Search Documents

By Jr. Kauffman

The data contained in this report were obtained incidental to the Bureau of Mine's investigation of the lime-soda sinter process as applied to the recovery of alumina from siliceous bauxite, kaolin, and other high aluminous materials. The Bureau of Mines was charged by Congress to investigate processes for the production of aluminum from domestic low-grade ores. The Eastern Experiment Station at College Park, Md., conducted laboratory and pilot-plant investigations of the recover-y of alumina by the lime-soda sinter process. Reports by the College Park staff covering the recovery of alumina from these sources have been published. The lime-soda sinter process involves the sintering of the finely ground siliceous bauxite or clay with limestone and soda ash in a rotary kiln. During the sintering the alumina supposedly reacts with the soda ash to form soluble sodium aluminate and the silica combines with the lime to form the insoluble orthosilicate. In the early stages of the investigation it was considered desirable to know the temperatures at which the phase changes occurred during the sintering operation. The total time involved in the passage of any given portion of the charge through the kiln was 28 minutes. The exposure time of the charge to temperatures above 600° C. (decomposition temperature of kaolinite) was, roughly, half the total. The exposure to the full temperature of the kiln, 1,100° C was only 3 minutes. (Subsequently, the maximum kiln temperature and retention time were increased.)

Jan 1, 1949

By John Nagy

Dust explosion data obtained in laboratory tests by the Bureau of Mines are presented for 181 miscellaneous materials that present an explosion hazard. Data are given also for 50 dusts that present primarily a fire hazard and for 88 dusts that did not present an explosion hazard.

Jan 1, 1968

By A. W. Fahrenwald

As an aid to studies of grinding, a batch laboratory classifier and elutriator has been developed at the U. S. Bureau of Mines Metallurgical Field Office at Moscow, Idaho, in cooperation with the University of Idaho. It is designed for use in conjunction with other batch laboratory apparatus, such as ball mills and flotation machines. It is shown in Figure 1. Description and Operation of Batch Laboratory Classifier The classifying column is a cylinder 4 feet 2 inches long, of 5 3/4-inch inside diameter, and terminates at its top in a cone or funnel 18 inches in diameter at the overflow elevation. The pressure chamber is of the same diameter as the classifying column, and has a conical bottom; it is provided with two openings, one in the cylindrical portion through which water is admitted, and the other, a small drain hole, in the apex of the conical bottom. The two compartments are bolted together and communicate with each other through the medium of a constriction plate provided with 3/16-inch holes spaced 1/2 inch apart. Constriction plates having any other percentage of opening may be substituted as the needs demand water is admitted to the compartment below the constriction plate at constant pressure. The volume of eater admitted is controlled with a valve. It should be mentioned that the classifying column at the bottom, just above the constriction plate, is glass.

Jan 1, 1929

By Mark Sheppard

This p aver is the second of a series recording the results of tests made at various quarries throughout the United States to determine, (1) the relation between the size gradation of feed to, and product from, primary crushers; (2) the particle shape of crushed product; (3) the differences in gradation and particle shape produced by different types of primary crushers; and (4) the differences in gradation and particle shape caused by crushing different kinds of stone. Primary crushing has received comparatively little attention in the technical literature in spite of the fact that the design of the whole crushing plant should be correlated to the performance of the primary crusher.

Jan 1, 1938

By A. C. Richardson, G. D. Coe, B. M. Bird

"The Hull mine of the De'Bardeleben Coal Corporation is located in the Warrior field, in Walker County, Ala., about 25 miles northwest of Birmingham. The Mary Lee bed at this point is coking coal and has been used in the manufacture of by-product coke, but at present it is sold exclusively as a domestic and locomotive fuel.The data in this paper, which is the third in a series on the washability of Alabama coals,5 have been obtained in connection with an exhaustive study of coal preparation in Alabama now being conducted by the U. S. Bureau of Mines and the University of Alabama with the cooperation of the different coal operators. The paper contains screen-sizing and float-and.-sink tests of a representative sample of run-of-mine coal, and flakiness tests and crushing tests of certain sizes.In addition, complete analyses of the ¾-inch to 3/16-inch size, raw coal, together with ash fusibility tests of the float-and-sink fractions have been made; those results are given in Tables 1 and 2. Since they indicate that the pr ration problem, like that at Lewisburg, Ala., is one of ash reduction, the further tests and the discussion have been restricted to that subject."

Apr 1, 1931

By Robert L. Rough

This report presents the results of an investigation by Federal Bureau of Mines engineers of water-injection projects in the northwestern Pennsylvania and southwestern New York area, where oil-producing wells have been converted from pumping to flowing. Data from 24 leases converted to flowing were collected and examined. Only 10 leases had information of significant scope for inclusion in the final analysis. The projects were classified in one of two categories. Group I consisted of leases operated to permit an evaluation of operational changes in terms of existing pressure differentials between injection and producing wells. Group II included remaining properties, for which enough information was available to justify an economic analysis but which did not have sufficient production data to support an engineering study because of radical changes in operational techniques. Variations in production and costs resulting from conversion to flowing were examined for production methods, well-spacing and completion techniques, and reservoir characteristics. Where water-injection rates were constant, oil production usually decreased rapidly at the time of conversion; production then increased slightly for 6 to 8 months before resuming a normal decline rate considerably below the estimated pumping rate. The abrupt decrease in production after conversion is indicative of lower pressure differentials between injection and producing wells, caused by the increased hydrostatic head in the producing wells.

Jan 1, 1960

By Edward F. Fries

The U.S. Bureau of Mines is conducting research that will lead to computer-assisted mining equipment. This research will facilitate improvements in safety by relocating workers from dangerous areas and will increase production by providing more accurate control with less downtime of equipment. A Bureau-developed microcomputer network enhances this research by permitting a group of diverse computers to interact with a mining machine as well as with each other over a common data link. The network is composed of specially integrated off-the-shelf hardware and industry-standard operating system and programming languages. Using the network, researchers can conduct various experiments with the mining machine using a diverse group of sensors, computers, and micro controllers. This report gives a brief background on the Bureau's work in computer-assisted mining, followed by discussions on the network hardware and architecture and the network packets, and an analysis of network operation.

Jan 1, 1992

By B. W. Gandrud, G. D. Coe

"INTRODUCTION The Southern Experiment Station of the U.S. Bureau of Mines, cooperating with the University of Alabama and Alabama coal producers, has made a series of investigations of the washability of coal from commercially important bens of Alabama. The results of 13 investigations pertaining to the Mary Lee, Clark, Black Creek, Jefferson, Pratt, Corona, Carter Brookwood, Blue Creek, Thompson, and Woodstock beds have been published. 4/ This report, the fourteenth of the series, deals with run-of-mine coal from the Henry Ellen bed at the Acmar No. 5 mine of the Alabama Fuel & Iron Co.The Acmar mine is 1/2 mile west of Acmar, Saint Clair County, in the northern part of the Cahaba field. Present production at the mine is about 800 tons per day, all of which, accept the lump coal, is treated in jigs. The washability data were obtained by means of screen-sizing and float-and-sink tests. There are included, also, tests showing the extent of liberation of impurities by recrushing the coarser sizes of coal from the top bench and tests showing the flakiness in selected sizes.SAMPLING AT THE MINEThe Henry Ellen bed at Acmar consists of two benches separated by a shale parting. At the point of sampling the top bench was 6 feet 3 inches thick and contained a 1-inch and a 1 1/2-inch band of bone. The bottom bench was 5 feet thick and was separated from the top bench by 20 inches of shale. In taking the samples for the washability study the working face was squared up, and a representative 2-ton section was out from each bench. The shale parting was discarded, according to usual mining practice."

Nov 1, 1936

Only limited work has been reported in the literature about the use of latex in soil. Unisol 91 2,3 (a 9:l oil-latex emulsion made b International Synthetic Rubber Company) and Phil1ips Petroset4 geotechnic emulsions are surface soil stabilizers which penetrate a maximum of two inches, but do not reduce permeability. Diamond Alkali 5 found that styrene-butadiene rubber latex as a one percent latex-soil mixture reduced permeability to 0.7 from 21 feet per year under a head of twenty feet of brine. We have found no literature reference for use of latex as sealant at depth in the soil, although asphalt has been applied at depth using civil engineering methods6,7. Most of the materials investigated as soil sealants in the present work were latexes, although some studies were also conducted with a variety of inorganic and organic chemicals. Of the latexes tested, most were rubber but a few were plastic, e.g. polyvinyl chloride. Sealants examined in this investigation are listed individually in Table I with supplier, code number, and other pertinent information. The materials consisted of the following general classes with additional details as indicated: 1.Anionic latexes: a. styrene-butadiene copolymers and terpolymers (SBR) b. butadiene-acrylonitrile copolymer (Paracrils®) c. polyvinyl chloride homopolymers and copolymers (WC) d. ethylene-propylene terpolymer e. vinyl acetate homopolymers and copolymers (VA) f. acrylics (acrylate copolymers) g. 2-chlorobutadiene homopolymer (chloroprene) (prepared specially as cationic material coagulated by soil). 2. Water Soluble polymers: a. polyvinyl ether b. methylcellulose c. polyethyleneimines d. polyacrylic acid homopolymer e. copolymers and terpolymers with acrylic acid types (water soluble as sodium or ammonium salts) f. alginates g. monomers (for polymerization in soil, e.g. acrylamide)

Jan 1, 1972

By Jack I. Paige

The devitrification of lithium silicate glasses was studied to determine the effect of annealing temperature, composition, and additives on nucleation and crystallization. High-purity glasses, prepared from reagent-grade chemicals, had close to optical quality when prepared by a vacuum induction melting method developed during this research, The progress of devitrification was traced by differential thermal analysis and thermal expansion for those lithium metasilicate-silica compositions containing 80 to 90 percent silica. Microscopic studies of glasses partially devitrified at various temperatures and annealing times indicated that the primary initial mode of formation of individual crystals ,vas from densely crystalline zones that filled in as crystallization advanced Of the additives tested, calcium, potassium, and sodium helped promote devitrification with the least cracking or surface deformation. Tin oxide was most effective in reducing volume contrast ion during devitrification, but was not ClS effective in preventing cracking as calcium or potassium additions.

Jan 1, 1965

By Uldis Jansons

This report evaluates the economic Mining feasibility of four selected mineral deposit types that can be anticipated to be found in (d)(2) lands in the western Brooks Range, Alaska. The major assumption made for this study is the availability of a rail system for transporting equipment and concentrates for the base metal mines. Commodity prices used are those in existence in July 1976. Mine models were established based on known deposits and then evaluated. A lead-zinc-silver-barite deposit for which grades were available but ore reserves were assumed would require approximately 25% higher ore grades or higher metal prices to yield a 15% discounted cash-flow rate of return an the investment if mined at a rate of 10,000 tons per day open pit methods. Large copper-zinc mineral deposits could be mined economically at rates either of 5,000 tons per day underground or 10,000 tons per day by open pit methods. A high-grade copper deposit require a copper price of over one dollar ryes pound to yield an economic profit to be mined at 2,000 tons per day by underground methods. A small high-grade gold underground mine would require a gold price of about $295 per ounce to yield a 20% discounted cash-flow rate of return on investment if all new mine equipment were used and if existing labor rates were paid: Enterprising mining groups operating as partnerships might be able to operate this mine profitably at a gold price of about $152 per ounce, perhaps slightly less.

Jan 1, 2012

By Carl Belser

This report is the first of a series dealing with the oil-shale reserves of the Green River formation in the Rocky Mountain Region. The known oil-shale reserves of northwestern Colorado at present considered to have economic value apparently are confined to the Piceanco Creek basin between the Colorado and White Rivers. The number of sampled sections is small, but there can be little doubt that the Piceance Creek basin is a potential source of enormous quantities of liquid fuels and the related byproducts obtained from oil-shale processing. The partly blocked and inferred oil-shale reserves of 25-gallon-a-ton shale are estimated to have an oil yield of 125 billion barrels and the reserves of 15-gallon-a-ton shale are estimated to have an oil yield of 494 billion barrels. The number of available sampled sections is inadequate for making firm estimates.

Jan 1, 1951

By J. H. Field

Results of studies by the Federal Bureau of Mines on a pilot-plant scale for removing hydrogen sulfide and carbonyl sulfide from gas mixtures by the hot carbonate system are given in this publication. Gases containing up to 10 pet. hydrogen sulfide and 48 grains carbonyl sulfide per 100 cu.ft. were treated. In most tests carbon dioxide also was present and was removed simultaneously with the sulfur compounds. Because the rate of absorption of hydrogen sulfide is much more rapid than that of carbon dioxide over a wide temperature range, selective removal of hydrogen sulfide occurred in the bottom section of the absorber near the point of gas entry. Hydrogen sulfide was removed to pipeline specifications with carbonate solutions by using split-stream flows in the absorber and regenerator.

Jan 1, 1960

By E. S. Shedd

The Bureau of Mines investigated electrowinning and tapping lanthanum metal from lanthanum oxide in a fluoride bath. The electrolyte was composed of LaF3, BaF2, and LiF. Metal containing 0.2 percent impurities was produced at a rate of over 2 pounds per hour. Principal impurities were carbon, aluminum, and silicon. Low-carbon metal was produced by continually discharging the carbon oxide gases and maintaining 0.1-atmosphere pressure. Anode reactions and cell design were found to be important factors in cell operation. Both frozen electrolyte skulls and tungsten metal crucibles proved satisfactory for collecting the metal and did not react with the molten lanthanum.

Jan 1, 1966

By E. O. Wagner, Manuel Gomez, W. S. Landers

The Bureau of Mines studied coking rates of a special Columbia - Geneva six - coal blend to establish the effect of the coking rate on coke properties . The tests were conducted in a 500 - lb , 14 - in experimental slot oven at essentially constant conditions of blend composition , size distribution , surface moisture content , and bulk density . The coking rate was varied as a function of oven flue temperature . Coking rates within the range of 0.56 to 1.35 in/hr were achieved . Increase in the coking rate decreased the size of the coke . The stability factor of the coke showed no significant change with coking rate until coking rates greater than 1.0 in/hr were reached , after which a decrease in the stability factor was observed . The apparent specific gravity increased to a maximum value at coking rates approaching 1.1 in/hr and decreased sharply with further increase in the coking rate . Coke parameters correlated well with the coking rate .

Jan 1, 1963

By C. R. Nisewanger, F. W. Brown

"The velocity of detonation of an explosive is one of its most important properties, because its performance depends markedly on the rate at which it releases its energy. Fortunately, the velocity of detonation is one of the few properties of an explosive that can be measured precisely. However, the velocity of detonation of an explosive may depend on several factors other than its chemical composition, such as density, physical state, degree of confinement, nature of confinement, and magnitude of initiating impulse. Presumably for an explosive of fixed chemical and physical properties there are certain limiting conditions of confinement and initiation under which the explosive will detonate at a maximum constant and uniform velocity. This velocity is its ""ideal"" velocity of detonation. It is obvious, however, that in order to evaluate performance properties of an explosive in all of its applications it may be necessary to measure its velocity of detonation under a number of conditions in which the velocity of detonation is far from the maximum ""ideal"" velocity.. Under certain-conditions the velocity of detonation may even,be,different at different points in the explosive.It is .relatively simple to determine the velocity of detonation of an explosive under a. standard set of conditions if one is free to use large quantities of the explosive and to form it into a convenient shape. Under these circumstances; one can use a thin column of explosive a meter or more in length. The time required for an explosion to travel the length of the column will not be less,of the order a few ten-thousandths of a second and can be readily and accurately measured .by means of the standard spark chronograph or by photographing the explosion with a rotating-drum camera. However in many applications the explosive charge may be of relatively small dimensions arid may not be in a form convenient for making velocity measurements and often may be enclosed in a case or other confining medium. It may be necessary to determine the velocity of detonation over distances of the order of a few centimeters, in which case the time intervals to be measured will be extremely small. For example, the time required for an explosion to traverse 1 centimeter of tetryl is of the order of 1.5 microseconds.Since no satisfactory method of determining time intervals of the order of magnitude of a few microseconds within an explosive charge was available,, at least not for all conditions that might be encountered in practice, it was necessary to develop a special electronic chronoscope which is capable of measuring time intervals as small as a microsecond with a fair degree of accuracy. This report describes the chronoscope and its application to measurements of velocities of detonation in explosives."

Mar 1, 1946

By Ernest W. Johnson

Diamond, drilling of some blast holes in stoning operations is practised in at least two iron mines in the Lake Superior district - the Soudan mine of the Oliver Iron Mining Co., on the Vermilion range at Soudan, Minn., and the Anvil-Palms mine, operated by Pickands, Bather & Co., on the Gogebic range at Bessemer, Mich. Diamond drilling, at the Soudan nine has partly replaced percussion drilling because of the extreme hardness of the ore and of the lean formation. According to Wolff,4/ the jasper or lean formation in this mine is the hardest rock regularly drilled in any commercial operation.

Jan 1, 1945

By Arthur L. Murray

"Oil-shale camps are peculiarly favored, in that before they are established it can be ascertained with a,of certainty, that the life of the project is not limited. Unlike camps at metal mines, where the metal content of a given area is frequently an unknown quantity until after years of development, oil-shale camps should, from the outset, be planned and built as permanent types of camps. Where this procedure is followed camps will be established which better serve the needs of the industry and the cost of their general care and upkeep will be less.Selection of camp or townsite.The site of the camp or town, whether on company property or not, should be selected with care. It should be separate if possible from the location of the plants of the company so as to be free from noise and fumes and so as to provide a change of environment for employees in going from their work to their homes.The principal features governing the site to be selected are as follows:Drainage. The general contour of the surrounding country should be such that drainage is away from the site. The camp or town should, if practical, be situated on higher ground than that in its immediate vicinity.Soil. The nature of the soil on which the camp or town is located may bear a decided relation to health. A porous, well under drained top soil of at least four feet in depth insures dryness and facilities the placing of foundations and the laying of water mains and sewer pipes. Such a soil also is an advantage in growing trees, shrubs and grass plots, which are a decided adjunct to making the community attractive."

Jun 1, 1921

By A. D. Garman

This digest of Brazilian mining law is based upon Decree 4265 of January 15 , 1921 , and its regulation , Decree 15,211 of December 28 , 1921. Unless otherwise stated , the references are to the latter exclusively , since it includes practically everything contained in the law itself . It should be borne in mind that these regulations do not necessarily apply to mines other than those on private and national land . Each State of the Union is free , in respect to State land , to regulate or interpret the national mining law , which is very general in its terms , as it sees fit . Whether such local regulations are anywhere in force with respect to the law of 1921 the bureau has not been informed . Article 64 of the Constitution indicates that only such portions of territory as are required for the defense of the frontiers , for fortifications , military constructions , and federal railways belong to the Union . Lessees of such lands , unless in debt to the Treasury , have preferential prospecting rights for one year ( art . 28 ) . This carries with it the right to work any mines discovered (Law , art . 12 ) .

Jul 1, 1930

By John B. Bennett

In this report estimates are presented of the impact of the passage of five recently proposed "acid rain" bills on electric utility costs for coal-burning utilities servicing the domestic aluminum smelting industry, and on the costs of production for affected aluminum smelters. As aluminum smelting is an energy-intensive industry, domestic increases in electricity prices could affect the industry's competitiveness. Energy costs in U.S. aluminum smelting are compared to aluminum smelting energy costs in the rest-of-the-world. Governmental policies affecting these energy costs are discussed.

Jan 1, 1988