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By William T. Griswold

Few metals or industrial minerals can boast a better growth record over the past fifteen years than the borates. This period of growth occurred before the influence of any large-scale use in plastics or high-energy fuels. These new developments not only provide expanding markets, but the programs related to their development are generating research information that will lead to many other new uses. The most dynamic growth areas for refined products of boron or borates are in the acid, the oxide and the reduced forms, such as the metal and the hydrides. Expanding requirements for these products will modify the emphasis on the use of naturally occurring sodium borates. Any borate from which boron can be economically extracted will become a potentially important ore. This is particularly true of the calcium borate, colemanite. Only one large deposit in the Western World has ever been developed where the principal economic minerals are sodium borates, This factor alone would discourage any exploration program directed solely toward the discovery of these ores; on the other hand, ample exploration opportunities for calcium borates exist in the desert regions of California and Nevada. It is therefore reasonable to restrict a program to this region, in spite of geologically favorable areas in foreign countries such as Turkey, Argentina and Chile.

Jan 1, 1959

By R. L. Nielsen

The thematic mapper (TM) aboard Landsat II records image data at seven wavelength intervals or bands. Three record the visible region; three record reflected IR energy. A false color image combining bands 7, 4 and 2 rendered as red, green and blue respectively provides maximum discrimination of rock types in arid regions. Structural analyses and interpretation defines regional structures, large volcano-tectonic features intrusive complexes, all which localize mineralization. Special digital processing using the ratio: Band 3 / Band 1 can identify limonites and other iron minerals. The ratio: Band 5/ Band 7 identifies clays and alunite. These ratio images show features and patterns of hydrothermal mineral systems: ?patterns of sulfide and alteration zoning in large porphyry systems, and zones of strong silica, quartz-alunite-illite, and pyrite-sericite in epithermal centers. Thus, digitally processed Landsat TM images are a cost effective and rapid means to recognize altered areas and define targets for large mineralized systems.

Jan 1, 1995

By John R. Duble

Through 1980, demand for cement in the Pacific Basin countries still seemed to exceed output. Availability of cement in the industrialized and developing countries of East Asia, Southeast Asia, and Australasia for the 1975 - 1980 period are discussed in this report. Quantitative data includes production, imports, exports, and apparent consumption. An account of new cement plants and plant extensions is provided. Countries and areas covered include: East Asia---Japan, South Korea, North Korea, Taiwan, China, Hong Kong, Philippines; South east Asia---Thailand, Vietnam, Singapore, Malaysia, Indonesia; Oceania (Australasia)---Australia, New Zealand, New Caledonia, Fiji.

Jan 1, 1982

By S. V. Tracy

The Outokumpu Skim-Air Flash Flotation machine was developed to separate valuable mineral from gangue as early as practical by floating it with specially designed flotation equipment installed in the grinding circuit. Machines already in service have shown the ability to produce final grade concentrate with an increase in overall recovery and flotation rate while decreasing filter cake moisture and reducing fluctuating feed grades to conventional flotation circuits. The first US production test was carried out in a southwestern copper concentrator with successful results. This report describes the results of the test along with an explanation of the process and the benefits obtainable.

Jan 1, 1986

By R. Cooper, K. De Wet, A. Janwong

"Horsehead Metal Products is a zinc refinery in Mooresboro NC treating crude Waelz Oxide (WOX) to produce Special High Grade Zinc by a hydrometallurgical process, comprising leaching, zinc solvent extraction/electrowinning (SX/EW), melting and casting and bleed treatment. Cadmium removal by zinc dust cementation plays an essential role in the bleed treatment circuit to prevent a build-up of cadmium in the circuit. Silica, although not present at significant levels in the WOX feed material (approximately 0.3%), had a significant impact on the efficiency of cadmium cementation with zinc dust, most likely due to the passivation of zinc dust particles with silica gel. Solid/liquid separation efficiency by filter press was also impacted. The silica levels were mapped throughout the circuit in an attempt to identify the source of the silica issues. Adjustments including using PLS as feed to cementation, pH control in WOX leaching and neutralization have been introduced to mitigate the issues created by silica gel in the circuit. INTRODUCTION Located in North Carolina, Horsehead Metal Products Inc. is a hydrometallurgical zinc refinery processing Waelz Oxide (WOX) to produce Special High Grade (SHG) zinc. The flowsheet, known as the Modified Zincex® process, consists of leaching, solvent extraction, electrowinning, melting and casting and bleed treatment as illustrated in Figure 1. Cadmium cementation, part of the bleed treatment process, provides an essential bleed of cadmium from the circuit, as metallic cement. The Cadmium cementation circuit consists of agitated cementation reactors, a zinc dust addition system, filter presses, agitated purification (releach) reactors and a cadmium concentrate filter press Silica can be found in several forms in acid leaching. The first form is fine silicate particles. The size of the particles can vary from one to twenty microns (1). Fine silicate particles can lead to the formation of crud in solvent extraction circuits (2, 3). At Mooresboro, crud has been observed in Depletion, which is part of the solvent extraction circuit. Silica content in the solution in this section is high. The second form of silica is monosilicic acid Si(OH)4, which begins to polymerize almost immediately upon being leached into solution. Monosilicic acid polymerizes to silica gel or a silica precipitate dependent primarily on supersaturation (5). Factors that influence the rate of polymerization include temperature, sulfuric acid concentration / pH, hydrofluoric acid concentration, seeding, and dissolved salts concentration such as zinc and aluminum in the solution (4, 5, 6). In sulfate systems, silica solubility is reported in the range of 150 to 450 ppm of SiO2 (3, 5, 7)."

Jan 1, 2016

By R. W. Utley

Over one half billion tons of coal per year is scalped, classified, deslimed, drained and rinsed, dewatered and final sized on rotary, vibrating, shaking or stationary screens. The vibrating screen is the industry work horse and performs the bulk of the screening functions in the coal preparation plant. There are two major types of brute force mechanical vibrating screens used in coal preparation plants: (1) the two-bearing one-shaft inclined screen and (2) the four-bearing two-shaft horizontal screen. Both of these types are familiar to coal producers.

Jan 1, 1966

By R. J. Heath

Potassium, together with nitrogen and phosphorous, is one of the essential nutrients required for growth. All living things need potash and so the major demand for potash (approximately 95% of, total demand) is as a fertilizer. Traditional agricultural techniques relied on the return of organic materials to the soil to provide nutrient requirements and maintain soil fertility, and the prevailing low crop yields required little in the way of added fertilizers. But agricultural productivity has increased dramatically in recent times, and this increase in crop yields requires substantial amounts of added nutrients to keep the soil fertile. It follows that there will always be a demand for potash. There is no substitute. Other fertilizers that contain N and P are complementary and not competing products.

Jan 1, 1987

By V. K. Gupta

A detailed experimental study of the variations in grinding rate with particle size, particle load, ball diameter, ball load, mill diameter, and mill speed was carried out for a soft cement clinker and a hard cement clinker. The effects of the ball diameter, ball load and particle load were observed to be material (hardness) independent, and those of the particle size, mill diameter and mill speed to be material dependent. A sharp change in the grinding behavior was observed for both the clinkers at about 150 µm size. Below this critical size: (i) the hardness difference between the two clinkers became insignificant, (ii) variation in the grinding rate with particle size became markedly more pronounced, and (iii) mill speed had little or no effect on grinding rate. The importance of these results in the context of process optimization and control is discussed.

Jan 1, 1987

By Bruce H. Mason

The exploration for a commercially acceptable deposit of limestone is consid¬ered by many to be a relatively easy task; however, trying to locate a zone of high calcium limestone of economic thickness within a formation, which outcrops only in a narrow band varying in width from a quarter mile to ten miles, adds considerably to the normal problems experienced during an exploration program. The existence of varying glacial and karst features in the outcrop area intensified the problems encountered and complicated the interpretation of the economic value of the deposit. This paper highlights a recently completed five year exploration program during which approximately 3,900 acres of ground in seven civil townships were evaluated as potential sources of high-calcium limestone. Details are given with respect to the final site chosen and the methods used in determining the suitability of the site. This site exhibited many karat features and several methods were utilized to determine the effect of these features on the gross characteristics of the deposit. Aerial photography for both mapping and interpretation were utilized. Black and white panchromatic photography, black and white infrared and color infrared photography were flown. Resistivity, diamond core drilling and close-interval angering were used to supplement the information obtained from the aerial photography.

Jan 1, 1974

By G. J. Lindenburg

The Velvet mine is located in the Big Indian district of the Colorado Plateau. The general area, also known as the Lisbon Valley district, is about 65 kilometers southeast of Moab, Utah and about 120 Kilometers southwest of Grand Junction, Colorado. As shown by the slide, the Velvet area is typical of the high desert of the southwest United States. The elevation at the decline collar is 1,967 meters above sea level. To date, the Velvet has produced 1.5 million kilograms of U308 and 2.1 million kilograms of V205. The current production averages over 4,000 metric tons of ore per month. Access to the Velvet mine is by a 1,160 meter long decline. Fresh air is supplied through the decline and a 152 centimeter cased borehole. Contaminated air is removed by two 152 centimeter cased boreholes. The east side of the mine is mined using a conventional room and pillar method; whereas the west side is mined as combination conventional and random room and pillar,

Jan 1, 1983

By J. L. Arola

Since start-up of fluxed pellet production in August: 1987, the Minorca Mine has made a number of process changes to improve pellet quality and productivity. Quality improvements include: 1. Installation of a contraction t:ester. 2. Installation of on-line calcium and silica analyzers. 3. Process autocation changes. Productivity improvements include: 1. A second fluxstone storage bin and feeder. 2. A new vacuum pump and disc filter. 3. A filter aid addition system. 4. Enclosing the filter cake reclaim feeder. 5. A new grate bar cleaner.

Jan 1, 1989

By R. V. Ramani

In this paper, the application of the concepts of reliability engineering to the evaluation of longwall system performance is illustrated with data from an operating longwall face. A number of cases are analyzed to highlight the impacts of longwall equipment, geological conditions and outby haulage on systems reliability and availability.

Jan 1, 1988

By Mark E. Gershon

A mixed-integer formulation of the mine scheduling problem is discussed and applied for the purpose of optimizing both the mine production sequencing and the mill blending and processing problems simultaneously. Previous attempts at solving these problems separately, although successful, fail to take into account the interrelationships between these problems. Project structure serves as the outline of this paper, which is directed towards a mining engineering audience. Generalized in its organization, this concept is useful for long, intermediate and short range scheduling. Actual applications are mentioned which show that the concept is also applicable to mining a variety of ores.

Jan 1, 1982

By Paul C. Jones

Summitville is an old mining district located south of Wolf Creek Pass in the southern San Juan Mountains of Colorado at an elevation higher than 3500 m (11,500 ft). The Summitville mine site is about 40 km (25 miles) southwest of Del Norte. The current mine, developed by Galactic Resources Ltd. and its subsidiaries in the mid-1980s, is on the north facing side of South Mountain. The area is drained by Cropsy Creek to the east and Wightman Fork to the north, both tributaries to the Alamosa River. Mining in the Summitville area began in 1870 when James Wightman discovered placer gold on what is now known as Wightman Fork of the Alamosa River. The first vein-type deposits were located in 1873 on South Mountain near the current Summitville Mine. Mining began in the district in 1875 and continued sporadically through 1942. Major mining episodes occurred from 1875 to 1894 and from 1926 to 1942. Total gold production from the mining district through 1949 totaled 7.5 t (240,000 oz). An additional 7.7 t (249,000 oz) were produced during Galactic's tenure. Natural degradation of the outcropping sulfide-rich veins in the area and the early mining activity, including development of the Reynolds, Dexter and Iowa drainage tunnels in the late 1890s, have polluted the streams draining the area with heavy metals and acidic water. Names of the various tributaries to Wightman Fork, such as Iron, Alum and Bitter Creek, testify to this natural pollution. This degradation has reduced, or killed, aquatic life in several area creeks, including Wightman Fork, for many years before recent mining activity.

Jan 1, 1993

During 1993, contraction of indus¬trial economies in Germany (-2%), France (-1 %), Japan (-0.1 %), Eastern Europe (-2%) and the former Soviet Union (-13%) dimmed prospects of a robust economic recovery for North America. Some European countries that suffer from high unemployment and large government deficits have non-com¬petitive cost structures that will require long-term economic reforms to solve. Restructuring in the United States also continued in 1993. The sluggish pace of the US economic recovery, in¬troduction of federal tax increases and the persistence of high levels of unemployment did little to inspire consumer confidence. By the end of the year, however, sales of consumer durable and capital equipment began to grow. Depressed demand for minerals by industrial economies in recession was partially offset by continuing rational¬ization or abandonment of non-competi¬tive productive capacity in Eastern Eu¬rope and the former Soviet Union. Al¬though aluminum, lead, titanium sponge and zinc prices fell, increases in copper and steel consumption helped steady their prices along with prices of some alloys. Cash flow to the mining industry - the primary source of exploration funds - was therefore constrained. For many companies, exploration expendi¬tures were reallocated geographically and in terms of commodities sought.

Jan 1, 1994

By Richard W. Amerman

The final cost and quality of a project employing equipment, labor, and materials is dependent upon the expediency and extent to which each of these parameters are used. An ideal solution then, would be one in which three solvable equations were given for each particular situation. The equipment, labor, and materials could then be solved for, and the perfect job would result. In reality, however, the ideal and most economical solution is seldom attainable by solving three given equations. Therefore, knowledge, experience, and sometimes guesswork must be relied upon when correlating equipment, labor, and materials. Drilling and blasting, in particular, is one operation which normally involves more uncertainty than other operations. It is also an operation in which the outcome is extremely critical for two reasons. First, the cost of the operation that follows drilling and blasting is dependent upon how well the material is fragmented. Second, once the drilling and blasting has taken place, it is impossible to return to the area, without considerable expense, and correct any mistakes that might have been made. Therefore, what is desired is a method by which drilling and blasting operations can be performed yielding optimum results at the lowest cost; this can best be accomplished by having the relationships between equipment, labor, and materials prior to their use. For obtaining best results, the selection of these three relationships must be based on knowledge, experience, and as little guesswork and uncertainty as possible.

Jan 1, 1969

By Denis Yeung

In an effort to find better ways to dispose of potentially toxic material, the effect of longitudinal and lateral dispersion on the dilution of toxic fluids was investigated numerically and experimentally. Homogeneous and non- homogeneous tests were conducted to model this effect for surface mine backfills. These tests used a high-density zone [package] to bury undesirable material. The studies, utilizing inert tracers, showed that an increase in density in a soil will decrease the maximum level of tracer in the discharge. Within the range of experiments performed and using only natural materials, a 65 percent reduction in peak concentration was obtained.

Jan 1, 1982

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 Gary F. Meenan

The industrial practice of froth flotation for upgrading the quality of fine coal is a relatively complex, expensive, and inefficient process when compared to the coarse- and intermediate-size coal cleaning circuits. The differences in cost and process efficiency can be attributed mainly to the lower equipment throughput, the added cost of flotation reagents, and the fact that flotation is typically a manually operated process susceptible to fluctuating feed characteristics that influence the overall operating efficiency. The emphasis in recent years has been on improving the flotation process efficiency and lowering the cost per clean ton. This has been achieved by larger flotation cell designs, implementation of flotation reagent evaluation programs, and improved process instrumentation and control. These developments are reviewed along with other current coal flotation practices.

Jan 1, 1999

By Ellen Amoako Afful, Michael Moats, Guang Xu, Ashish Kakoria

Electrowinning and solvent extraction are crucial steps in the production of high-purity copper. However, safety concerns have been raised regarding the acid mist generated from the electrowinning process. The mist generated results in health risks to workers and damage to machinery and infrastructure. Currently, chemicals and pellets are used to control acid mist. However, the effectiveness of these controls may vary depending on the type of organic solvent used in the solvent extraction process, which can influence the generation of acid mist. This study aims to evaluate the impacts of organic solvents and surfactants on acid mist suppression. In this study, an electrolyte is contacted with organic solvents to simulate the solvent extraction. The electrolyte is dosed with 20 mg/L of surfactant at each contact. Acid mist testing is performed on the electrolyte separated from the organic phase at the end of the solvent extraction step. The mist collected is analyzed to determine the level of acid mist generated. The results of this study indicate that organic solvents and surfactants showed significant acid mist suppression, but with somewhat different suppression efficiencies. After first contact, Licorice and the organic, for instance, showed a suppression efficiency of up to 69.7% but its efficiency gradually decreased as the number of contacts increased.

Feb 1, 2025