Search Documents

By Gerald H. Luttrell, Joe Shoniker, Jaisen N. Kohmuench, Christopher J. Barbee, Michael J. Mankosa

The HydroFloat technology was specifically developed to upgrade phosphate sands that are too coarse (>0.6 mm) to be efficiently recovered by conventional flotation methods. In this novel process, classified feed is suspended in a fluidized bed that has been aerated using an external sparging system. The air bubbles selectively attach to particles that have been made hydrophobic through the addition of a fatty acid collector. The teetering effect of the fluidized bed forces the low-density bubble-particle aggregates into the overflow, while hydrophilic particles are rejected as a high solids content underflow Since the HydroFloat is actually a density separator, the process can treat much coarser feeds than would be possible using traditional flotation processes. In addition, the high solids content of the teeter bed promotes bubble-particle attachment and reduces the cell volume required to achieve a given capacity. This paper presents test data from ongoing pilot-scale trials of the HydroFloat cell in the phosphate industry.

Jan 1, 2002

By J. Felipe Costa, Andrew H. White, Marcot T. M. B. Vilhena

Ordinary kriiing (OK) is an interpolation algorithm mostly used in earth sciences applications where it provides satisfactory results. Robust kriging (RK) is an alternative algorithm which at- tempts to minimise the problems caused by the existence of outlier values within a given data set. Robust kriging essentially consists of an editing step prior to running the traditional OK method. This study compares the interpolation results obtained by OK and RK. Two data sets were used. The first data set consists of 140 samples mimicking a drilling survey named cluster.dat. An additional feature of this sample data is that its parent population, the reference data set, is available, thus permitting direct quantitative assessment of the effectiveness of a given estimation technique. The second data set consists of a grid sampled at 1x1 m. The estimates obtained by OK and RK using cluster.dat were compared to the reference data set. RK provided better results in terms of quality of the estimates than OK

Jan 1, 1996

By A. M. Al Taweel, S. M. El Mofty, T. A. Hassan, M. R. Moharam, A. M. Ramadan

The axial mixing characteristics of a pilot-scale flotation column were investigated with the objective of identifying means to mitigate the extent of axial mixing that adversely affects its grade/recovery performance. A wide range of design and operating conditions was investigated and the experimental results, obtained using the dynamic response method, were analyzed using three axial mixing models. The dynamic response of the column can best be described using the axial dispersion model. The results obtained suggest that the value of the axial dispersion coefficient, EL. can be signi6cantly reduced by judicial selection of hydrodynamic conditions and/or the use of column inserts that suppress the onset of hydrodynamic instabilities inherent to the operation of conventional flotation columns. Up to 40% reduction in the value of EL was thus obtained by using spargers that produce more uniform bubble sizes, while up to 30% reductions were obtained by controlling the residual frother concentration.

Jan 1, 1995

By William C. Cooley

Modern tunnel boring machines are subject to excessive cutter wear and bearing failures when used in hard and abrasive rock. In very hard rock, the high cost of cutter and bearing replacement, combined with slower excavation progress, make it more economical to drive tunnels by conventional drill and blast methods. The use of high pressure water jets to break rock provides a promising alternative. Experimental data indicate that the specific energy (the energy expended per unit volume of rock broken) decreases as the water jet pressure increases. Continuous jets are generally limited to pressures below 100,000 psi, whereas pulsed jets from a water cannon can attain much higher pressures. Therefore, the Federal Railroad Administration of the U. S. Department of Transportation has sponsored the design (Ref. 1 & 2) and the fabrication and testing (Ref. 3 & 4) of a water cannon to determine its effectiveness in rock disintegration at very high pressures. This paper reports the results of laboratory tests with pulsed jets against large rock samples at pressures of 125,000 to 650,000 psi and field tests against dolomitic limestone and granitic gneiss at pressures near 450,000 psi. Although initial tests were made with a small nozzle, operating at off-design conditions (Ref. 4), this paper only covers results with the full-size nozzle, including 55 laboratory test shots and 67 field test shots.

Jan 1, 1974

By E. Woodburn, R. P. King, R. Putman

Flotation plant simulation, a relatively recent methodology in mineral processing, is defined and corresponding uses are discussed. Typical simulation structures are compared. Current problem areas exist although these are not insurmountable. Following a brief state of the art discussion, the N. I. M. simulation program is reviewed. In general, digital plant simulation is expected to be of substantial benefit in the near future.

Jan 1, 1976

By L. Piga, G. Belardi, V. Alesse, N. Shehu, J. Freund

The physico-chemical interactions among minerals such as olivine, chromite and serpentine; the most commonly present ions in solution such as Ca and Mg; and flotation reagents such as EDTA and oleic acid were investigated. The study was conducted via release tests, electrophoretic measurements and microflotation of selected minerals coming from the Kukes deposit in Albania. The results were confirmed in beneficiation tests on two ores, one from the Kukes (Kalimash) deposit and the other from the Rizo deposit in Greece. It was demonstrated that, when Na-oleate is used as collector, chromite, olivine and serpentine can be separated at pH 2.5 and/or pH 5.5 when employing ethylenediamine tetraacetate (EDTA) on previously deslimed material. This approach ensures flotation concentrates with a Cr203 content better than 50% with a recovery of more than 75%.

Jan 1, 1998

By Timothy P. Smirnoff, Arthur P. Chase, Herman J. Smith

INTRODUCTION The Newtown Creek Pollution Control Project (P.W. 53) is a major system of facilities designed to collect wastewater from large areas of the Boroughs of Manhattan, Brooklyn and Queens, then channel it to a treatment plant where the wastewater is processed and discharged. The North Branch interceptor collects wastewater along the east side of Manhattan and transports it downstream to a Junction Chamber at Avenue "D" near East 13th Street. The South Branch interceptor similarly collects wastewater from the southern part of Manhattan Island on both east and west sides of Manhattan and transports it to the same Junction Chamber from where both flows are delivered to the adjacent Manhattan Pumping Station which pumps the wastewater under the East River to a treatment plant in Brooklyn. This system is shown in Figure 1. Construction of the Manhattan Pumping Station began in the Summer of 1966 and was delayed by a number of mishaps. In the vicinity of the North and South Interceptors, approximately 3,060 cubic meters (4,000 cubic yards) of soil flowed into the excavation: 765 cubic meters (1,000 cubic yards) at the North Branch Interceptor, and approximately 2,300 cubic meters (3,000 cubic yards) at the South Interceptor. These movements were accompanied by surface subsidence, collapse, or both. On June 4, 1973, while pumping station construction was underway, approximately five to seven cubic yards of sand entered the junction chamber through a temporary bulkhead valve in the North Branch Interceptor.

Jan 1, 1979

By T. J. Lyman, M. J. Robison, W. A. Ruemmele

INTRODUCTION The first phase of the Los Angeles Metro Rail Project consists of 7.1 km (4.4 miles) of subway and stations running through downtown Los Angeles from Union Station to MacArthur Park. Contract A171, the Wilshire/Alvarado Line, involves tunnel construction beneath 7th/Street from the 7th/Flower Station to the Wilshire/Alvarado Station. The project consists of the excavation and lininig of 3000 m (9900 ft) of twin-bore, 6.7 m (22 ft) excavated diameter, 5.5 m (18 ft) finished diameter subway tunnels. The location of the project is shown in Figure 1. The majority of the excavation passed through weak siltstone/ claystone bedrock; although, portions of each tunnel approaching the 7th/Flower Station passed through fine-grained alluvium. Both tunnels were excavated with a digger shield. The project also included the excavation and lining of 6 cross passages, 2 communication rooms and a sump, all at tunnel grade between the two bores. A program of geotechnical instrumentation and building monitoring was performed to detect and document the response of the ground and adjacent structures and facilities to tunnel excavation. The instrumentation program was also intended to provide information that would permit implementation of remedial measures, when and as required, to prevent damage to structures, facilities and utilities along the tunnel alignment. The purpose of this paper is to discuss the ground response to tunneling on Los Angeles Metro Rail Contract A171. This paper presents a description of the tunnel project, the excavation and support method used in construction, the subsurface geology, and

Jan 1, 1989

By Charles R. Garrett

The American Borate Company, a wholly owned subsidiary of the Owens Corning Fiberglas Company under a management contract to the Hanna Mining Company, owns and operates an underground borate mine in Death Valley, California. The mine, named the Billie Mine, is located 24 km (15 miles) southeast of Furnace Creek along Highway 190. The ore body is under Death Valley National Monument with the major portion of the surface facilities located just outside the monument boundary. (See Figure 1.) The Billie Mine produces approximately 227 000 metric tons of crude ore per year. About 65% of finished product is supplied to Owens-Corning, the remainder is sold to other fiberglass producers. Geology The borate minerals in the Billie ore body were deposited in the lower main member of the Furnace Creek Formation, which is Pliocene in age. The ore body is thought to have formed from volcanic springs in or near a small lake basin. The deposit is essentially a limestone breccia that is permeated with borate minerals and surrounded with limey lake bed mudstones and shales. The ore body is mineralized with two main borate ores, colemanite and probertite. A third borate ore, ulexite, mainly occurs in the upper part of the ore body. The original mineral of deposition is thought to have been ulexite. Ulexite is a sodium-calcium borate hydrated with eight molecular waters. Due to heat and pressure from burial by later sediments, the ulexite had water forced out of its structure and recrystallized as probertite. Probertite is another sodium-calcium borate, with five molecular waters. Colemanite formed when surface water seeped into the prober-

Jan 1, 1985

By Eric C. Schwamberge, Clem A. Pelletier, Deborah L. Muggli, George W. Poling

The Pit Lake at Island Copper has evolved into a 3-layered meromictic system. Acid Rock Drainage (ARD) is collected and injected into the lake at 220 m depth via 2 diffuser systems. In situ dye studies were conducted during 2 differing hydrological regimes in order to determine the behavior of the ARD plume within the Pit Lake. Results indicated that when runoff from the waste dumps was low, the injected ARD remained within the bottom half of the intermediate layer of the Pit Lake, initially below depths of 90 m. However, when runoff from the waste dumps was high, the injected ARD at -220 m depth rose through the intermediate water column layer rapidly, but did not breach the top pycnocline at -10 m depth. Overall, the system is currently performing as a mixing bowl with a strong boundary or cap at the upper pycnocline. maintaining mixing below the 10 m depth water level.

Jan 1, 2000

By David J. Kruse

The proper modeling of granular flow using discontinuum mechanics has the potential to be one of the most significant scientific advancements in the mining industry today. This paper will examine the status of discrete element technology, specifically focusing on current and future applications. The fundamentals of the Discrete Element Method (DEM) will be briefly introduced, as well as relevant design parameters. Various types of granular flow problems currently being solved using the DEM methodology will be presented. The results and potential benefits of these cases will also be discussed. All simulation results and figures used throughout this paper are from studies and designs preformed by the DEM group at Conveyor Dynamics, Inc. (CDI).

Jan 1, 2000

By Laura J. Carroll, Gordon A. Goldsmith

Experts, like many of the speakers at the SME Annual Conference, are frequently called upon by lawyers to assist them in litigation. Due to the technical nature of many cases, the testimony of an expert with knowledge and experience in a particular field is necessary to help a judge or jury understand and decide certain issues. Environmental litigation is no exception. Experts routinely are called upon to offer testimony to establish the existence of contamination and its source, as well as the potential health and environmental risks associated with the contaminants. This article will briefly discuss the factors courts apply to determine whether to admit expert testimony after the recent Supreme Court decision in Daubert v. Memell Dow Pharm., Inc., 509 U.S. 579 (1993). The Court's decision in Daubert overruled a long-standing test that had based the admissibility of scientific evidence on its "general acceptance" in the field in issue. Next, the article will discuss in general terms what a party must do to "link a particular defendant's conduct to the contamination involved in order to recover from that defendant. This link, known as causation, varies depending upon the type of claim being asserted. Expert witnesses are used extensively to help establish causation. JUNK SCIENCE OR GOOD SCIENCE- HOW DOES A COURT DETERMINE WHAT TO LET IN A frequent complaint in litigation involving technical or scientific issues is that one party or another is trying to use so-called "junk science" to prove its case. While some expert testimony might be so clearly lacking in support or so "off the wall" that a court can easily determine to exclude it, other testimony, especially testimony on the "cutting edge," is much more problematic. In 1923, the District of Columbia Circuit Court of Appeals decided the case of Frye v. United States, 293 E 1013 (1923). In deciding whether to admit certain expert testimony, the court in Frye stated that while a court will "go a long way in admitting expert testimony deduced from a well-recognized scientific

Jan 1, 1998

By Fathi Habashi

OXIDE ORES can be divided into two groups: 1) Simple oxides (Table 3.1). 2) Complex oxides. Those ores containing minerals composed of two oxides; an acid oxide (Cr2O3, Nb2O5, etc.), and a basic oxide (CaO, FeO, MnO), as shown in Table 3.2.

Jan 1, 1970

By J. W. White, J. P. Olson

Computer-based dispatching in open-pit truck haulage operations yields many benefits of current interest to mine management. The key tangible benefit is a substantial productivity increase with a given fleet of equipment or, alternately, a significant reduction in equipment required to meet production quotas. Other tangible benefits in mines with concurrent operating objectives include minimizing rehandle, meeting several blending constraints simultaneously, and ensuring a target plant feed rate. Intangible benefits include production forecasting, performance comparisons of trucks or shovels of different manufacture, and extensive on-line report generation. Recent advances in mini- and micro-computer hardware and software and solid state electronics permit design and implementation of system features not feasible a few years ago. This paper discusses system aspects with emphasis on dispatching algorithms needed to meet concurrent objectives.

Jan 1, 1987

In 1990, US mine production of barite increased 54.1 %. Barite consumption, sold or used by grinding plants, increased by 27.6%. Imports were about the same as 1989. World mine production in¬creased 12.3%, according to the US Bureau of Mines. The value of domestically produced barite, fob mine, decreased 12.7%, according to the Bureau. The declared value, cif US port, of all imported crude barite during the year 1990 increased from $40.27/t ($36.54 per st) in 1989 to $40.61/t ($36.84 per st). Nevada continued to be the leading producer of barite with 82% of the total, followed by Georgia and Missouri. It is estimated that 750/c, of the domestically mined barite was used as a weighting agent in drilling fluids. The remaining 25% was used in barium chemicals, glass or as a filler. Most of the production from Missouri, Georgia and Tennessee was used in the non-oilfield sector. Of the total barite used by grinding plants and chemical manufacturers, it is estimated that 90% was used in drilling fluids and 10% in the non-oilfield sector. This includes barium chemicals and fillers in paper, plastics, and glass. Tonnage consumed in the drilling fluids market increased due to the higher average rig count during 1990. The average number of rotary rigs operating, (1010), was 16.2% more than the 1989 average of 869 in the US.

Jan 1, 1991

By Paul Mitchell, Clive Potter, Miles Watkins

Meldon Quarry is a seemingly rare occurrence of acid rock drainage (ARD) in a quarrying operation.4 With surface waters discharging to a tributary of a salmon-bearing river, it is subject to stringent discharge conditions. The quarry predates effective environmental management, and preventative, control and treatment measures were not implemented until relatively recently. However, retrospectively implementing standard preventative approaches at the site is costly, technically difficult and of uncertain benefit. This paper overviews the recent site history and introduces data from a demonstration by KEECO (UK) Limited of its Silica Micro Encapsulation (SME) water treatment technology.

Jan 1, 2000

By F. F. Aplan

Prologue Antoine Marc Gaudin (Fig. 1) was truly a giant in the field of mineral processing, and his shadow is still cast long on our profession. "Tony," as his students affectionately called him (but never to his face), came to the United States in 1917 and enrolled at Columbia University where he studied under Professor Arthur F. Taggart. Later, as a lecturer, he wrote his classic comminution paper (Gaudin, 1926). This important work led to his appointment as an associate professor at The University of Utah, where he conducted highly original work on flotation fundamentals that is still widely quoted today (Gaudin et al., 1928-30). In 1929, he was appointed Research Professor of Ore Dressing at the Montana School of Mines in Butte. Shortly thereafter, he published his first book, Flotation (Gaudin, 1932). Because Gaudin could so quickly cut through the fog to get to the essence of a problem, this is still a valuable reference book. It is a valued part of my personal library, and I consult it frequently. Over the next decade, he conducted an outstanding graduate research program at Butte, but, more importantly, he honed his undergraduate lectures and produced the century's outstanding text in the field, Elements of Mineral Dressing (Gaudin, 1939). More than 50 years later, this terse book is still found to contain most of the elements of the discipline. Its sections on the

Jan 1, 1994

By E. W. Cokayne

GENERAL DESCRIPTION OF THE METHOD The original application of sublevel caving was in ground so weak that it would collapse even in small headings when the support was removed. Heavily tim¬bered drifts were driven across the ore body; the timber was removed at the end of the drift, and the ore caved and slushed out. When dilution became excessive the next set was removed and so on. This method gave high dilution and poor recovery and was slow, but it was the only way to mine this type of ore body at that time. In more recent times the method has been adapted to stronger ground which needs to be drilled and blasted, so it is not a caving method as far as the ore is con¬cerned. However, the method does rely on the walls to cave and so the name sublevel caving has been retained. The method as presently generally applied is shown in Figs. 1, 2, and 3. Sublevels are established at approximately 7.6 to 12.2-m (25 to 40-ft) vertical intervals. They are usually accessed from a ramp system. A haulage drift is driven down the strike of the ore body, but in the waste. Production drifts are turned off the haulage drift and driven across the ore body on about 10.7-m (35-ft) horizontal centers. This divides the ore body into a geometrical pattern. Slot raises are driven at the end of the drifts near the ore-waste contact and the slot is expanded to the shape of the fan drilling. Up holes are drilled to break towards the slot at burdens of 1.2 to 1.8 m (4 to 6 ft). They are drilled past the next sublevel to the production drift im¬mediately above. When a sufficient number of fans has been drilled, production can start by blasting one or two fans at a time towards the slot. Load-haul-dump (LHD) units are used to muck the ore, which rills out into the drift. At first, when only a small area is mined, the walls may not cave, and the operation will be similar to open stoping. Later, sloughing from the walls will fill any voids created, and the ore after blasting will be con¬tained by the caved waste and gravitate downwards as mucking proceeds. This process is repeated in each of the production drifts as the face is retreated towards the haulage drift. When the top level has been retreated back a safe dis

Jan 1, 1982

By B. Kolonja

This paper considers simulation of truck dispatching system designs using maximum expected production of the truck-shovel system as the measure of performance. Two methods are utilized, multiple comparisons with the best (MCB) and the combination of MCB and the variance reduction technique known as common random numbers (CRN). These two techniques are compared via simulation experiments. The results show that the combined procedure of MCB with CRN is the superior tool to reduce the total number of replications needed to ensure the specified probability of correct selection over the finite number of designing systems. In this case study, MCB with CRN reduces the variance by 29% and the number of required replications by 48%. Also, the MCB with CRN procedure narrowed the confidence interval by 18%.

Jan 1, 1994

By I. Dunlop, A. Goulsbra, R. Dunne

Mineral liberation or more aptly the particle size at which cost effect liberation is attained is an important mineral processing parameter. This implies that not all the mineral is liberated as further size reduction is not economically warranted. For ores of low grade minimising both the comminution capital and operating costs are crucial aspect to ensure project visibility. As a consequence the focus of attention for the most part is direct­ed to 'coarsening the grind" ahead of any downstream process­ing treatment. In most cases, recovery will be sacrificed to pro­vide for 'more tonnes' of capacity and in general this is eco­nomically justifiable. Preferential liberation and its measurements is an aspect of mineral processing that has created much attention and contro­versy. It is not the purpose here to discuss this matter in depth other than to state in broad terms that if an ore from the same source is subjected to comminution by two different methods, such that the product particle size distribution is similar, and subsequent downstream treatment demonstrates substantial dif­ferences in recovery, then there is reason to believe that prefer­ential liberation has occurred. Comminution by high pressure grinding rolls (HPGR) is a relatively new technology claimed to have two major advan­tages over conventional comminution. Firstly and more impor­tantly is the ability to improve comminution power efficiency. Power reductions of 10 to 40 percent being claimed. (Pagett et al (1995), Sargent (1995)). A secondary benefit claimed is that preferential liberation can occur. Generally, for HPGR there is a natural tendency of the product to have a skewed particle size distribution to the finer size. This in its own right could manifest itself in improved leaching and preconcentration performance. The question remains that if in using another comminution device, other than a HPGR, to produce a similar product size distribution as the HPGR, will there be any difference in downstream between the products from this and a HPGR.

Jan 1, 1996