figure 5, but feasible solutions with pauses inside the harvesting process are now excluded, e.g., when the farmer harvests during one day, stops the second day, and terminates the job the third day. However, we have never seen such useless breaks in the optimal solutions of the complete model and, anyway, they do not correspond to agricultural practices: indeed, due to meteorological uncertainties, farmers prefer to work continuously once they start harvesting.

The condensation of harvesting chains into macro-tasks must be done manually and carefully, but then the database and model modifications are relatively easy. The model encompassing all these simplifications, called “compact model” is applied to a large-scale case in the next subsection.

6.3 Large-scale example

To appraise the performance of the compact model, a large case was built after a long work to collect data and format them for our database. Although many detailed data at the farm level are protected in France by the statistical secret, the main results per municipality of the 2010 Agricultural Census are publicly available, including the number of farms, the cultivated area, and the dominating profile, e.g., “cereals and oilseed crops”, “viticulture”, etc.

The web site http://agreste.agriculture.gouv.fr/chiffres-cles-4/commune/ provides for instance one file for the 2,292 cities of the Picardie Region (north-west of France). To build a realistic scenario, we selected in this file the cities with a profile compatible with rape, i.e., with codes 15 (“cereals and oilseed/protein crops”) and 16 (“field crops of general type”). Among them, we kept the 460 cities at 50 km maximum from Compie`gne, where a local biorefinery is foreseen. The “farms” correspond to the resulting cities, as the data for the underlying 2,146 real farms are not accessible. To estimate the harvestable amount of rape, the cultivated area of each selected city was divided by 3, assuming a classical crop rotation rape-wheat-barley. The resulting area was finally multiplied by the average rape yield in the region, i.e., 6.95 tons/ha. Rape is obtained via the harvesting chain of Figure 2.

A partner of the research project has sent questionnaires to the operators of centralized storages, again within a maximum distance of 50 km to Compie`gne. The answers were typed in an Excel file giving the following data for 46 storage sites: kind of storage (silo or platform), capacities in tons for silos and square meters for platforms, storage costs, input and output costs, availability window in the year. Storage capacities vary from 200 to 60,000 tons. Each farm may send its products (seeds, straw bales and chaff bales from rape) to the nearest centralized storage, but not directly to the refinery. The planning horizon is one year subdivided into 52 weeks. The total refinery demand is 50,000 metric tons per year and road distances were computed again using MapPoint.

The resulting model contains 588,249 constraints and 574,795 variables. After a reduction to 4,801 constraints and 19,558 variables by the pre-solver, it is solved to optimality in less than one minute (47 seconds).

Our model and its results can be compared BioFeed (Shastri et al., 2011a). This closest model in the literature is more restrictive than ours, since it considers a single product from a single crop and a unique harvesting chain in three steps (harvest, rake, and bale). In Shastri et al. (2011b), BioFeed is applied to a switchgrass supply chain involving 31 farms, 1 centralized storage, and 1 biorefinery. The harvesting period of 120 days is divided into 15-day time steps. In the rest of the year, divided into 60-day time steps, flow variables for farm activities are not generated. The model requires 5,706 seconds of CPU time on a Dell PowerEdge 1900 server with 8 processors, a more powerful computer than our portable PC. So, although the instances compared differ substantially, it seems that our model can tackle larger supply chains, in a more flexible way, and in shorter CPU times.

7 CONCLUSION

A mixed integer linear programming (MILP) model was formulated to optimize biomass supply chains. The state-task network used to describe a chain is very flexible, since its allows to model in details farm activities, equipment selection, pretreatments, storages, and transports, for different crops and multiple products per crop, over a one-year planning horizon divided into days or weeks. The state-task network and other data such as resource characteristics are described in a database from which the mathematical model is automatically generated.

Although this MILP can already solve instances of respectable size, simplifications were introduced to reduce the number of variables, in particular integer variables. One of these simplifications, the macro-task system which aggregates all states and tasks related to harvesting activities in a farm, has made possible the exact resolution in less than one minute of a large instance with 460 biomass production zones, 46 centralized storages and 1 refinery, over 52 weeks. Instances of that size have never been solved so fast in the literature, especially for such complex supply chains.

The database and the model have been designed carefully to evolve easily, for instance new crops or harvesting chains and multiple refineries can be already handled. They are already integrated in a software prototype from which the development of a commercial version is foreseen.

The next step of our work will be to study dedicated algorithms, such as decomposition techniques, Lagrangean relaxation, and metaheuristics, for large-scale problems beyond 500 farms. We wish also to add to the model not only the possibility of using multi-modal transportation and tackling uncertainties in biomass availability, but also multi-objective optimization in the Pareto sense, to minimize both cost criteria and environmental impacts (up to now these criteria can be coped with, but only in a weighted sum).

ACKNOWLEDGMENTS

This work was carried out, in partnership with the SAS PIVERT, within the frame of the French Institute for the Energy Transition (“Institut pour la Transition Energe´tique”) PIVERT (www.institut-pivert.com), selected as an Investment for the Future (“Investissements d’Avenir”). This work was supported, as part of the Investments for the Future, by the French Government under the reference ANR-10-IEED-0001-01.

REFERENCES

  • 1
    BA BH, PRINS C & PRODHON C. 2016. Models for optimization and performance evaluation of biomass supply chains: An operations research perspective. Renewable Energy, 87: 977-989.
  • 2
    BAKKEN BH, SKJELBRED HI & WOLFGANG O. 2007. eTransport: investment planning in energy supply systems with multiple energy carriers. Energy, 32: 1676-1689.
  • 3
    CUNDIFF JS, DIAS N & SHERALI HD. 1997. A linear programming approach for designing a herbaceous biomass delivery system. Bioresources Technology, 59(1): 47-55.
  • 4
    DE MEYER A, CATTRYSSE D, RASINMÄKI J & VAN ORSHOVEN J. 2014. Methods to optimise thedesign and management of biomass-for-bioenergy supply chains: A review. Renewable and Sustainable Energy Reviews, 31: 657-670.
  • 5
    DUNNETT A, ADJIMAN C & SHAH N. 2007. Biomass-to-heat supply chains: Applications of process optimization, Trans. IChemE Part B (Process Safety and Environmental Protection), 85(B5): 419-429.
  • 6
    EKSIOGLU SD, ACHARYA A, LEIGHTLEY LE & ARORA S. 2009. Analyzing the design and management of biomass-to-biorefinery supply chain. Computers & Industrial Engineering, 57(4): 1342- 1352.
  • 7
    EKSIOGLU SD, LI S, ZHANG S, SOKHANSANJ S & PETROLIA D. 2010. Analyzing the Impact of Intermodal Facilities to the Design and Management of Biofuels Supply Chain. Transportation Research Record. Journal of the Transportation Research Board, 144-151.
  • 8
    HAQUE M & EPPLIN FM. 2012. Cost to produce switchgrass and cost to produce ethanol from switchgrass for several levels of biorefi y investment cost and biomass to ethanol conversion rates. Biomass and Bioenergy, 46: 517-530.
  • 9
    KONDILI E, PANTELIDES CC & SARGENT RWH. 1993. A general algorithm for short-term scheduling of batch operations - I. MILP formulations. Computers and Chemical Engineering, 17(2): 211- 227.
  • 10
    LIN T, RODRÍGUEZ LF, SHASTRI YN, HANSEN AC & TING KC. 2014. Integrated strategic and tactical biomass-biofuel supply chain optimization. Bioresource Technology, 156: 256 266.
  • 11
    LIN T, RODRIGUEZ LF, SHASTRI YN, HANSEN AC & TING KC. 2013. GIS-enabled biomass-thanol supply chain optimization: Model development and Miscanthus application. Biofuels, Bioproducts and Biorefineries, 7: 314-333.
  • 12
    SAMSATLI S, SAMSATLI NJ & SHAH N. 2015. BVCM: A comprehensive and flexible toolkit for whole system biomass value chain analysis and optimisation - Mathematical formulation. Applied Energy, 147: 131-160.
  • 13
    SHABANI N & SOWLATI T. 2013. A mixed integer non-linear programming model for tactical value chain optimization of a wood biomass power plant. Applied Energy, 104: 353-361.
  • 14
    SHAH N, PANTELIDES CC & SARGENT RWH. 1993. A general algorithm for short-term scheduling of batch operations - II. Computational issues. Computers and Chemical Engineering, 17(2): 229- 244.
  • 15
    SHASTRI Y, HANSEN A, RODRIGUEZ L & TING KC. 2011a. Development and application of BioFeed model for optimization of herbaceous biomass feedstock production. Biomass and Bionergy, 35: 2961-2974.
  • 16
    SHASTRI Y, HANSEN A, RODRIGUEZ L & TING KC. 2011b. A novel decomposition and distributed computing approach for the solution of large scale optimization models. Computers and Electronics in Agriculture, 76: 69-79.
  • 17
    VAN DYKEN S, BAKKEN BH & SKJELBRED HI. 2010. Linear mixed-integer models for biomass supply chains with transport, storage and processing. Energy, 35(3): 1338-1350.
  • 18
    TECHNICAL DATA AND COSTS FOR VARIOUS FARM EQUIPMENT. http://www.marne.chambagri.fr/gerer-mon-exploitation/bareme-dentraide.html
    » http://www.marne.chambagri.fr/gerer-mon-exploitation/bareme-dentraide.html
  • *
    Invited paper.

Publication Dates

  • Publication in this collection
    Jan-Apr 2018

History

  • Received
    12 Jan 2018
  • Accepted
    15 Jan 2018
Sociedade Brasileira de Pesquisa Operacional Rua Mayrink Veiga, 32 - sala 601 - Centro, 20090-050 Rio de Janeiro RJ - Brasil, Tel.: +55 21 2263-0499, Fax: +55 21 2263-0501 - Rio de Janeiro - RJ - Brazil
E-mail: sobrapo@sobrapo.org.br