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By S. Forgeron

Presentation ? Introduction ? Canadian Underground Coal Mines ? Standardization of Geological Assessment ? Geomechanics Base-line Studies of Canadian Coal Mines ? Cape Breton Development Corporation Prince Mine ? Quinsam Coal Corporation ? 2 North and 4 South Mines ? Smoky River Coal Corporation 5B-4 Mine ? Conclusions and Baseline Comparison ? Figures

May 1, 2001

By Jef M. van der Zel

The idea of veneering rich yellow gold alloys with a low-melting, high expansion porcelain, has been a driving force for metal-ceramic research in dentistry. Since 1990, with the advent of the Carrara System (1), a low firing temperature veneering ceramic allowed the use of gold alloys with a lower content of platinum and palladium than the traditional gold-platinum ceramic alloys and thus a richer yellow color. The earlier high gold-platinum ceramic alloys contained at least 12 percent platinum group metals to allow for dimensional stability when firing the relatively high melting traditional ceramics. This amount of platinum group metals gave the alloys a greyish tinge which made them unattractively steel colored and difficult to present as ?high gold alloys?. In the 90?s the new generation universal low-melting, high expansion gold alloys gained market share at a steady rate, starting in Germany, and have now for a great part replaced the traditional gold-platinum alloys (Fig. 1). The first alloys contained 75 wt-% gold and up to 9 wt-% platinum or palladium. They provided a metal-ceramic system in which a gold alloy having an aesthetic yellow colour is fired on with a dental porcelain tailored thereto. The tailoring is meant in respect of compatible coefficients of thermal expansion, and compatible melting or softening points of metal and porcelain. The major concerns in the beginning were with thermal stability during firing, the thermal expansion coefficient of the alloy against the porcelain (compatibility) and the yellow color. In a later stage, alloys with gold contents in the range of 50-60 wt-% gold were developed in analogy with the pale yellow gold-reduced alloys that were formerly used for crown & bridge work and the white gold-reduced alloys used for metal veneering where gold was substituted in part by palladium.

Oct 1, 2003

By Jennifer Pakula

Productivity improvements in underground mining are becoming harder to find. Most mines quickly identify deficiencies in their processes and then struggle to make productivity gains beyond that plateau. One way to increase productivity in this situation is to modify existing methods of operation. Vale?s Stobie Mine has been in operation since the late 1800?s employing a variety of mining methods. Many mining advances have been incorporated over time. With the advent of mechanized rubber tired equipment, sublevel cave mining was introduced to allow economic extraction of a large low grade area. Additional productivity gains were seen in the sublevel cave area with the introduction of preloading production drill holes. In preloading, the holes are loaded with bulk emulsion ahead of the production cycle and then primed for blasting as needed. The introduction of preloading, although giving the Stobie sublevel cave process an overall productivity gain, saw an increase in oversize due to the collar priming technique employed. Handling oversize material prohibited the operators from handling additional units of optimally sized material. Prepriming, adding detonators at the toe and midcolumn of the production holes during the preloading process, was identified as a change that could reduce the formation of oversize. This paper describes the introduction of prepriming to the sublevel cave mining method and focuses on the process Stobie employees followed to ensure a safe transition to this productivity improvement.

Nov 1, 2011

By J. Fournier

A novel sol ? gel (SG) synthesis procedure utilizing varying ratios of glycine and ethylene glycol to total metal cations has been developed to create high purity nanometer sized La0.65Sr3.5MnO3 powders. X-ray powder diffraction (XRD), transmission and scanning electron microscopy (TEM, SEM), and dynamic light scattering (DLS) have confirmed that the crystallite sizes of such powders are ~ 20 nm, and the aggregate particle sizes vary between 100 to 300 nm. Mixing varying weight percents of SG LSM powders with commercially available Praxair LSM in a composite LSM/YSZ functionally graded cathode has been shown, through the use of electrochemical impedance spectroscopy (EIS) and cyclic voltammetry (CV), to exhibit enhanced oxygen reduction kinetics vs. at conventional cathode materials.

Jan 1, 2005

By L. Sun

Recently, micro-tubular solid oxide fuel cells (SOFCs) have attracted the attention of many researchers because of their numerous advantages over larger tubular and planar SOFCs. These include excellent thermal shock properties giving rapid startup/shutdown capability, a high volumetric power density compared to larger tubular SOFCs, and reduced sealing problem compared to planar SOFCs. In order to screen cathode materials for micro-tubular SOFCs, the perovskite cathodes were deposited, using a variety of methods, on 10.5 mol % yttria-stabilized zirconia (YSZ) tubes. Their electrochemical properties were then evaluated by using electrochemical impedance spectroscopy and steady-state polarization methods, based on a three electrode configuration, and with the reference electrode position carefully optimized. The oxygen reduction reaction kinetics at the cathode/electrolyte half cell were then investigated in detail.

Jan 1, 2005

By Guy Chevalier

QCM?s pellet plant, located in Port-Cartier, Quebec, produces up to 8.6 million tons of iron ore pellets annually. Four different types are produced: three for blast furnace operations and one for direct reduction furnaces. The paper presents the scientific approach that led to the installation of new process equipment to improve the reducibility of direct reduction pellets (DR pellet). The findings, the equipment selection and some post start-up modifications are presented. This low silica DR pellet is used in Midrex and HyL shaft furnaces. A good DR pellet has to meet strict chemical, physical and metallurgical specifications. An important metallurgical property is its ability to release oxygen when exposed to reducing gases. Considering that the market for DR pellets is expanding and being aware that reducibility is critical for our clients, a program to improve the latter was undertaken. Test work showed that one factor which has a negative effect on reducibility is the proportion of particles larger than 75 microns. Knowing that the best way to reduce the amount of coarse particles was to close our open grinding circuits, we began evaluating the most suitable classification equipment applicable to our process operations. We settled on hydro-classifiers based on their very sharp cut and their low operating costs. In light of the hydro-classifiers performance it was also decided to replace the hydro-cyclones of an already closed circuit.

May 1, 2003

By Chin J. Chang

Powder metallurgy (P/M) technique is known for its capability of producing near-net-shape parts. Its specific characteristics have resulted in low cost and eliminated of many secondary machining. However, more and more P/M parts do require additional operations to fulfil their complex geometric features and surface roughness. Many of the machining factors that influence the machinability of cast and wrought steel parts, such as cutting speed, feedrate, coolant, tool geometry and shape, are also considered in the machining of P/M components. The special feature in P/M structure is the porosity that can decrease the machinability and shorten the tool life. Different variables have been considered in the machinability of P/M materials. Densities and the free machining additive manganese sulphide (MnS), are the two main factors of material composition, which dominate the P/M machining performance. Machining process is the main method that generates the desired working surface of machining components. This paper will discuss the metallurgical structure of the powder metallurgy components, their physical properties and possible issues when encountering machining operation. Turning operation has been tested in this investigation to show the relationship between the cutting speed, federate, cutting forces and chip formation. This investigation also discusses how the free machining additive, manganese sulphide, affects the P/M structure and machinability in order to understand how the metallurgical structure can affect the machining operation and, how to obtain the optimised surface results.

May 1, 2001

By Anthony Finch

Many mines combine open pit with underground mining, and on many occasions the underground mine is an extension of the open-pit. In these circumstances the decision about where the open-pit stops and the underground starts is crucial and driven by many factors. This paper looks at some of the ways that this cut-over can be calculated and specifically examines the calculation of it using modern mine optimization software. The paper provides a case study which will review various outcomes using these techniques, and demonstrates the influence of various factors on the optimal transition cut-over point. Biographies Mr Finch is a Divisional Manager and a Principal consultant at Snowden Mining Industry Consultants in Vancouver, Canada. At Snowden Mr Finch leads a team of engineers that perform mining engineering studies for projects around the world. Prior to joining Snowden Mr Finch was the Mining Manager at Barrick?s Henty mine in Tasmania Australia. Prior to that Mr Finch has held a variety of roles in both consulting and operations working for various organisations at various levels in the Asia Pacific region. Mr Finch gained a bachelor?s degree in Mining Engineering from the University of Queensland in 1986, and a bachelor?s degree in Economics from the University of Queensland in 1993. His expertise is in mine planning, mine optimisation and mine management. Dr Elkington is a Consultant at Snowden Mining Industry Consultants in Perth, Australia. He is responsible for the design and implementation of Snowden?s proprietary optimization software products. Prior to joining Snowden Dr Elkington completed his PhD in Mine Optimisation at The University of Western Australia, and bachelor?s degrees in Engineering (Hons) and Commerce from The University of Western Australia. He specialises in optimization and trade-off studies, and has consulted on projects across all major commodities and regions.

May 1, 2011

By A. Gillis, J. Keyes

"This is a prelirr1inary report on automatic control at East Malartic Gold Mines.After installation of the cyclones in the East Malartic grinding circuit, the interest was aroused in the automatic control system for the circuit. Investigations were made as to the possibilities of such an installation. This resulted in a preliminary survey of the circuit by Milltronics Ltd and an analysis of the circuit by Mines Branch personnel. A study of the investigation and analysis indicated that a cost reduction and improved efficiency could be expected by the installation of an automatic control system in the grinding circuit. It was also indicated tl1at such installation should pay for itself within a year. This was the point that sold management on such installation. The need of three operators was expected to be eliminated .The installation was to consist of a central control panel, microphoncs on each mill, regulation of feed rate, pneumatic valves for addition of solt1tions, density control of the cyclone overflow, which is a grinding circuit product, rod mill feed box plugging detector and a conveyer weightometer for tonnage indication and control.As well as the elimination of one man per sl1ift, other benefits which were to be received but unable to estimate were: 1) More tonnage per clay by operation of the mills at the proper capacities. 2) Lower grinding costs. Less under-loading should result in less steel wear and lower pumping cost. In the condition of overloading, a coarser grind is obtained resulting in greater impeller and liner wear. The overloading and underloading showed up on the n1icropl1oncs. 3) An improvement in the recovery as a result of less over-load. The tailings loss from a coarser grind are not as frequent."

Jan 1, 1965

By R. Tipman

"In 25 years, processing of tar sand progressed from two small pilot plants to two major commercial operations owned by Syncrude and Suncor. These plants mine tar sand and extract the bitumen which is then converted into a synthetic crude oil. Considerable research on extraction of bitumen from tar sand has been undertaken by these two companies as well as other major oil producing companies, private individuals, universities and the federal and provincial governments. These studies have produced a number of alternate processing schemes which have yet to be commercialized. The producing companies are focusing their efforts on achieving increased processing efficiency, which includes improved bitumen recovery, reduced unit cost, energy conservation, and equipment reliability. In this review, the Syncrude process and examples of new process developments will be briefly described. IntroductionTwenty-five years ago, tar sand processing was limited to two pilot plants owned by Cities Service Athabasca Ltd., and Great Canadian Oil Sands. Earnest Manning was Premier of Alberta and was inviting proposals for the construction of a commercial tar sands plant. The invitations called for a much larger operation than those which had been undertaken in the past. All of the previous attempts at commercial operations up to 1960's had failed, largely because of a poor technical understanding of the process requirements, lack of suitable equipment, and lack of adequate capital. The previous record was not good. The pending new large scale plant was based on improved but not proven technology and equipment, which were developed from the pilot plant studies. In addition, the surplus of conventional oil in Alberta and low world oil prices were factors reducing the need for such a plant."

Jan 1, 1987

By Ajit K. Sinha

"Electromagnetic surveys were conducted over the Yava sandstone-hosted lead deposit in Nova Scotia to evaluate the usefulness of such surveys for detecting and mapping sedimentaryhosted metallic ore deposits. Both transient and multifrequency systems were used for that purpose. The deposit consists of three zones of disseminated galena which also contain minor amounts of pyrite and sphalerite filling the interstices of the sandstone grains. Each zone overlies a basement depression and is separated from the adjacent zone by an intervening basement high. A conductive shale layer underlies the galena-rich sandstone formation at all three zones.Because the concentration of galena (3070 to 4% ) and other sulfides is too low to affect the resistivity of the sandstone formations for detection by ground electromagnetic (EM) methods, the strategy for our survey was to look for areas of basement depressions and the presence of conductive shale in those depressions by EM depth soundings. The presence of the galena-rich sandstone formations could be inferred because of the close association of these two features with the deposits in the Yava area. Both transient and multifrequency EM systems were successful in mapping the basement depressions and detecting conductive shale at the three known mineralized zones. The technique, therefore, seems to offer good prospects for mapping similar stratabound sedimentary-hosted sulfide deposits."

Jan 1, 1993

By U. Dillon, G. Blackwell

"Geographic information systems (GIS) provide an efficient means for the recording, manipulation, revision, display and analysis of spatially referenced data. GIS are widely used at the exploration stage of mine development, and are increasingly used for reclamation planning. The ability of a GIS to perform spatial searches and query spatially referenced data make it a powerful tool for use at all stages of mine development. As the amount of data available for analysis increases, so does the power and flexibility of GIS as a planning tool.Starting from the exploration database, this paper describes how a GIS can be used for the development of mining plans based on topography, geology and mineralization information stored in a relational database. Planning decisions approaching the optimal can then be made for a wide range of parameters, including stockpile and waste dump locations, the location of potentially acid generating and neutralizing material for dump design, profitable and risk-controlled mine extraction sequencing, and haul road locations. This is made possible by the overlay and buffer analysis capabilities of a GIS which are explored and exploited to produce a continuous mine production planning program, as well as site remediation and reclamation using a successful case study. The Ore and ProductsThe mines in the Saskatoon area — Agrium, PCS-Cory, PCS-Allan, PCS-Patience Lake, PCS-Lanigan and IMC-Colonsay — extract the ore from the Patience Lake member. The mines in the southeast corner of Saskatchewan — IMC-K1 and K2, PCSRocanville — extract from the Esterhazy member, while IMC-Belle Plaine, near Regina, solution mines potassium chloride from both potash-bearing members.Ore from the Patience Lake member is a medium-grained mixture of sylvite and halite, with a KCl content of 36%, insolubles averaging up to 5.5%, and little or no carnallite.The ore from the Esterhazy member is a coarse-grained mixture of sylvite (KCl) and halite (NaCl) with a small amount of water insolubles, and some carnallite (a K-Mg chloride). Average run-of-mine grades are about 30% KCl."

Jan 1, 2003

By V. I. Birss

Planar solid oxide fuel cells (SOFCs) offer great promise as stationary power generation devices, primarily due to their flexibility in terms of fuels, high energy conversion efficiency (when both electricity and heat are captured), and their relatively low fabrication costs. However, the anode performance can be compromised by such factors as exposure to certain sulfur-containing fuels and the deposition of coke when using hydrocarbon fuels. In terms of the cathode, its performance is limited primarily by the slow kinetics of the oxygen reduction reaction, while its lifetime can be negatively affected by factors related to the corrosion of currently used stainless steel interconnect materials. This talk will present an overview of these challenges and some possible solutions to these problems. The presentation will also focus on how electrochemical methods can be used to evaluate and improve the performance of SOFC anodes, cathodes, and interconnect materials. In addition, recent promising research efforts directed towards performance enhancement of SOFCs through the use of nanoscale electrocatalysts will be discussed.

Jan 1, 2005

By S. M. Bulatovic, D. M. Wyslouzil, K. R. Rawlings

"The suitability of a new organic reagent DS20 as a depressant for oxidized and carbonaceous pyritic lead-zinc ore from Nanisivik Mines Ltd. has been evaluated in the laboratory and in the plant.The depressant DS20 is a mixture of Lignosulphonate-Dextrin-Quebracho and was developed specifically for depression of highly oxidized and carbonaceous pyrite.The laboratory test work indicated that the poor metallurgy resulting from the oxidized ore could be improved to normal plant performance by the addition of the DS20 depressant with the existing plant reagents. The laboratory data suggested that lime consumption could be reduced when using DS20.In this paper, the development work and the plant trials with DS20 are described.INTRODUCTIONNanisivik Mines Ltd. treats approximately 2000 tonnes per day of lead-zinc massive sulphide ore, containing currently 1% Pb and 9% Zn. The concentrator operations have been described previously (1,2) and typical metallurgical performance is detailed in Table I.The concentrator flowsheet (Figure No. 1) and the standard reagent scheme (Table No. 2) demonstrate the relative simplicity of treatment of this coarse grained ore.A recently discovered satellite orebody - Area 14 - containing 2% Pb and 12% Zn was brought into production in October 1983. This ore had been oxidized to varying degrees by ground water; the pyrite mineralization was found to be very fast floating and a carbonaceous constituent present in higher than normal proportion also affected flotation. The simple high lime addition could not control the pyrite, and very low grade lead concentrates resulted; zinc metallurgy was also affected by this oxidized condition (Table 3)."

Jan 1, 1986

By Richard Morland

The Ekati Safety Guarantee is a conversation that has been taking place at Ekati for the last two years. It is a challenging, confronting, inspiring conversation which encourages people to see and pursue the possibility of guaranteeing that nobody who works at Ekati will be seriously injured or killed at work. The conversation takes us out of the normal, incremental approach to safety improvement; it takes us out of the world of striving, of seeking, of trying, and allows us to stand in, and be a stand for the future possibility of Zero Harm. It requires an unreasonable stand for, and commitment to, our own safety and the safety of our colleagues. A Powerful Conversation The safety guarantee began with conversations between executive team members and has been propagated regularly through the line through management meetings, pre-shift meetings, during workplace inspections, job safety observations, job and project planning, orientation and induction sessions, and when opportunities present themselves. This is a conversation that continues outside of Ekati with family, with government, with community members. It is a stand for safety as a value. The conversation about the safety guarantee is now pervasive at Ekati and forms part of a framework of initiatives that have led to sustained improvement in safety performance. During the last two years, the recordable injury frequency at Ekati has dropped to its lowest level in Ekati?s history. At the same time, job safety observations have increased from 500 per month to 4000 per month, whilst the overall number of people at Ekati has reduced by 30%. It has led to new ways of thinking about the conduct of operations. It influenced the 2008 upgrade of the Ekati process plant, resulting in the development and implementation of a crane lift protocol that eliminated injuries during over 100 lifts in two weeks, in an area of difficult geometry and with multiple entrances. It created space to successfully conduct a challenging commissioning period for the process plant crusher, during which time the machine was disassembled and reassembled several times, without incident or injury. No production pressure was permitted to interfere with this work, in line with our stated aim that we wanted everyone involved to guarantee that they would not be seriously injured or killed?our people had the space to do the work at a pace, and in a way, that guaranteed this outcome.

May 1, 2010

By John C. Loretto

"Answers to some of the problems ofRecovery and Metallurgical AccountingIn Gold and Silver Hydrometallurgical PlantsThe start-up over the last few years of new hydrometallurgical plants for the recovery of gold and silver has brought to the surface again a number of problems. Most of the problems have existed for some time and they manifest themselves mainly in two ways. Firstly, the plant results do not agree with the Metallurgical Test work figures and secondly, the Metallurgical Accounting figures do not balance.The plant results not agreeing with testwork figures are mainly due to:a) The testwork samples were not representative of the eventual plantfeed;b) Misinterpretation or misunderstanding of testwork;c) Plant losses;d) Plant design not allowing testwork results to be achieved;e) Operating deficiencies.a} The testwork samples being dissimilar to the plant feed occurs on a very high proportion of projects. The effects of this can beccr.ie exaggerated because the upper levels of the mining company often regard the original testwork figures as sacred and therefore base their judgement of current plant performance on these figures.Frequently the test work samples represent only a minor part of the orebody or alternatively a single composite of the whole ore body is used for the testwork long before it has been determined that all of the potentially different ore zones behave in the same manner. These errors can be compensated for by repeating the ""testwork tests 11 on current plant feed on a routine basis and using these tests to determine whether or not the plant is operating satisfactorily."

Jan 1, 1982

By E. Norton

"Even though the subject of this panel discussion is dust control, rather than dwell on the design aspects of dust collection systems which are well documented in numerous publications, :it was considered more pertinent to the present economics of mining to examine the energy costs involved.At the present time, the facts of shrinking fossil fuel reserves and spiralling fuel costs are being constantly brought to our attention. Industry is being motivated to consider the possibilities of incorporating heat recovery systems in areas where they prove to be economical. Unfortunately, it is not a simple exercise to determine if the installation and operation of heat recovery equipment is feasible and economical. Each process involving heat recovery potential must be thoroughly studied in all aspects.In a paper presented at the 1975 Annual General Meeting of the Canadian Institute of Mining and Metallurgy in Toronto, Ontario, entitled ""The Influence of Energy Conservation on Concentrator Design"", it was stated that the largest single energy consumer in winter is space heating with the largest portion of this supplied to crushing and screening plants. (1) Within the scope of this panel discussion we will study, as one example, a crushing and screening plant using natural gas heat in the province of British Columbia and we will explore the feasibility and economics of installing air-to-air heat recovery equipment."

Jan 1, 1976

By M. Eikerling

The full competition between mass transport and reaction in PEMFC unfolds in cathode catalyst layers (CCLs). Recently developed models provide vital insights into effects of thickness and composition on effectiveness of catalyst utilization and performance. However, the CCL's key function in liquid water removal is rather unexplored. Studies of water balance in PEMFCs focus mostly on other cell components. Notwithstanding this prioritization, a simple calculation shows that the CCL is the PEMFC's favourite medium for conversion of liquid water into vapor. Porous structure and wetting properties steer the interplay of evaporation, transport and reaction. A model will be presented, that links pore space morphology, composition, distributed properties (concentrations, pressures, reaction rates, potential) with global performance (critical phenomena). It reveals how problems of flooding in the fuel cell could be mitigated by properly adjusting catalyst layer structure and operation conditions and under which conditions all liquid water arriving in the CCL would leave it as water vapour through the CCL/GDL interface. Results for a simple variant of the model emphasize the role of the CCL as a watershed for the whole cell.

Jan 1, 2005

By A. P. E. Dirige

In order to maximize the recovery of ore in variably dipping ore zones of moderate width, cemented backfill is normally placed to serve as structural support. With the intention of saving on costs, backfill of low cement content can be used, which are often supported by a sillmat of higher strength. The stability of the low cement backfill face, exposed during adjacent mining, must be carefully studied to provide very effective, safe and economic mining operations. Improper design of these stope support structures may result in fill mass failure resulting in relaxation and failure of the stope walls, with consequent losses of production, ore dilution, and in safety problems. This paper presents a study conducted to assess fill performance during adjacent pillar mining and to provide a comprehensive understanding of backfill behaviour, the failure modes that may occur and the consequences to production, ore dilution and to safety problems, and accurately predict their stability. The design study investigated the effects of stope width and height, orebody geometry and inclination, and wall roughness on the stability of cemented backfill during adjacent pillar mining. Fill properties used were based on paste fill specimens cured for 28 days. Paste fill performances were assessed based on analytical and numerical modeling studies for the different mining conditions. Analytical modeling was carried out using limiting equilibrium analysis and numerical modeling was carried out using FLAC3D. The modeling results suggested that, for stopes that are inclined with smooth wall rock conditions, backfill failure, driven by the fill self-weight, has minimum dependency on the binder content and is reduced by resisting forces developed on the footwall-fill contact. For inclined stopes with rough wall rock conditions, wall roughness contributes significantly to the stability of the backfill during adjacent pillar mining. The analytical modeling approach was demonstrated to be useful in providing some approximate parameters for predicting the behaviour of paste fill exposed faces during adjacent mining, but cannot predict the mode or mechanisms of failure. Numerical modeling not only assess the stability behaviour of paste fill free faces, but also is able to provide a better idea of paste fill failure modes and possible failure mechanisms. The depth of failure and the potential for instability for a simulated stope filled with paste fill can be predicted, and may be useful in estimating the mass of material that could possibly fail and ore dilution levels.

May 1, 2009

By M. Carvalho

The primary motivation underlying the proposal of polygeneration systems for mine sites is to increase the efficient use of natural resources by combining different technologies and energy resources while satisfying energy service demands. For many mineral producers, particularly in Canada?s mining extremes of climate and depth, energy in support of mineral production can be the second largest cost centre after labour. A generic methodology is proposed for the design of energy supply systems in mine sites, based on a search for the minimum discounted cost of energy supplied for all feasible different plant configurations. These configurations can be represented within a connectivity matrix which corresponds to a network representation. A Mixed Integer Programming formulation is set out for the multiperiod synthesis and operational planning problem. This is characterized by i) binary variables for the selection of technologies, ii) integer variables for the determination of the number of units installed, and iii) by continuous variables for the representation of energy and economic flows. Through the integration of particular energy supply strategies matching specific mine circumstances (on-grid, remote, degree days, etc) and consideration of technologies that improve energy efficiency, hitherto not considered new technologies and demand management systems or new perspectives on optimal mine site energy supply can be investigated. Some of these investigations identify the economic conditions through which biomass energy feedstocks should be used, for direct heat production, for gasification and providing for Fischer-Tropsch syndiesel manufacture. As well as integrating demand from mobile diesel-fuelled plant into an optimization procedure that hitherto has only been considered for static energy production and consumption plant, this analysis shows how the techniques can be used to explore economic conditions of threshold prices for biomass (purpose-grown biomass and peat are considered herein) and trucked-in diesel. The methodology also allows for electricity and syngas storage and diesel and biomass bunkering. Within the paper the energy demands for a remote, open pit mining operation located in Northern Ontario are considered as a case study to illustrate the technique and investigations. As expected, for mines close to electricity, natural gas, and diesel distribution infrastructures, the optimal choice is to connect. When a constraint is applied specifying that connection is not possible, as would be for the case exemplified, the optimal choice includes some of the more exotic options for mine site energy supply.

Aug 1, 2013