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By A. R. Garcia, A. S. Myerson, W. R. Ernst, J. D. Carruthers, M. D. Franke, L. H. Hilzik

A method for removing nickel and vanadium contaminants from spent HDS catalysts involves pretreating the catalyst with H2S followed by extracting the metals with an acidic solution of ferric ion. The ferric ion solution alone removes significant amounts of active ingredients, cobalt and molybdenum; however, by pretreating with H2S, the extraction becomes more selective for removal of Ni and V.

Jan 1, 1988

Published by ?MILOS CONFERENCE CENTER ? GEORGE ELIOPOULOS? Editor Professor Z. AGIOUTANTIS Editorial Coordinator HELIOTOPOS ? PROFESSIONAL CONGRESS ORGANIZERS Layout IRINI KALOGIRU Production HELIOTOPOS ? PROFESSIONAL CONGRESS ORGANIZERS Cover PANAYOTIS PAPASTAMATIS HELIOTOPOS - PROFESSIONAL CONGRESS ORGANIZERS

Jan 1, 2003

By G. G. O. O. Uwadiale

Starting from a crude ore assaying 45.6% Fe, a fine-grained oolitic iron ore was concentrated by the oil agglomeration technique to 90% Fe recovery and 65% Fe assay. The ore required grinding to minus 5 µm to effect adequate liberation, and the technique yielded optimum results at pH 9. The roles of pH, collector, and bridging liquid concentrations on selectivity and yield of iron minerals in the concentrates are discussed.

Jan 1, 1991

By S. D. Thompson, J. C. Dzurino

This investigation mainly focused on designing a bunker system for a large underground coal mine. The primary purpose of this bunker system was to keep high- and low-sulfur coal segregated on the underground belt system. These bunkers were also required for protecting the mine faces from out by belt delays. Methodologies used in developing this plan are briefly discussed. The final design and the procedures formulated for implementing it are also presented.

Jan 1, 1987

By S. Behl

A major limitation in developing successful selective, flocculation schemes is the difficulty encountered in adsorbing the polymeric flocculant only on the desired substrate. In this paper, a correlation between selectivity of flocculant adsorption and separation efficiency is outlined, and a potential technique to achieve selective adsorption of flocculants is discussed.

Jan 1, 1994

By D. J. Barratt

The specification of the prime mover of an autogenous-semiautogenous mill involves an analysis of the likely operating conditions within the mill and the choice of a nominal operating speed. For variable speed mills, the operating range for mill speed has to be defined so that mils power-torque requirement can be matched by the motor power-torque capability. This paper describes how thin relationship can be influenced by ore grindability.

Jan 1, 1995

By Randy J. Mikula

Cleaning of low-rank coals can have several meanings, depending upon the definitions of the terms "low rank" and "cleaning." In general, low-rank coals would be lignite or subbituminous according to the ASTM classification. For the purposes of this summary, cleaning is defined to be any process which materially reduces the proportion of inert material in the coal. For low-rank coals, this often means a reduction in moisture content since moisture is the major inert component in these coals. A brief discussion of conventional cleaning processes is included, as is an extensive reference list.

Jan 1, 1991

By Robert Jedrzejczak

The Endako Mine is an open-pit molybdenum mine located in the north central region of British Columbia, Canada, about 960 km (600 road miles) north of Vancouver. Production for the latter part of 1992 was expected to averaged 63.5 kt/d (70,000 stpd). Of that amount, 27 kt/d (30,000 stpd) was the mill feed. This production is achieved with five 11.5 to 14.5 m3 (15 to 19 cu yd) electric shovels, six Euclid R190 and two Unit Rig M120 diesel-electric haul trucks, and three 320 mm (12.25 in.) electric rotary drills. There are three ore zones delineated into pit areas: the Endako, Denak East and Denak West. Present mill feed source is the southeast stage of the Endako Pit. Stripping is carried out in the south wall stage also of the Endako Pit. The mine high grade aggregate is reduced in the primary and secondary crushing circuits before processing in conventional RM-BM-flotation circuits. The majority of the molybdenum sulfide (MoS2) is roasted on site to produce technical grade molybdenum oxide (M003). A portion is further refined and treated to yield a 99.9% pure MoS2 product.

Jan 1, 1993

By S. R. S. Sastri, K. K. Bhattacharya, K. S. Narasimhan

Experimental results obtained on the recovery of below 0.5 x 10-3m coal fines by flotation employing geometrically similar columns of 0.056m, 0.080m, 0.100m and 0.220m diameter have been presented. The hydrodynamics of such a unit as well as its performance have been related to operating parameters to establish optimum conditions. The results have further been analysed critically in the light of the known relationship on the behaviour of similar systems to assign reasons for the critical factors established in a bid to reduce the empiricism required to be followed in the scale up of such a unit.

Jan 1, 1988

By Erland A. Tillman

The U.S. National Committee on Tunneling Technology under the aegis of the National Academy of Sciences has long recognized that productivity in major underground construction projects could be increased through better contracting practices and better management. Between 1974 and 1978, this Committee has prepared three reports on these subjects. This paper reviews these reports and their recommendations. It covers the extensive actions by the U.S. National Committee on Tunneling Technology to bring the recommendations to the attention of leaders in the underground construction industry and thus further their adoption and implementation. These activities are continuing. Visibility in this session will give these reports and recommendations increased exposure.

Jan 1, 1981

By Henry Brehaut

The International Network for Acid Prevention (INAP) was formed in 1998 by 17 international mining companies to promote significant improvements in the management of sulphidic mine materials and the reduction of liability associated with acid drainage through knowledge sharing and research and development of technology. Since its inception two panels have been formed to identify and move forward with research projects and eight networks have been constituted to initiate interaction and knowledge sharing within the membership in specific areas of technical interest. An INAP web site has been developed to facilitate the sharing of information and to encourage the exchange and development of new ideas.

Jan 1, 2000

By Marian W. Otrebski, Julian A. Korneck

Long distance, overland conveyors require significant capital outlay of which up to 70% may be contributed to the cost of belting. Significant savings may be achieved by identifying possible risk areas and applying modern technology methods to reduce or eliminate risk. Recently, Sasol Coal commissioned an overland belt conveyor system comprising three belt conveyors of 7 km, 5 km and 4.5 km in length. These were designed and constructed taking the above into consideration. Contained in the paper are the belt conveyor system requirements, designing assumptions and methods applied in the designing process as well as ways and means to eliminate or at least reduce risks.

Jan 1, 1998

By Jorgen Elbrond, Xiaoli Tang

In this paper we apply continuous-time option pricing theory (Dixit 8 Pindyck 1994) to show how to obtain an optimal investment rule for a mining project which requires sequential in- vestments. The application per se is to some extent very simple. The main purpose of the paper, however, is to draw the attention of mining people to how the option pricing theory may be used to capital investment decisions. This topic in economics is quite new but is attracting a lot of attention.

Jan 1, 1996

By James P. Cooney

The global mining industry is in the process of redefining its activity and purpose in terms of sustainable development. This process is impelling a growing number of companies to engage their stakeholders on environmental and social issues. Nongovernmental organizations (NGOs) have customarily acted as critics of the mining industry's performance. A new relationship between mining companies and NGOs is emerging in the context of sustainable development, ranging from dialogue to joint action. If positive interaction among mining companies and NGOs is to succeed, clear terms of engagement must be articulated, and measurable progress toward achieving both corporate and NW objectives must be demonstrated. The experience of Placer Dome is illustrative of the rewards and challenges of engaging with NGOs.

Jan 1, 2001

By Frank Palkovits

All technologies move through a cycle from infancy to maturity. Thickened tailings have moved into the young adulthood phase of its development. Many mining companies like the idea of reducing their water-taking and water disposal issues. This limits the risks associated with traditional surface water-covered tailings facilities and the reduced dilution possible through underground disposal of thickened or paste tailings. Just as home theater systems advertised as ?plug and play? are rarely quite that straightforward, implementing and improving a thickened-tailings system has its challenges. However, the technology has also developed in recent years so it is more accessible. Some success factors have emerged because of the new technologies. Is thickened tailings the right solution? The first step in success with thickened tailings should be whether it is, in fact, the right solution for a particular mine. And, if so, what type of thickening is best. The answer depends on several factors, including: ? Grain size: The grain size that is optimal for maximizing mill recovery is some-times not suitable for thickening. Other mineralogical factors, such as mica content, may also influence whether the tailings are suitable. ? Water issues: Available water does not always have the purity necessary for the process. Another issue to consider is that if water is in short supply, as is increasingly often the case, thickening may be a way to reduce the need to both take and dispose of water.

Jan 1, 2008

By Henry R. Tiedemann, William H. Hansmire, Harvey W. Parker

Although the use of precast concrete segments for tunnel linings has been common for many years in Europe, acceptance of this type of lining has been slow in the United States. This paper explores the cost, design, and construction considerations of concrete segmental lining with a view to promoting its use in this country when favorable conditions exist. The different perspectives held by owners, designers, and contractors are discussed. In addition to cost, other considerations include previous design and construction experience, size, length and function of tunnel, watertightness, and liability. Cost comparisons are made to traditional ground support and lining. Under favorable conditions, the use of precast concrete segmental linings can be technically feasible and cost effective.

Jan 1, 1987

By J. P. Golightly

The nickeliferous laterites of Soroako are described in their setting in the huge Cretaceous ultramafic complexes of central Sulawesi, Indonesia. The ore bodies occur on spurs, ridges and hill flanks beneath remnants of extensive erosional surfaces. Weathering pro- files that have developed on unserpentinized harzburgite and on strongly serpentinized lherzolites show distinctive laterite structures, mineralogy and chemistry. The former are unique to the Soroako area and permit an unusual degree of upgrading by rejection of unserpentinized peridotite boulders. A mass balance calculated for a selection of profiles indicates that in situ leaching of a column of peridotite 20-50 meters thick has taken place with only minor lateral migration of nickel in solution.

Jan 1, 1979

By D. W. Fuerstenau

In mineral processing, the last century of the current millenium has been the century of froth flotation. The process did not result from fundamental research, but was developed over the years by empirical methods. In more recent years, our understanding of the fundamental principles of the flotation process have made significant strides. This paper reviews some of the historical perspectives of developments in flotation reagents, the development and application of experimental tools for delineating flotability and interfactial phenomena, advances in flotation fundamentals, and the development of flotation kinetics, both macroscopic and microscopic subprocesses. Through the application of surface chemistry, the flotation process has permitted economic utilization of a vast array of complex ores.

Jan 1, 1999

By L. G. Closs

Gold continued to be the primary focus of minerals exploration worldwide during 1995. Other targets, though, included primary diamonds and base metals, especially copper deposits amenable to solvent-extraction/electrowinning (SX/EW) processing. The discovery of nickel, copper and cobalt at Voisey Bay in Labrador, Canada was an unusual surprise. Meanwhile, exploration geochemistry continues to evolve to meet new challenges. The major event in this category during 1995 was the17th International Geochemical Exploration Symposium (IGES) held in Townsville, Queensland, Australia in May. The meeting was sponsored by the Association of Exploration Geochemists, which celebrated its 25thanniversary of service to the mineral industry, and the Economic Geology Research Unit of James Cook University, Townsville.

Jan 1, 1996

By David J. Collins

The emergence of activated charcoal adsorption as the most popular recovery method for precious metals, has led to numerous innovations aimed at increasing the efficiency of the process. This article describes a change in traditional charcoal transfer methods which will aid in reducing charcoal attrition losses. Studies have shown that significant charcoal attrition takes place during transfer, be it when using airlifts or centrifugal pumps. Tests conducted at Pinson Mines indicated a 4 to 8% loss to the minus 20 mesh fraction of charcoal after three (3) hours of pumping charcoal. Tests conducted while the author was at Jerritt Canyon indicated that charcoal transfer was a major contributor to charcoal losses; a decrease in the amount of coarse charcoal (plus 12 mesh) and an increase in the amount of finer charcoal (minus 16 plus 20 mesh) was noted as charcoal was moved to the head of the adsorption circuit.

Jan 1, 1998