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By P. R. Tisot

This report discusses the waxes made from shale-oil wax distillate, a specific fraction obtained- from crude shale oil. The plate wax crystals Were exceptionally well suited to solvent extraction. Methyl ethyl ketone was the preferred dewaxing solvent.' The quantity of wax recovered at 32°F was 18.8 percent of the wax distillate, or 6.6 percent of the crude shale oil. The laboratory batch processes used for separating the wax from the distillate and subsequent refining were based .upon conventional petroleum methods. Three grades of shale-oil waxes were made and designated as crude, semirefined, and fully refined. The solvent-extracted wax consisted mainly of paraffin and olefin hydrocarbons. The physical Properties of the fully refined shale-oil wax were the same as er corresponded closely to those of Billy refined petroleum paraffin wax. Inasmuch as the crude and semirefined shale-oil waxes can be separated and refined in much the same manner as petroleum waxes, the cest of manufacture should be about equal to that for making petroleum paraffin wax. The cast of making a fully refined shale oil wax will be somewhat greater than for making .a fully refined petroleum paraffin, due to the loss of the oleofinic material from the shale-oil wax by acid treatment and the increased quantity of acid required for its removal. An analytical method for the determination of wax in shale-oil dietillates, a list of the physical properties that wore determined for the waxes, and the method for testing those properties are given in the appendix to this report

Jan 1, 1950

By G. E. Johnson

A bench-scale study was made of removing hydrogen sulfide from synthesis gas at elevated pressure by iron oxide impregnated on wood chips. The gas contained 0.02 to 0.06 percent oxygen. The removal of hydrogen sulfide by iron oxide impregnated on wood chips is more efficient at elevated pressure. At constant space velocity, longer periods of operation at 400 p.s.i.g. are possible before the exit gas reaches a given maximum concentration of hydrogen sulfide, compared with 200 p.s.i.g. or atmospheric pressure. In tests at room temperature, 60° C., and 100° C., the most effective removal of hydrogen sulfide was obtained at room temperature and the least effective at 100° C. Dry impregnated wood chips removed only about half as much hydrogen sulfide as chips wetted to a water content of 50 percent.

Jan 1, 1962

By N. A. Gokcen

This Bureau of Mines report reviews and summarizes recent studies of the rates of chlorination of aluminous resources with CO and C12 mixtures with and without COC12. No reaction mechanism could be obtained from the existing results; however, diffusional barriers in the gas and solid layers probably control the chlorination rate in thermogravimetric experiments. Fluidized beds of particles smaller than 0.1 mm appeared to show very little solid layer diffusional barrier. For optimum chlorination the particle size should probably be less than 8 mm, the calcination temperature approximately 700° C, and the chlorination temperature from 650° to 750° C. Relatively rapid chlorination with COC12 in thermogravimetric experiments was attributed partly to the simultaneous supply of reductant and chlorinator by one gas to the sample reaction site. Comparable results for chlorination of fluidized beds with COC12 are not available. Equimolar mixtures of CO and C12 produced the optimum rate of reaction. Addition to the calcine of 10 to 20 wt-pct NaCl accelerated the rate of chlorination, and addition of SiC14 to the gas mixture decreased the rate of chlorination of SiO2 drastically, but at the expense of chlorination of significant fractions of Al2O3. Further research in various areas is suggested.

Jan 1, 1983

By Larry G. Stolarczyk

This report deals with information regarding a new Medium Frequency (MF) Wireless Communication System for underground mines. This new telecommunication system works on low loss electromagnetic wave propagation modes which allow it to provide quality radio communications almost anywhere in a mine. Tests show the MF system can provide improved safety and managerial control, increased productivity, better organizational team-work and reduced maintenance cost; furthermore, MF's unique design allows for easy installation at a minimum cost. This paper covers the following: 1) MF design plan, 2) Overview of mine radio communications systems, 3) Preparations needed for designing an MF system, 4) MF equipment, 5) MF installation, 6) MF design considerations, 7) MF design specifica¬tions, and 8) Recommendations dealing with MF system. Experiments in four mines are illustrated to demonstrate the success and via¬bility of the MF system. The mines range from small (500 tons/day) to large (67,000 tons/day) capacity and represent several different mining methods. The MF Wireless Communication System represents an advancement in mining communication and the groundwork for other advanced mine systems.

Jan 9, 1984

By C. C. Stevenson, Thomas Varley

"The art of treating ores by the chloride volatilization process is still in the experimental stage. The process has not been sufficiently developed along chemical and metallurgical lines to state definitely just what place it will occupy in the metallurgical industry. The theory upon which the process operates has received the attention of prominent metallurgists for the past twenty years, and research and experimental work has been conducted by many investigators.Much of the experimental work done has never been published, and it seems that the accumulation of such results if made known would be an important aid to the further development of the process. The object of this paper is, therefore, to bring salient features of the process to the attention of the metallurgical industry, both for the purpose of furnishing information, and receiving from interested parties any comments which the reading of this article may suggest. A bulletin covering the work done at the Intermountain experiment station of the U. S. Bureau of Mines, situated at Salt Lake City, Utah, is in course of preparation.The chloridizing roast is usually accompanied by appreciable losses due, to the volatilization of the metals as chlorides during the roast, these losses often running as high as 30 per cent, depending upon the temperature, the character of the ores and the associated gangue material. It was not until 1891 that Croasdale, (Croasdale, Stuart, Engineering and Mining Journal, Aug. 29 1903) by observing this and stack deposits from the chloridizing roast, recognized the possibility of making volatilization a major instead of a minor feature of the roast. He then made tests on a large number of tires from different, localities, the result of which showed the, general application of the process. The main difficulty, as stated, by Croasdale, was the lack of a suitable means for recovering the fume from the furnace gasesIn 1913, Cottrell (See Mining and Scientific Press, March 29, 1913; alsoTrans. American Institute of Mining Engineering, September 1918. (Additional informa-tion is available from the owners, The Research Corporation of New lark, and Western Precipitation Co., .Los Angeles, Calif.), announced his invention of the electrostatic precipitator, which solved the problem of separating the solids from the furnace gases."

May 1, 1921

By F. P. Haver

The purpose of this investigation was to determine the effect of common impurities, that is, oxygen, nitrogen, carbon, and iron, on the Brinell hardness of electrolytic titanium. On a weight basis, nitrogen had the greatest hardening effect, followed by oxygen, carbon, and iron in order. The hardening effects of oxygen and carbon were almost identical up to a concentration of approximately 0.1 percent by weight. Above this concentration, the relative hardening effect of carbon decreased rapidly, possibly because of its limited solid solubility in a-titanium. Hardness vs. composition curves for both oxygen and nitrogen were essentially straight lines over the range of Brinell hardness numbers (B.h.n.) covered in the investigation. The hardness of titanium was also determined as a function of the percentage of impurity atoms. On this basis, iron in concentrations up to 0.17 atomic percent had a greater hardening effect than either oxygen or carbon. INTRODUCTION Determination of the as-cast hardness of arc-melted titanium is a method of quality control widely used in industry. Numerous studies4/ have been made of the effect of impurities on the hardness obtained by this method. However, most of them have been based on the use of either iodide titanium or commercially pure Kroll sponge (B.h.n. >90), as a starting material.

Jan 1, 1959

By Leonard Obert

The various underground rooms in the Bureau of Mines Oil-Shale mine, Rifle, Colo., have been open for periods ranging from 3 to 5 years. During this time 3 roof falls have occurred; 1 was induced, and the other 2 were unintentional. The three roof falls are described in this report. Two causative factors are discussed -a time-dependent deterioration of the roof rock and an unfavorable system of jointing that occurred in the strata overlying the present roof horizon. Irrespective of cause, the operating life of any stoping area would have been short com-pared with the life of the roof (1 to 4 in the most unfavorable instance), if a high-production system of mining had been employed. The report is concluded with several recommendations that should be considered in planning future mining operations.

Jan 1, 1958

By Dwight L. Sawyer, Roy T. Sorensen

The Bureau of Mines has investigated the recovery of alumina by hydrochloric acid leaching of calcined kaolinitic clay . Bench- scale studies indicated that horizontal belt filtration was a pprraaccttiiccaall method for separating the siliceous residue from aluminum chloride liquor generated in the leaching step . Miniplant -scale continuous testing was performed to evaluate the filter circuits and to compare filtration response of different calcined kaolin feed materials and of different agitatorbaffle designs in the leaching reactors . Soluble alumina recovery with a single filter ranged from 94 pct with minus 10 -mesh feed more than 96 pct with minus 35-mesh or misted feed . Process advantages were confirmed for the calcined misted kaolin feed material prepared by a Bureau-developed misting process . With two filters in series , an overall filtration rate of 100 lb solids /hr.ft - 2 of filter area was attained with a soluble alumina recovery of more than 99 pct . More than 99.5 pct alumina recovery was obtained with a thickener and a two - filter circuit for either the minus 35-mesh or the misted feed . Modifications in leaching reactor design made to decrease particle- toparticle attrition were successful and significantly increased filtration rates and decreased flocculant requirements .

Jan 1, 1965

By H. C. Miller

For nearly a score of years the American petroleum industry has faced the problem of maintaining its economic structure while oil -producing potentialities greatly exceeded the increasing market demand for oil and its products . However , the combination of maximum civilian demand with rising defense requirements caused an all - time peak in crudeoil production in the latter half of 1941 , with a daily production (as estimated by the Bureau of Mines ) of 4,139,000 barrels in December - an increase of 16 percent over the daily production of 3,573,000 barrels in December 1940. In the event of a long war , a continuing , steady, and adequate supply of petroleum and its products for military and required civilian needs is essential, and the efficiency of recovery of oil from natural underground reservoirs will have to be maximum. Whereas it may not be possible to increase production in some fields , the output from others may have to be drawn at a much faster rate than formerly . More than 10 years ' experience in operating oil fields under proration control has demonstrated to petroleum engineers that some of the efficiency of recovery of oil from reservoir sands and rocks is sacrificed if the oil and gas are withdrawn at too . rapid a rate . As petroleum is an irreplaceable natural resource for which suitable substitutes probably will not be available in desired quantities for many years , any producing method that jeopardizes the quantity of oil that may be recovered from underground reservoirs must be considered at this time of declared war against aggressor nations as conflicting with the best interests of national defense . At best, the efficient recovery of oil is a complex problem . It involves not only a knowledge and application of the fundamentals of fluid flow through porous mediums, but the sources of energy responsible for the movement of oil and gas through reservoir sands and porous rocks to wells must be known to determine the best practices for extracting these hydrocarbons . Reservoir energy is of two kinds - (1 ) water under hydrostatic head underlying the oil in the extraneous parts of the reservoir system and ( 2 ) natural gas under pressure as "free " gas in the reservoir or in solution in the oil . Inasmuch as the efficiency of oil recovery depends largely on the manner in which reservoir energy is used to move oil through reservoir sands and porous rocks to wells , optimum practices for withdrawing the oil cannot be determined until it has been established that the oil in the reservoirs is being forced to wells by an internal gas expansion, by a natural water drive , or by a combination of gas expansion and water drive . There is a fundamental difference in the performance characteristics of gas - expansion and water - drive reservoirs . In a strictly gas - expansion reservoir the energy available to move oil and gas through the porous formations to wells results solely from gas pressure , which is maximum when the reservoir is tapped by the first well . Pressures decline as oil and gas are withdrawn ; consequently, the energy available for moving oil and gas through the oil - bearing formations to wells decreases with production . Curtailing the oil - production rate or shutting in gas - expansion reservoirs entirely will not act to replenish energy previously used in the production of oil and gas ; in their operation , therefore , it is especially important not to waste reservoir energy - the production of oil with high gas : oil ratios will be reflected in lower ultimate recoveries of oil .

Apr 1, 1942

By Fred D. Wright

Some new equipment for drilling vertical holes, cleaning blast holes, hauling explosives, and conditioning Diesel exhaust gas has been developed. at the Bureau's Experimental Oil-Shale mine near Rifle, Colo, The equipment has application, not only in oil-shale mining, but in many of the country's underground mines in which room-and-pillar methods of mining are employed. This report presents the Bureau's experience in testing the following equipment in the Experimental Oil-Shale mine: 1. A four-drill benching jumbo for drilling 23-foot vertical blast holes 2. A jet borehole blower for efficient cleaning of deep, vertical blast holes. 3. An explosives truck equipped with two compartments to provide safe conveyance for dynamite and detonators. 4. A mobile, electric substation to provide switching equipment, low-voltage and overload protection, and transformer facilities to remote locations in the mine. 5. A chemical conditioner for scrubbing the exhaust gases from Diesel-powered equipment used in underground operations. 6. Other units of equipment which have been tested at the Experimental mine.

Jan 1, 1951

By NIOSH Publication

In 2004, a total of 7,074 sand and gravel mining operations reported employment to the Mine Safety and Health Administration (MSHA).

Sep 1, 2007

By Forrest T. Moyer

In conjunction -with the statistical survey of the lime industr-.r in 1939, by the Bureau of Hines, producing companies reported the lime-fuel ratios attained in their plants according to type of kiln and kind of fuel. Each ratio, expressed as the number of pounds of lime burned by a unit quantity of fuel, was weighted according to the tonnage of quicklime pro- . duced at the reporting plant and grouped with similar data from other plants, so that an average ratio for each type of fuel and,kiln could be calculated. By this method the variables trat affect ratios of individual plants are more or less equalized, and the computed average lime-fuel ratios provide a fair measure of kiln and fuel efficiencies during 1939.

May 1, 1941

By H. W. Kilau

The Bureau of Mines evaluated synthetic fluorspar as a substitute for natural fluorspar flux in basic cupola ironmaking. The synthetic fluor-spars tested were prepared from waste fluosilicic acid generated during the processing of fluorapatite ore. The cupola trials showed the synthetic products to be the equivalent of natural fluorspar from an operational standpoint. However, wet scrubber sampling showed that substantial losses of volatilized fluorine occurred from the cupola during operation. The losses during synthetic fluorspar trials considerably exceeded those from natural fluorspar trials. Laboratory viscosity testing, using a high-temperature rotational viscometer, confirmed this finding and indicated that fluorspar volatility in slags is related to slag basicity. Synthetic fluorspar is accordingly recommended more for highly basic cupola operation (>1.3 basicity) than for neutral or acid operation, because of the increased potential for pollution and baghouse filter detezioration"

Jan 1, 1989

By R. Barany

The heats of the glass-crystal transformation of nepheline (Na0.7794K0.2206AlSiO4) and wollastonite (CaSiO3) and the heat of formation of nepheline at 298.15° K were determined by solution calorimetry. For the glass-crystal transformations, the heat values were -9.0 ± 0.3 kcal/mole for nepheline and -8.1 ± 0.2 kcal/mole for wollastonite. The heat of formation of nepheline was -34.8 ± 0.6 kcal/mole from the oxides and -501.0 ± 0.5 kcal/mole from the elements.

Jan 1, 1966

By D. J. Stoops, H. Kato, M. D. Carver

The effects of impurity elements silicon , aluminum, copper , nitrogen , and manganese , at 50 to 300 ppm, on properties of the zirconium alloy Zircaloy 2 were investigated . Variations in microstructure , mechanical properties , and corrosion behavior in some inorganic acid and salt solutions were observed with variations in level of impurity element . Corrodents were solutions of sulfuric acid , phosphoric acid , copper chloride , and iron chloride . Silicon was found to modify annealed microstructures by spheroidizing and dispersion of secondphase material throughout grains . Silicon or manganese improved ultimate and yield strength of the alloy without loss in ductility . All five elements affected corrosion rates of the alloy , the effect being generally different for each element .

Jan 1, 1964

By Albert E. Long

To date the commercial diamond bit setters have been principally interested in the speed with which they could produce a sharp, fast-cutting bit. Thus, a premium has been placed on setters who combine a high degree of manual dexterity with the ability quickly to select the Sharp points and edges of the diamonds and set them in the mold without lost motion. The premium on speed does not allow the setters the time, nor are they trained, to consider also the crystallographic structures of the diamonds which are the clues indicating the harder and more suitable working surfaces. Since early fall of 1949, the Bureau of Mines has been conducting a long-range series of experiments in which drill bort have been oriented in diamond bits in an effort to determine the effects and economic practicability of utilizing the hardest surfaces of the diamond crystal structure. The preliminary experiments completed to date indicate that a substantial saving in diamonds may be affected by using the harder areas of the diamonds as working surfaces in the crown of diamond bits. The experimental work is being conducted by the Bureau of Mines in the laboratories and full-scale mine of the Mining Research Branch, Minerals Technology Division, Region VIII, of the U. S. Bureau of Mines at the Mount Weather Station, Bluemont, Va.

Jan 1, 1951

By L. D. Schmidt, H. G. Graham

Several processes for the production of ultra-clean coal for electrode carbon were developed in Germany prior to and during World War II . These processes have been investigated since the end of the war by the British and U. S. Government missions . As the reports of the investigations are not readily available to the public , it is the purpose of this paper to present the information which has been obtained regarding the methods by which ultraclean coal was produced . Almost all the ultra-clean coal was used in the manufacture of electrodes for the production of aluminum and magnesium . Standard raw materials for making these electrodes are pitch coke and petroleum coke , which are nearly ashless . The inclusion of ash in the electrode carbon results in lowered efficiency and impure metal from the reduction process . Petroleum coke and pitch coke were in very short supply in Germany during the war , so that it was necessary to augment the supply with carbon produced from coal . In the emergency , methods were developed to clean coal which had never before been economically feasible . However , a demand for nearly ash-free coal might develop in the United States if a shortage of petroleum coke were to occur at the same time as a strong demand for light metals . Other uses of ultraclean coal are in direct hydrogenation of coal , in production of activated carbon, and for special fuels . Specifications for electrode carbon are rather severe owing to the necessity for producing pure metal . Maximum amounts of impurities allowable in American practice are as follows : Total ash , 1.0 percent ( in finished coke , 0.7 percent ) Silica , 0.08 percent Ca or Na, or their sum , 0.12 percent Sulfur , 2.0 percent Ba , Ni , Cr , Mn , Co , and V are objectionable in very small amounts . The most important process for ultra cleaning of coal in Germany was froth flotation . Froth flotation had been used widely there to process washery -water sludges and to recover coking coal from high - ash fines . Its use was indicated , therefore , when the demand for ultra low-ash coal arose . In two plants the coal cleaned by froth flotation was treated with acid or caustic to lower further the ash content . Another process used on an industrial scale was that of dissolving the coal substance in the middle oil from direct hydrogenation of coal under controlled pressure and temperature . The resulting paste was heated, filtered , and the oil distilled off . The residue was a low-ash organic material that could be carbonized for electrode carbon or could be hydrogenated directly . Several other processes had been developed to the laboratory or pilot - plant stage but had never been used on a commercial scale . These processes included cleaning by centrifugal action , cleaning by electrostatic action , and cleaning by forming a paste with oil in water . The coal-preparation plants at the Carl Alexander mine , Augusta Viktoria mine , and Kőenigin Elisabeth mine are described in Bureau of Mines Information Circular 7389 : " Coal Preparation Practice in Western Germany" , by Thomas . Fraser and M. G. Driessen . Most of the special equipment used at these plants is described in the above publication .

Oct 1, 1948

By K. K. Kershner, J. G. Donaldson

This investigation was conducted to obtain data on optimum conditions for chloridizing metal sulfides . Salt- roasting galena at 450° C for 8 hours chloridized 75 percent of the lead ; in an equal time of treatment at 750° C , the process chloridized 42 percent of the zinc in sphalerite . Hydrogen chloride at 500° C completely chloridized galena in 15 minutes , and at 600° C converted all of the zinc in sphalerite to the chloride in 4 hours .

Jan 1, 1963

By G. H. Gronhovd

This is the final report on a research program to develop a pilot plant gasifier for slagging gasification of lignite at high pressures and to obtain process data under various operating conditions. An operable pilot plant was developed, and the test results show that lignite is well suited for the process. Tests were run at pressures from 80 to 400 psig, and the results indicated that pressure had little effect on gas composition or the material requirements per unit gas produced. Gas production rates as high as 26,000 scfh/sq ft of reactor area were obtained at 300 psig, but limitations on auxiliary equipment prevented full-capacity operation at 400 prig. In several tests lignite having a 37-percent moisture content and 2,500° F ash-fusion temperature was successfully gasified. Refractory materials were found to have a short life in contact with high-temperature slag, and a water-cooled taphole was developed. Exploratory tests with coking coal were unsuccessful.

Jan 1, 1970

By V. E. Edlund

Laboratory batch flotation tests were conducted on copper converter slags to evaluate the relative merits of recovering copper from slow-cooled versus water-quenched slags. Three slags containing 1.6, 5.0, and 6.6 percent copper were used. More than 90 percent of the copper was recovered in a rougher concentrate leaving a 0.2- to 0.3-percent copper tailings when treating slow-cooled slag. Lower recoveries and higher copper tailings ranging from 0,5 to 0.6 percent copper were obtained from quenched slag. Grindability studies were made on the respective heat-treated slags. Quenched slags proved more difficult to grind than slow-cooled slags. Cost studies showed that (1) the cost of slow cooling and crushing off-sets any advantages of higher copper recoveries from slow-cooled slag, and (2) water-quenched slag, which requires no crushing preparatory to grinding, could be treated more economically. Costs based on processing 1,000 tons of slag per day would be $1.85 per ton for quenched slag versus $2.37 per ton for slow-cooled slag.

Jan 1, 1971