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By G. E. McElroy

[The ventilation of development faces in mines for diluting gas or dust concentrations aid in hot mines for providing air-motion cooling affect, by fan-pipe units discharging high-velocity streams of air close to the face, is an important phase of mitre ventilation. The effectiveness of such units depends largely on the air-flow distribution between-the pipe discharge said the face, a subject on which little definite information is available. A study of the air, flow from grills into rooms3/ has provided sore basic data, but under conditions so different from mine fan-pipe installations in development ends that tae data to are of doubtful application to mine installa¬tions, owing to differences in air-flow conditions. The purposes of this report is to present and discuss the results of an initial series of tests of a general investigation designed to yield definite laws and design data for the discharge of fan-pine lines in nines. The s series was planned to yield preliminary data on the effects of velocity of discharge, size and shape of tripe, and adjacent calls on the air-flow distribution. Tents were made on 10-inch pine with seven different end conditions and one change of wall condition. Changes in size and shape of discharge wore made b y short transformation pieces directly at the discharge end, with the result that effects due to contraction and expansion of the flow, which proved to be of much greater importance than was expected, totally obscured any normal effects cue to size anti shape. The results of this series of tests, therefore, relate to 10-inch pipe with various discharge designs is and ago se reported.]

Jan 1, 1940

By T. D. Hackett

Multislice mining methods were analyzed by the U.S. Bureau of Mines to determine their application to western United States thick coal seams; ground control, geology, and costs were considered. Multislice mining is used in widely varying seam conditions worldwide, including flat seams too thick to mine in a single pass, pitching thick seams, and seams containing a rock parting. Longwall multislice methods predominate, but room-and-pillar variants also exist. The initial use of the method in western seams is planned at a deep Colorado mine where a rock parting will be used to separate two slices mined by longwall. Ground control and spontaneous combustion are major hazards associated with multislice mining. A well-consolidated upper slice gob can reduce ground control problems and provide a seal against spontaneous combustion. Geologic analysis indicates that the consolidation of the gob depends on the composition of the upper slice roof, the presence of water, and sufficient overburden pressure. A geologically competent intermediate rock parting can also reduce ground control problems and seal against spontaneous combustion. To compete in western coal markets, the cost of multislice mining must be within the range of normal longwall costs. Analysis indicates that multislice operating costs should be within this range, and that multislice mining costs decrease as panel width increases. Relatively wide (600 to 800 ft) panels also provide increased coal recovery.

Jan 1, 1990

By Parry. V. F., W. S. Landers

"INTRODUCTION Approximately 1,250,000 tons of 2-1/2-inch and 1-1/2-inch slack, representing over half of the output from 40 to 50 mines, is produced in the Denver region each year. Part of this slack is made by crushing lump, and some of it is rescreened to make pea and modified pea sizes measuring 1-1/2 inches by 2-1/2 inches and 3/4-inch by 1-1/2 inches, round-hole. Modified pea is popular as domestic stoker fuel. Approximately 900,000 tons of slack 0 by 2-1/2 inches, 0 by 1-1/ 2 inches, and 0 by 3/4-inch in size are consumed by industrial plants, the principal consumers being a large power plant and the beet-sugar industry. The power plant uses annually 250,000 to 275,000 tons of pulverized fuel and can pulverize slack of any size, while the sugar factories consume about the same quantity of coal in stokers. The sugar factories store about 110,000 tons of 2-1/2-inch slack under water from January to October, and burn the remainder of their consumption directly during the campaign season from October to December. For this purpose, sugar-factory power plants can use any size of slack, which is recrushed to pass a 3/4- or 1/2-inch screen before burning on chain-grate stokers. About one-third of the 2-1/ 2- inch slack produced in the field is used in smaller industrial plants that employ stokers.Certain factors affect the utilization of 2-1/2-inch slack in the Denver region. The increasing production of hydroelectric power has reduced the consumption of coal at power plants slightly. If more hydropower is generated, the trend of consumption of slack might be downward, unless industrial activity offsets this greater output. Rapid increase in number of domestic stokers during recent years has necessitated preparation of greater quantities of stoker coal, with the result that more lump is crushed, and preparation facilities are changed. At present about 19 percent of the coal produced is crushed to meet the constant demand for industrial fuel as well as the increasing but variable demand for the small domestic stoker sizes. The quantity crushed has increased 12 percent during the last 6 years. These factors are shifting constantly. The trend toward the use of clean and smaller sizes for domestic stokers gives a slack having a larger proportion of fines. In future, even greater quantities of small stoker coal probably will be prepared, and the resulting greater quantities of small slack will have to be used for industrial purposes."

Aug 1, 1942

By Yael Miron

The presence of pyrite (FeS2) in coal can cause or contribute to several problems for the coal mining industry. These problems, which include spontaneous combustion, roof falls, floor heave, and accidental explosions in coal surface mining when ammonium nitrate fuel oil (ANFO) explosives are used, result from pyrite oxidation. Pyrite oxidizes exothermically in the presence of air and moisture to form a large variety of products, including hydrated ferrous and ferric sulfates, and sulfuric acid. Some of the products are reactive chemicals and strong oxidants. The volume of many of these oxidation products exceeds the original volume of the pyrite; as a result, the adjacent coal disintegrates and its surface increases, rendering it more susceptible to oxidation. The heat from pyrite oxidation raises the temperature of the adjacent coal, accelerating the oxidation and self-heating rates of the coal. These combined chemical, physical, and thermal effects are the cause of the aforementioned problems. When ANFO is used in surface coal mines and contacts ferrous sulfate, a highly exothermic reaction ensiles. Additional hazards are fires or explosions caused by the frictional ignition of methane when the pyrite in the coal is struck by a cutting bit during mining.

Jan 1, 1994

By W. S. Landers

This bulletin is a detailed study of low-temperature, entrained-bed carbonization of a Texas lignite. The lignite studied was from the Sandow strip mine and is representative of the Rockdale formation of the Wilcox formational group. Carbonization was conducted in a continuous entrained-bed reactor at several temperatures in the 8801 to 1,52°C F range, and at air-coal ratios it the 0 to 10.30 scf/lb range (moisture- and ash-free basis). Carbonization rates ranged from 97.1 to 410.0 lb/hr (as-received basis), At the higher air-to-coal ratios employed, all or most of the carbonization heat was provided by internal combustion with air in the reactor. At the lower air-to-coal ratios, parts of the heat for carbonization was supplied externally. It was demonstrated that the entrained-bed carbonization of lignite is a complex reaction and that several variables, of which carbonization temperature, air-to-lignite ratio, and the average size of lignite are important, act together to influence both the carbonization yields and the properties of the resultant products, Process variables established by pant tests were used to design the industrial scale carbonizer operated at Rockdale, Texas, by the Texas Power & Light Company as agents for the Aluminum Company of America. Properties of the carbonization product obtained from the industrial scale reactor were essentially the same as those obtained from the pilot plant reactor operated under the same conditions.

Jan 1, 1968

By D. W. Frommer

Composite samples of nonmagnetic taconite from the western Mesabi range were evaluated by reductive roasting, fine grinding, and magnetic separation to determine potential sources of concentratable material. Although large tonnages of nonmagnetic taconite are known to occur in the western Mesabi district, these materials are not as yet a commercial source of iron ore. The technique employed permits the evaluation of individual composites and blocks of composites in terms of responsiveness to a process of potential commercial significance. The 159 composites, from open-pit mines located between Grand Rapids and Chisholm, Minn., were evaluated in the following sequence: 1. Minus 8-mesh material was roasted at 500° C. in hydrogen. 2. The roasted are was ground to one or more sizes in the minus 100-to minus 400-mesh range. 3. The roasted ground ore was magnetically separated in a Davis tube. 4. Composites were classified according to degree of grinding required to produce minimal concentrates. (Minimal concentrates are herein defined as those containing less than 10 percent silica, and responsive composites as those yielding minimal concentrates.)

Jan 1, 1962

By James H. Aase

[This study provides data on the physical and hydrological makeup of the ,t hakes waterway system and forecasts quantities, traffic patterns, and ping cost of prospective bulk mineral commerce projected to be transported it. Factors affecting the shipping cost of iron ore, bituminous coal, imestone were quantified and integrated into a computer program that can d to estimate costs under varying sets of conditions. Combined ship of iron ore, bituminous coal, and limestone in 1995 were estimated at million tons. The cost of operating the U.S. vessel fleet for trans-ng an indicated 80 percent of this traffic tonnage was projected to be $163. 5 million.]

Jan 1, 1970

By Albert L. Toenges

The Grundy coal field is in process of development, and this circular was written to describe the mining methods and practices in use in the mines now being worked in this field. In lieu of man-hour labor data for individual mines a consolidated sheet of mine costs, which includes expenses for labor, material, and power, is given for all mines. The costs are for a working day only, based on average daily production. Because the demand for coal is seasonal, the costs for idle days, which vary at each mine, have not been estimated. Approximate reserves of coal seams have been estimated from data and maps taken from Bulletin XVIII of the Virginia Geological Survey4/.

Jan 1, 1936

By T. A. Henrie

The Federal Bureau of Mines has investigated methods of sodium reduction of titanium chlorides to produce high purity titanium metal (14).4/ This investigation was made to obtain a better understanding of the reactions involved in sodium reduction of titanium chlorides and was part of the Bureau's activities toward improving the technology of titanium. Theoretical and experimental evidence show that sodium reduction of titanium tetrachloride occurs by stepwise reactions. The first stage reduction between sodium vapor and vapors of titanium chlorides produces titanium di-and trichlorides which subsequently condense with sodium chloride to form a salt mixture. The second stage reduction takes place in the condensed salt mixture between sodium and titanium subchlorides. Final reduction is a heterogeneous reaction between two separate phases, the a phase which consisted of sodium dissolved in sodium chloride and the ß phase titanium subchlorides dissolved in sodium chloride. The mechanism of the heterogeneous reaction between these phases is electrochemical in nature. The model proposed is a galvanic reaction at the interfacial region.

Jan 1, 1960

By Sidney Katell

The present report, a continuation of the series of Bibliography of Investment and Operating Costs for Chemical and Petroleum Plants, is concerned with articles published from January 1958 through December 1958. The periods covered in previous reports are as follows: January 1930 - August 1948 I. C. 7516 September 1948 - June 1952 I. C. 7705 July 1952 - June 1954 1. C. 7751 July 1954 - December 1956 I. C. 7847 January 1957 - December 1957 I. C. The following sources were used to obtain the references to and the abstracts of the published articles included in this report: 1. Bureau of Mines Information Circulars. 2. Bureau of Mines Reports of Investigations. 3. Chemical Engineering. 4. Chemical Engineering Progress. 5. Coal Age. 6. Coal Utilization. 7. Cost Engineering. 8. Industrial and Engineering Chemistry. 9. Nucleonics. 10. Oil and Gas Journal. 11. Petroleum Engineering. 12. Petroleum Refiner. 13. World Oil.

Jan 1, 1959

By Raymond B. Ladoo

"Domestic Situation:The greatly increased use of lithopone as a base for paints, particularly for interior use, has timulated the demand for barytes to such a degree that the supply cannot keep pace with the demand. Lithopone is an artificially prepared compound composed of about 70 per cent barium sulphate and 30 per cent zinc sulphide, precipitated together. Its most important use is in paint, but it is also used in oilcloth, linoleum, rubber goods, shade cloth, etc.Prior to the war large quantities of barytes were imported from Germany, but during the war imports were negligible, domestic production increased very greatly and is still increasing. Ground barytes as used in paints/ formerly regarded as an adulterant, but now it is generally recognized as a valuable paint constituent. Mile domestic sources have expanded rapidly they have not overtaken the demand and there is need for still greater expansion. Stocks are low, little is being sold on the open market, and prices are high. Since barytes is a gangue mineral associated with metallic ores now being mined in the west, it is suggested that more attention be given to its recovery as a by-product.The following tables compiled from reports of the U.S. Geological Survey and the Bureau of Foreign and Domestic Commerce, indicate the growth of domestic consumption."

Jan 1, 1920

By William C. Cooley

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Jan 1, 1975

By Berk. A. A.

"INTRODUCTION Corrosion of sections of piping used in steam-heating systems is frequently regarded as unavoidable, and periodic replacement is provided. Surfaces exposed to newly condensed steam appear to be especially vulnerable to attack. As an added nuisance, solid products of the corrosion tend to accumulate, plugging return lines.The trouble is ascribed in the main to carbon dioxide and oxygen 3/ 4 / 5/ 6/ dissolved in the condensate. When oxygen is the principal factor, the corrosion usually is characterized by pitting. Carbon dioxide tend3 to cause an acidic condensate which dissolves the metal more uniformly and produces the familiar failure at threaded areas where the piping is relatively thin, and where high stress may tend to acceletate the attack. Carbon dioxide enters the system with the feedwater, generally in a combined form such as carbonates and bicarbonates. Oxygen enters both with the raw feedwater-and as air leaking into lines under partial vacuum. The larger central-heating plants have sought to reduce corrosion by eliminating these gases as much as possible. A smaller plant ordinarily lacks the equipment and technical supervision required for this purpose."

Jun 1, 1944

By W. J. Kroll

This investigation was undertaken with the idea of studying a number of unconventional methods for making chromium to determine whether production cost could be lowered and to discuss some of the more recently described processes. These comprise carbon reduction of the oxide in vacuum, nitride dissociation, fusion electrolysis of the chloride, amalgam method, iodide dissociation, calcium reduction of the oxide, hydrogen reduction of the chloride, and reduction of this compound with zinc and with magnesium. Preference is given this latter method, which is shown in a flow sheet. Special attention is given purification of the chloride and separation of the vacuum at about 900° C. A reduction method for the elimination of traces of oxide contained in pure chromium by pure hydrogen obtained from the dissociation of zirconium hydride is described. The various methods are compared in a table in the appendix. Aluminothermic and silicothermic methods for the reduction of chromium oxide and the aqueous electrolysis have been disregarded in this investigation.

Jan 1, 1950

By A. W. Deurbrouck

Five preparation plants employing concentrating tables for washing 3/8- inch to 0 raw coal were tested. Two of the plants were washing Pittsburgh-bed coal, two were washing Pocahontas-bed coal, and one was washing Elkhorn-bed coal. Samples of the feed to and products from the tables were collected over the normal operating shift. These samples were analyzed, and complete performance criteria were determined. The results of this study show that the concentrating table is an effective fine-coal cleaner even when operating at 40 percent over the recommended 10 tons per hour feed rate. Recovery efficiencies for the 3/8-inch to 200- mesh size fraction ranged from 97.3 to 99.3 percent; maximum yield errors and ash errors were 2.4 and 1.0 percent, respectively; probable errors ranged from 0.074 to 0.115 specific gravity units and error areas from 52 to 73 square centimeters. The amount of minus 200-mesh material in the water used for feed water and dressing water to the table had no significant effect on the sharpness of the separation achieved but did have an effect on the ash content of the clean- coal product. In the one plant studied, the substitution of fresh water for plant circulating water reduced the ash content of the clean coal by about 6 percentage points.

Jan 1, 1963

By C. H. Fisher

Coal carbonization, the basis of a major industry, consists in heating coal in the absence of air at various temperatures (ranging from 500° to 1,000° C.) that are selected according to the kind of products desired. During this treatment, the complex organic substances that comprise the major part of the coal are converted into several useful products that are quite different from the original material. The principal products of coal carbonization or distillation are coke and gas. These products, as well as others of which lower yields are obtained (light oil, tar, and ammonia), occupy an important place in present-day commerce and civilization. This paper is concerned with the composition of the tar and light oil, which, as complex mixtures of organic compounds, are the source of many important dyes, inter-mediates, medicinals, resins, etc. The volatile products obtained when bituminous coals are destructively distilled or carbonized are tar, aqueous liquor, and gas. These products vary in composition and properties, depending on the nature of the coal and the temperature and conditions of carbonization. The tar is a dark, rather thick and viscous liquid at ordinary temperatures, becoming semisolid when cooled to the freezing point of water. The aqueous liquor (chiefly water) contains several inorganic substances and certain organic compounds, which, because of their solubility characteristics, have been extracted from the tar. The carbonization gases consist chiefly of carbon dioxide, carbon monoxide, hydrogen, hydrogen sulphide, ammonia, methane, ethane, ethylene, and several hydrocarbons of higher molecular weight. The hydrocarbons of higher molecular weight (benzene, toluene, xylene, etc.) may be re-moved as liquids from the gas by suitable means. This liquid and the first fractions obtained on distilling the tar are known as light oil.

Jan 1, 1938

By Oliver Bowles

Wire saws have been used for many years in European travertine, marble, and slate quarries. This method of sawing found very limited use in America until 1927 when it was accepted as standard equipment in elate quarries in Pennsylvania where it has been remarkably successful. Details of its operation in slate have been published in a recent bureau report.3 The very limited extent to which the wire saw has been employed in limestone and marble quarries in the United States and the seeming lack of interest even in experimental work to determine its advantages are difficult to explain in vied of its wide use in cutting similar rocks in Europe and its unquestionable advantages in sewing slate in America. In order to encourage improvement in quarry practice the United States Bureau of Mines has endeavored to obtain information as to the extent to which wire saws are used in Europe together with data on the rate and cost of sawing. The information at hand is by no means complete either in territory covered or in details of operation; it nevertheless brings out certain significant features that may be of interest and advantage to quarrymen in the United States.

Jan 1, 1931

By W. W. Odell

The results of the 1921 cooperative experiments conducted by the U. S. Bureau of Mines and the University of North Dakota at the University mining substation plent at Hebron , North Dakota , pointed clearly to certain definite dep ficiencies in the schemes hitherto developed for benefiting and utilizing lignite . First The apparatus used in the carbonizing process or used to produce carbonized lignite suitable for briquetting is too costly , that is , the cost per ton day of residue made is too high . Second - The depreciation of the carbonizing appara tus is too high . Third The carbonizing apparatus can not be operated intermittently without seriously damaging it and impairing its efficiency of performance . Fourth Too little attention has been given to the possibility of using at least a certain percentage of the carbonized lignite directly in suitable stoves and furnaces without briquetting or other treatment . Accordingly , consideration was given to the design of an oven that could be built at a mine without the importation of highly skilled and specially trained construction men , erected at a low first cost , readily kept in a state of repair , operated at a rela tively high capacity and put into operation or shut down at will without seriously damaging the brickwork . The need of such an oven was appreciated also by the University of North Dakota and a cooperative agreement was made to build and operate such an oven during the summer of 1921.

Feb 1, 1923

By J. A. Taylor, H. F. Yancey

"INTRODUCTION Froth flotation as applied to coal is a process for separating desirable carbonaceous material from undesirable inorganic matter. In general, the feed must be finer than one eighth inch in size. The principal use of the process in the preparation of coal appears to be in the treatment of the fine sizes produced by breakage during mining and preparation.The Bureau of Vines in Information Circular 6714 has published general information on coal flotation, summarized investigative studies of the process, and described operating plants throughout the world with their tonnage, reagent consumption and operating costs.4ACKNOWLEDGMENTSThe present study of means for depressing pyrite and reducing ash ty froth flotation was conducted at the Northwest Experiment Station of the United States Bureau of Wines in cooperation with the College of vines. University of Washington, under the general direction of A. C. Fieldner, chief engineer, Experiment Stations Division, Bureau of Wines. Grateful acknowledgment is made for suggestions and criticisms received from W. H. Coghill, supervising engineer, U.S. Bureau of Mines Mississippi Valley Experiment Station, Rolla, Mo.; J. B. Morrow, and R. E. Zimmerman, of the Pittsburgh Coal Co.; and Dean Milnor Roberts and Prof. Joseph Daniels, of the College of Mines, University of Washington.FLOTATION AND DEPRESSIONA substance will tend to float if its surface attracts a gas film more strongly than it does a liquid film when both air and liquid are competing for this attraction. On the other hand, a substance will not float if its surface attracts a liquid film more strongly than it does a gas film. All theories of depression depend upon this fact. A wetted particle of floatable size most likely will be found in the tailings after the flotation process has been completed.The crux of flotation is the selective wetting of the undesirable material that tends to float. Two general methods 5, 6, 7 of depression are in use: One combines a chemical substance with the surface to form a wettable compound, and the other employs some colloidal or ionic substance which the surface selectively adsorbs, thereby forming a wettable surface."

Jan 1, 1935

By Fred D. DeVaney

The Mesabi iron district of Minnesota has a potential production of over 50 million tons of iron ore annually. The large shipments of ore each year are gradually depleting the reserves, and if the present rate of production is to be maintained there must be a growth in the present available ore supply. Growth is a natural course. The growth of a city may be affected by the addition of city blocks or by the improvement of utilities necessary for its betterment. These may go on in the order named or concurrently. The city-block type of growth of the Mesabi has been tremendous, and the "betterment" type has followed in due course. Probably the former has reached its limit, and if so, more time will be allotted to the latter. It is not the intent of this paper to present either a eulogy of the wonderful mining methods or a history of the milling, but it is pertinent to say that if the lean-ore area continues to produce, the continuance will be more the result of further improvement of milling methods now well under way than of extension, of boundaries by the city block plan of growth. In an examination of the western end of the Mesabi district one finds sludge basins containing millions of tens of millable ore rejected by washing plants which were built for economy in operating cost and with little thought of conservation, and rich tailings piles of jigging plant rejects. In addition, there is an appreciable tonnage of bowl rake products so low-grade that it requires mixing with the best ore of the district to make it merchantable.

Jan 1, 1932