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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 John W. Cole

The Butte district has been the principal producer of metallurgical-grade manganese in the United States since World War I. Manganese dioxide nodules are produced from rhodochrosite ore by concentrating the rhodochrosite and roasting the concentrate in rotary "cement-type" kilns. The Anaconda Copper Mining Co. is the only producer at present. Under the stimulus of a purchasing program administered by Metals Reserve Company during World War II, however, several independently owned or operated mines (including the Norwich) produced manganese carbonate ore. These mines were examined in Juno 1949 by John W. Taber, mining engineer, Bureau of Mines. A core-drilling program to develop ore in the Norwich mine was recommended and approved. drilling was completed early in 1950. This report gives factual data obtained.

Jan 1, 1951

By J. F. Barkley

At the request of several Federal agencies, tests were conducted on a relatively recent type of anthracite -burning equipment named the Anthratube. This device, rated at 130,000 B.t .u. per hour, was designed to burn Pea-size anthracite automatically for steam or hot-water house heating and for domes-tic hot -water supply. ACKNOWLEDGMENTS The helpful cooperation of the Anthracite Institute and the manufacturers of the equipment, Axeman-Anderson Co., Williamsport, Pa., is gratefully acknowledged.

Jan 1, 1953

By R. V. Lundquist

The compound 2Na2O?3CaO?5Al2O3 occurs as a minor phase in lime-soda sinters prepared for extracting aluminum from siliceous aluminum-bearing materials. About 99 percent extraction of sodium and aluminum from synthesized 2Na2O.3CaO.5Al2O3 was obtained in solutions of NaOH-Na2CO3 at leaching temperatures of 50° C and above. Extractions in water were low because insufficient NaOH was generated by hydrolysis. Extractions in NaOH solutions were limited to about 80 percent owing to the precipitation of hydrated calcium aluminates. Rapid extractions of 100 percent were obtainable in NaaC03 solutions, but the subsequent rapid precipitation of alumina trihydrate caused losses in alumina recovery.

Jan 1, 1965

By R. Hogg, T. F. Dumm

"A procedure for evaluating the size/specific gravity distribution of ultrafine coal and the distributions of sulfur and ash with respect to particle size and specific gravity is described. The procedure is essentially an extension of the conventional coal washability technique in which special precautions are taken to ensure particle dispersion in the heavy organic liquids, centrifuges are used to obtain adequate separation rates, and micromesh sieves are used for size separation at fine sizes. An example of the application of this technique to the evaluation of the extent of liberation of sulfur and ash in a coal sample ground to 90Z passing 200 mesh (74 um) is described.INTRODUCTIONIn order to determine the potential for deep cleaning of coal by fine grinding to liberate sulfur and ash-forming minerals, it is necessary to obtain data on the distributions of these species by size and specific gravity. In conventional coal processing operations, this information is obtained by means of a standard ""washability"" analysis. Attempts to extend this procedure to ultrafine coal, however, have generally been unsatisfactory and have often led to unreliable and inconsistent results [11. The present authors have described a modified washability procedure in which cumulative specific gravity fractionation is combined with sub-sieve size analysis (by laser diffraction/light scattering) to determine the particle size/specific gravity distribution of ultrafine coal [2]. Unfortunately, because this technique does not involve separation of the individual fractions, only limited information can be obtained on the specific distributions of sulfur and ash.The objective of the work described in this paper was to develop and evaluate a procedure for size and specific gravity fractionation of ultrafine coal and to use conventional analyses for sulfur and ash to determine their relative distribution in the coal. The procedure is essentially a simple extension of the standard washability analysis [3] but incorporating special precautions for treating ultrafine particles.EXPERIMENTAL Material The material used in the development and evaluation of the ultrafine coal fractionation procedure was a medium volatile bituminous coal from the Lower Kittanning seam. A sample of the coal (nominally - 1/4 inch), obtained from the Penn State Coal Data Base, was ground to 90% passing 200 mesh by the following two-stage grinding procedure: About 2 kg of the as-received coal were ground to about 30Z passing 200 mesh in a Model 4-E Quakertown mill (""coffee grinder""). About 1 kg of this product was then ground to about 90Z passing 200 mesh in a Holmes Model 300 Pulverizer."

Jan 1, 1989

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 H. B. Brunot

A complete list of permissible mine equipment , tested and approved by the Bureau of Mines previous to January 1 , 1947 , was published as Information Circular 7432.27 A list of permissible mine equipment tested and approved by the Bureau of Mines during the calendar year 1947 was published as Information Circular 7465.3/ The present list supplements Information Circular 7432 and includes all of the equipment approved during the calendar years 1947 , 1948 , and 1949. It therefore supersedes Information Circular 7465. The list also includes an appendix ( No. 2 ) giving the symbol that must be used by every cable manufacturer in marking trailing cables that have passed the test for flame resistance as stated in the amendment of October 21 , 1947 , to Schedule 2E . The items are numbered to indicate the consecutive order in which each type of machine or device was approved in its particular classification . Thus , Information Circular 7432 showed six air compressors on the active list ; five additional compressors , Nos . 7 to 11 , inclusive , in this category were approved during 1947 , 1948 , and 1949 . Several items that were listed in Information Circular 7432 have been repeated in this circular where it was necessary to show that approvals of such equipment were extended to cover an additional voltage rating or other changes . Equipment listed in these circulars is approved by the Bureau of Mines only when found , upon inspection and test , to comply with minimum standards of safety as outlined in schedules prepared on the basis of many years of experience in dealing with safety problems of the coal -mining industry . The use of such equipment in mines known to be gassy , as well as in those that may become so , is earnestly recommended in the interest of safety . This circular is published so that the industry may be kept informed as to the many types of machines , devices , and lamps that are available for reducing explosion and other hazards incident to coal mining . This circular and Information Circular 7432 give the complete list of permissible mine equipment that is available under the various classifications .

May 1, 1950

By A. J. Kraemer

This paper on the physical and chemical properties of crude oils from California fields is one of a series of reports on the on the districts of the United States. The paper includes a short discussion of results, tabular data, and individual analyses of eight. California crudes. Analyses of other crude oils from California have been published it Reports of Investigations 2595, 2608, and 2846. The samples were obtained by members of the San Francisco office of the Bureau of Mines. The collecting 65 samples was facilitated by the courtesy of representatives of oil companies in California. The methods used in testing and analyzing the samples are described in detail in Bureau of Mines Bulletin 207. A discussion of the interpretation of crude-oil analyses, as made by the Bureau of Mines, is given in Bureau of Mines Report of Investigations 2806.

Jan 1, 1931

By O. C. Blade

A comparison of certain properties of the commercial aviation gasolines produced in the United States during October 1949, 1950, and 1951 is presented in table 1, the 1951 data being average values from tables 3 through 6 of the present report. Trends in the average values of certain characteristics of these fuels may be seen in figures 1 through 4 which also indicate the minimum and maximum values. As may be observed, with the exception of changes in kinematic viscosities, the properties of commercial aviation gasolines have not varied greatly during recent years. A list of aviation-gasoline survey reports published by the Bureau of Mines is given on page 6. A summary of the average values of the properties on jet fuels is shown in table 2.

Jan 1, 1952

By G. L. Oldright

This paper is the twelfth of a series on smelting in the lead blast furnace and the fifth dealing with blast-furnace gases. It was noted in Report of Investigations 2957 that the gases evolved from the top of the lead blast furnace at Tooele were similar in composition to those from the top of an iron blast furnace. It was noted in Report of Investigations 3095 that at Kellogg, where a smaller percentage of coke on charge and shorter stock column were employed, the gases evolved were much less reducing. At times there was a considerable amount of oxygen in the top gases at the second plant. More SO2 was also evolved from sulphides in the charge. Then operations were conducted as at Kellogg, the gases were alternately reducing and oxidizing. This paper deals with the gases evolved in smelting a charge containing more zinc than at either of the other two plants with about the same amount of coke as was used at Kellogg,: To compare other factors influencing the composition of the gases, it may be noted that at Tooele the approximate height of the charge column was 15 feet, at Kellogg 9 feet and at Trail 13 feet. The furnaces have about the -same cross-sectional area- tog. The furnaces at Tooele are about 6 inches wider at the tuyeres, being 54 inches wide against 48 for the other two plants. At Tooele and Kellogg the furnaces are fed at the top from bottom-dump cars. At Trail the charges are dumped from Decauville cars (bottom cars which dump when tilted), which run on tracks placed on both sides of the blast furnaces. The hoods through which the waste gases are conducted are directly above the shafts of the furnaces. The flues for removing the effluent gases lead off from under the charge floor at Tooele and Kellogg. (Charging and distribution of the feed in the furnace covered later in a rate paper of series.)

Jan 1, 1934

By Foster Fraas

The electrical conductivity of minerals increases with increase in temperature as a result of the thermal activation of the electrons. Some oxidizable minerals have a change in the stoichiometric proportions after heating in air, and the conductivity does not return to the original value after cooling. Similar changes occur in reducing atmospheres. Other minerals, such as carbonates and hydrates, are completely decomposed. Electrical resistivity measurements on single particles when compared to standard separation measurements show that minerals having resistivities above 1013 ohms respond as nonconductors. Those below 1011 respond as good conductors.

Jan 1, 1956

By J. H. Jacobs

The first authorization, in November 1940, was for a plant of only several hundred pounds capacity at Boulder City, Nev. Improvements in the process and subsequent additions to some sections have enabled the plant to produce more than 2,000 pounds of manganese per day for substantial periods. By the time pilot-plant operations were suspended in June 1945, over 1,500,000 pounds of metal had been produced. The future of electrolytic manganese production obviously depends not only on satisfactory development of methods but on availability of raw material and demonstration of valuable uses. Investigations of manganese-ore deposits in this country, made since 1938 by the Bureau of Mines, have revealed large amounts of ore suitable for making electrolytic manganese. At first the pilot plant was operated on ore from the Three Kids mine near Las Vegas, Nev. After practical features of the process had been worked out, other ores from throughout the United States were tested in the pilot plant. The purpose of this paper is to compare the results obtained on the following ores: Three Kids; Ladd mine, Tracy, Calif.; Chamberlain, S. Dak., nodules; and ore from Metals Reserve stockpiles at Deming, N. Mex.; Cushman, Ark.; and Philipsburg, Mont.

Dec 1, 1947

By R. B. Moore

The story of helium is one of the romances of science . Probably nothing , except perhaps radium , compares with it in human interest . Helium is one of the best examples of a discovery in pure science that has wide commercial application . In 1868 , an eclipse of the sun was visible in India , several scientific men who were in India making observations of the eclipse turned a spectroscope for the first time on the solar chromosphere - that part of the atmosphere of the sun , about 10,000 miles deep , which merges into the corona . A bright yellow line was observed and was thought at first to be due to sodium . Janssen showed , however , that this line was not just the same as either the D or D₂ line of sodium, although it was extremely close to these lines , hence he suggested that the new line have the designation D₂ . Frankland and Lockyer decided that Dz was due to an element in the sun not previously discovered on the earth , and suggested for it the name "Helium" from the Greek work " Helios " the sun . For several years nothing more was done in connection with this element . In 1894 , Sir William Ransay , in conjunction with Lord Rayleigh , made his memorable discovery of argon in the atmosphere , which was announced at the British Association meeting in the same year . After this discovery , Ramsay looked for other sources of the element . Through Sir Henry Miers , he learned that Dr. W. F. Hillebrand , of the United States Geological Survey , had obtained an inert gas from certain uranium minerals , which gas he had decided was nitrogen . Ramsay believed that part of it might be argon ; he obtained from Hillebrand for experimentation , a sample of the mineral , cleveite , one of the uranium minerals , and after extracting gas from the mineral and purifying it , he ran it into a spectrum tube . The lines obtained ' were , however , different from those of argon; among them was the bright yellow line noted by Janssen . Thus was terrestrial heliun discovered .

Jun 1, 1922

By C. B. Barmore, B. W. Gandrud, B. M. Bird

"The Bradford mine of the Alabama By-Products Corporation is located in the Warrior coal field of Alabama, in the northern part of Jefferson County, about 25 miles north of Birmingham. The coal mined from the Black Creek bed at this point is not considered to be ideal for coke making by itself but because of its exceptionally low ash content is mixed with the higher-ash coking coals from other beds of the district to control the ash content of coking mixtures. Further reasons for using this coal only as a diluent of the higher-ash opals are that the thinness of the bed renders the production costs relatively high and the reserves are somewhat limited.This paper, which is the fourth of a series on the washability of Alabama coals, Like its predecessors dealing with the Mary Lee beds and the Clark bed,6 contains screen-sizing and float-and-sink tests of a representative sample of the raw coal, and flakiness tests showing the proportions of flaky particles in certain selected sizes. However, inasmuch as the float-and-sink tests of the coarse sizes showed excellent liberation of coal from impurities, crushing tests have not been considered necessary.The data on which this report is based 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. As the work progresses other papers will follow containing further data on Alabama coals and giving results obtained in preparing these coals by various methods."

Apr 1, 1931

By R. G. Meara, O&apos

The land-pebble district of Florida, wnich in 1928 supplied 96.7 per cent of the phosphate production of that State and 82 per cent of the domestic requirements of the United States, is centered in Polk and Hillsboro Counties about 30 miles east of Tampa The deposits are unconsolidated sediments occurring as beds of phosphate matrix overlain by a mantle of barren sands and clays. The matrix consists of a mixture of sand (quartz grains), clay, and phosphate rock in which the coarsest sand is much finer than the coarsest phosphate; that is, the sand is segregated in the fine material. Before the introduction of classifiers the concentration consisted of log washing, and screening at about 20-mesh, which was usually the finest size that could be taken to maintain commercial grade, 66 per cent B. P. L. (bone phosphate of lime) or more. When classifiers were introduced some of the fines that had escaped at the head of the washery and some of the minus 20-mesh material isolated during the washing and formerly lost supplied the feed. During October, 1927, the United States Bureau of Mines in cooperation with the University of Alabama and the Missouri School of Mines and Metallurgy began to investigate the amenability of phosphatic sands to gravity methods of concentration. The work was under the immediate supervision of B. W. Gandrud, acting supervising engineer of the Southern Experiment Station of the U. S. Bureau of Mines at Tuscaloosa, Ala., and Will H. Coghill, supervising engineer of the ore dressing section of the U. S. Bureau of Mines. More comprehensive testing followed and in the early part of 1930 some of the companies cooperated with the bureau and the above-mentioned institutions in conducting a series of tests on hydraulic classification and tabling. The results indicated that marketable concentrates could be obtained with a recovery of 25 to 45 per cent of the phosphate formerly lost. As a result two companies have introduced hydraulic classification to treat the current tailings, and one of them has substituted classifiers for the 20-mesh screens which had been unsatisfactory. Because the phosphate grains and quartz grains have nearly the same specific gravity, the use of concentrating tables by the customary methods is not applicable. The washeries included in the following report are designated as Nos. 1, 2, and 3.

Jan 1, 1931

By Herbert R. Babitzke

As part of a project to develop refractory metal alloys suitable for high-temperature structural applications, the Bureau of Mines applied solid solution and precipitation-hardening techniques to columbium and tantalum alloys. Thirty-three alloys were evaluated to determine their formability, strength, and oxidation resistance. Three alloys had tensile strengths near 40,000 psi at 1,200° C: Cb-1N-5W-5V-10Hf (No.4), Cb-15Hf-5W-0.5B (No. 31), and Cb-15Hf-SW-IB (No. 32). Oxidation resistance of the high-strength alloys was good. Alloy4 gained only 34 mg/cm2 at 1,200° C, and 21 mg/cm2 at 1,000° C in 2 hours. Hot forming was done without any protection from oxidation.

Jan 1, 1968

By Jr. East

The Bureau of Mines conducted an investigation of the Nightingale tungsten deposit about 38 miles north of Fernley, Nev., from September 1939 to March 1940, to determine possible resources of tungsten ore. The property was owned by the Gold, Silver & Tungsten, Inc., which maintained its offices in Boulder, Colo. Ore was discovered in 1917, and some ore was mined in 1918 and treated in a mill at Toulon, a station on the Southern Pacific Railroad, 40 miles east. Same shipments were made since 1918, but no production figures are available. The ore is mined from nearly vertical tactite bodies at the limestone-granite contact. The Bureau of Mines excavated 944 linear feet of trenches, drifted 52 linear feet, sunk a shaft 20 feet in depth, sampled the underground workings by cutting 743 linear feet of channels, sampled the surface trenches by cutting 415 linear feet of channels, and drilled 9 diamond-drill holes, totaling 3,000 feet. The ensuing sections note the location and physical features of the district and specify the property and ownership. The history of the mine is briefed, and the geology and mine workings are described. The work done by the Bureau of Mines is summarized and supplemented in detail by assay maps, logs of diamond-drill holes in appendix A, and a table of sample analyses in appendix B.

Jan 1, 1950

By C. B. Manula, R. L. Sanford, R. A. Rivell

This report was prepared by The Pennsylvania State University under USBM Contract No. 60111808. The contract was initiated under the coal Mine Health and Safety Program. It was administered under the technical direction of DMSE, with M. G. R. Schottler acting as the technical project officer. Mr. J. A. Herickes was the contract administrator for the Bureau of Mines.

Jan 1, 1974

By Frank E. Cash

Accident prevention is an integral part of the operating procedure of the petroleum industry, and refinery officials and employees throughout the United States are exerting concerted effort to reduce the frequency and severity of accidents and are realizing definite results. In other words, the petroleum industry is safety conscious to a much creator decree than most of the other mineral industries. On January l, 1936, there were 11 operating, refineries in Louisiana with a crude-oil capacity of 199,750 barrels per day.4/ This report deals with safety in four of these refineries representing. 72 percent of the refinery capacity of Louisiana.

Jan 1, 1940

By Lindsay D. Norman

Four chloride and seven fixed-nitrogen processes for recovering manganese from domestic resources are described. The chloride processes are divided into two classes (leaching and chloridization) depending upon the major operation responsible for converting the manganese minerals to the chloride from which manganese oxide products are obtained. The fixed nitrogen processes, all of which yield high-grade manganese oxide products, are essentially either leaching or roasting processes. The 11 processes include HC1 leach, HC1 chloridization, HC1 chloride volatilization, CaC12 chloride volatilization, NO2 leach, HNO3 leach, HNO3 ?NO2 leach, H3 ?CO2-H2O system leach, (NH4)2SO4 leach, (NH4)2SO4 roast , and ammonium salt roast .

Jan 1, 1963