Search Documents

By Sandip K. Mukherjee

This report presents the results of the economic analysis of several applicable alternatives to increase airflow in four underground coal mines. Pressure-quantity surveys were conducted underground and measurements were also made at the main mine fan(s). The existing ventilation networks were modeled using the modified Penn State ventilation simulator. The applicable alternatives were simulated. Performance data obtained from these simulation runs were utilized to conduct the cost-effectiveness analysis. The costs for each of the alternatives included capital, operating and operating costs. These costs were expressed as annual ventilation costs per active section in terms of dollars per cfm taking into account the economic life associated with each of the alternatives. The benefits were expressed as increased airflow quantity in the critical sections. A section of this report also deals with comparison of simulator predicted air quantity values against air quantity values measured under-ground. This volume constitutes Volume II of the report and contains the outputs of the computer simulation runs.

Jan 1, 1983

By H. E. Perlee

The concentration limits of flammability and autoignition temperatures of trichloroethylene in atmospheres of air, oxygen, and nitrogen tetroxide have been determined in a spherical vessel. The autoignition temperatures of TCE in atmospheres of air, oxygen, and nitrogen tetroxide were found to be 419°, 396°, and 221° C, respectively. The flammability zones of TCE-air, TCE-oxygen and TCE-nitrogen tetroxide mixtures at 100° C were found to be 10.5 to 41, 7.5 to 91, and 13.5 to 69 volume percent TCE, respectively. In addition, maxi-mum combustion pressures of 50 ps and 140 were recorded for constant volume combustion of the lower limit mixtures of trichloroethylene in air and oxygen, respectively.

Jan 1, 1966

By Bruce D. Sartwell

A program was written which utilizes a remote teletype input to a time- sharing computer to plot charged particle or X-ray energy spectra which are stored in the memory of multichannel analyzers. The program, written in FORTRAN V, accepts the data printed out by the pulse height analyzer on paper tape and then, after reading these data tapes into the computer, plots on the teletype the desired energy spectra on a scale automatically adjusted for the maximum number occurring in the data. The program is flexible enough so that the researcher can subsequently expand or contract the vertical (intensity) or horizontal (energy) scales. With a slight modification, the program will accept data printouts from scalers or analog to digital converters. The program also includes a feature for integrating the energy peaks obtained by pulse height analysis.

Jan 1, 1970

By Charles P. Lazzara

Concentration profiles of low-pressure, slightly lean CH4-02-Ar flames have been measured in situ for the following unstable species: oxygen atom, hydrogen atom, hydroxyl radical, methyl radical, and formyl radical. The observed maximum mole fractions were 2.0X10-2 for H, 1.1X10-2 for OH, and 0.8X10-2 for 0; the maxima occurred in the recombination zone. Methyl and formyl radicals have maximum mole fractions in the reaction zone of 2.2x10-3 and 6x10-5, respectively.

Jan 1, 1973

By A. C. Richardson

The mine of the Porter Coal Co. is located at the town of Porter in the northwestern part of Jefferson County, Ala., about 20 miles west of Birmingham. The operations in this mine are confined to the middle and bottom benches of the Mary Lee bed. The coal from the Porter mine is handpicked and washed before being placed on the market. The handpicked lump coal and the washed egg and nut coal are sold chiefly as domestic and steam-raising fuel. The coal finer than 1 inch is washed in 2-compartment jigs and utilized in the manufacture of metallurgical coke. The coal company has found that, when coal ranging in size from 1 to 0 inch is washed in jigs, a considerable amount of high-ash material finer than 3/16 inch remains in the washed coal. This paper gives the results of an investigation which was conducted for the purpose of determining the washing characteristics of the through 3/16-inch raw coal and the extent to which the ash might be reduced by means of coal-washing tables. This investigation has been made in connection with an extensive study of the coal-washing problems now being conducted by the United States Bureau of Mines and the University of Alabama, with the cooperation of the coal-mining companies of the State.

Jan 1, 1933

By M. B. Shirts

Numerous alternative processes have been proposed as being potentially more economical or less polluting than the traditional smelting of copper sulfide concentrates. One such process as recently developed in the laboratory by the Bureau of Mines is composed of a two-stage fluid-bed, oxidation-reduction roasting followed by ammoniacal leaching, solvent extraction, and electrowinning. A copper-leaching recovery of 97.4 percent was obtained, and electrolysis of the acid strip solution deposited metal assaying 99.99 percent copper. The roaster gases contain over 95 percent of the sulfur at a concentration of 12 percent which is better suited for acid making or elemental sulfur production than conventional smelter gas. When considering byproduct recovery, a preliminary estimate indicates copper production costs are com-parable to the conventional smelters.

Jan 1, 1975

By George S. Rice, W. L. EGY, H. P. Greenwald, L. M. JONES

CHAPTER I. INTRODUCTION AND SUMMARY. BY GEORGE S. RICE. PREFATORY STATEMENT. This bulletin describes the second series of coal-dust explosion tests conducted by the Bureau of Mines in the experimental mine near Bruceton, Pa. It covers a period from 1913 to 1918, inclusive, of more or less consecutive testing, during which many important conclusions were drawn regarding the way a coal-dust explosion may originate, the mechanism of an explosion, and the methods of pre- venting explosions and of limiting incipient explosions. The manuscript was prepared in 1918, but its publication had to be put aside during the World War for more pressing publications and it was not until this fiscal year 1922 that funds could be allotted for its printing. Meantime the general facts concerning methods of preventing explosions have been made known to the mining industry, with great advantage, it is believed, as explosions of coal dust in mines in the United States have become infrequent. This fact, however, must not lull the consciousness of mining men to the terrible potential danger that lurks in untreated coal dust. The experiments described in this volume should be of aid to them in planning to keep the ever present coal dust in an innocuous condition. The first series-reported in Bulletin 56, "First Series of Coal-Dust Explosion Tests in the Experimental Mine"-included only pre- liminary tests of the ability to start explosions of coal dust under the conditions in the experimental mine. After this fact had been determined and several violent dust explosions had been demon- strated before large audiences of mining men, the work had to be suspended in order that necessary repairs and extensions might be made in the fall and winter of 1911-12. Although the question of the possibility of coal dust causing explo- sions had been considered for more than a century, and much testing in laboratory apparatus and in small surface galleries had been done, coal-mining men generally did not believe that coal dust was explo- sive and considered that fire damp or gases of unknown composition were responsible for the mine explosions that had cost thousands of lives in the various coal-mining countries during the last century. As coal mines increased in number, size, and depth, explosions became alarming in their frequency. Finally came the Courriéres disaster in northern France, 1906, by which 1,100 lives were lost, and the following year in this country, the Monongah mine explosion, in West Virginia, which killed 361 men, and the Darr explosion, in Pennsylvania, which killed 239 men. These two disasters, both in December, 1907, led Congress to make an appropriation for an in- vestigation of the causes of mine explosions. The funds became available July 1, 1908, and the work was placed under the United States Geological Survey's technologic branch, with the late Dr. Joseph A. Holmes in charge. Before undertaking the investigations Dr. Holmes visited Europe, accompanied by the senior author of this bulletin, to study the methods foreign countries used to prevent mine explosions, to obtain details regarding tests being made in several countries, to procure safer explosives and better safety lamps for use in gaseous and dusty mines, and to study the methods used in coal-dust explo- sion tests in the recently completed galleries at Altofts, England, and Liévin, France, and in the older galleries at Gelsenkirchen, Germany, and Frameries, Belgium. At all of these stations the explosions tests were made in surface galleries. The Austrian gallery at Segengottes, near Brünn, Moravia, visited by the writer in 1911, is an underground gallery, but the testing done in it was limited, dealing with ignition of coal dust rather than with propagation. Although the results obtained in the foreign galleries had indicated that coal dust was explosive, mining men in the respective countries were of the opinion that the dust would not explode under mine con- ditions. This situation led Dr. Holmes to the conclusion that testing must be done in a real mine, to make certain that the conclusion would be reliable and would be accepted by the mining public as decisive.

Jan 1, 1922

By W. M. Myers

[Utilization of small stone is recognized as one of the important problems of the lime industry. The term ?small stone' is used to designate material that is too small for calcination in tie shaft kilo. The maximum dimension A such stone rosy be placed at four inches. The introduction of any considerable quantity of stone having demensions lee: than this into the charge of a kiln impedes the draft and readers successful operation of the kiln difficult on impossible. Attempts design a shaft kiln which would calcine stall stone satisfactorily have not been successful to date. Thousands of tons of this small stone arc produced daily, and while part of it finds a market, for it has many uses, the profit is usually small an competition is teen and prices are low. Production of the material is, however, so greatly in excess of market that surplus of hundreds or possibly thousands of Jose axe place daily in stock piles and classified as waste. in a few instances a fortunate combination of circumstances, such as a program of or other work requiring large quantities of concrete aggregate, may mate it possible some quarries to market this stone later at a profit, teat in general the chances A profitable utilization are slight, and the quarry operator has the expense of handling this waste stone and providing a storage site for it. The brittle nature of limestone makes it impossible to quarry the stone and crush, it to size suitable for the shaft kilns without producing an excess of undesirable fines. Elimination of fines by changes in quarrying or crushing practices cannot lee expected. On the contrary, the adoption of more modern methods of quarrying in recent years has increased the proportion of small material. The tendency is to blast the roan with large charges of explosives and crush it with mechanical crushers, which produces more fines than the older methods of careful blasting with small char yes and sledging the rock by hand.. We increasing use of underground mining of limestone has also increased the production of small stone, as blasting in the confined space of an underground stope shatters the rocs more completely than quarrying in the open. The use of the very friable limestones, such as the limestone of Florida for the manufacture of lime adds a new factor to the calcination of small stone. These friable lime limestones have a low tensile strength and crumble in the kiln, causing trouble. Successful calcination of these stones is accomplished in specially]

Jan 1, 1926

By C. E. Schmidt

Condensate waters from the Bureau of Mines Synthane process for coal gasification have been investigated by mass spectrometric methods to determine the organic contaminants. Waters from the gasification of six coals were extracted with methylene chloride, yielding 0.6 to 2.4 weight-percent extractable material. Using high-resolution mass spectrometry (HRMS), combined gas chromatography-mass spectrometry (GC-MS), and low-voltage mass spectrometry, 60 to 80 percent of the extract was found to be phenolic. About 20 organic contaminants have been identified and are present in the condensate waters from each coal gasified. The relative distribution of contaminants in the condensate water was nearly the same for the six coals gasified under various conditions; phenolic compounds were the most abundant in all cases.

Jan 1, 1974

By Foster Fraas

A comparison has been made between cubes and spheres in the matrix of the high-intensity wet magnetic separator. For two inclined plane surfaces, such as may occur with cubes, the maximum force value, H [dH-dx] is at the point of nearest approach and is much higher than the force resulting from adjacent spheres. Although the maximum force value for cubes is higher, it decreases more rapidly at increasing distances. The maximum force for spheres is at an appreciable distance from the point of nearest approach. At field intensities for magnetic saturation of the iron spheres, the force extends to further distances with greater uniformity approximating that of the constant force or isodynamic field. The force is also independent of the sphere diameter, which permits the scaling of the sphere diameter to provide changes in particle migration distances without changes in force gradient.

Jan 1, 1972

By C. N. Adams

The purpose of this investigation was to evaluate the physical and mechanical properties of high-purity titanium made by two processes. Sodium-reduced metal with 58 Brinell hardness number (B.h.n.) and electrorefined metal with 60 B.h.n. and 70 B.h.n. were used. Titanium of these hardness levels did not work-harden excessively, and beyond 40 percent cold work the hardening effect was not great. Rapid softening occurred when the metal was annealed at temperature between 300° and 600° C. Full annealing, as determined by property and microstructure studies, was accomplished after 30 minutes at 700° C. A recrystallization diagram is presented which is based on determinations of annealed grain size as a function of rolling reduction and annealing time. For reductions of less than 20 percent, exaggerated grain growth occurred during annealing; for reductions greater than 20 percent, the variation in grain size for each annealing temperature was minor.

Jan 1, 1961

By J. M. Davidson, F. Fraas, J. E. Conley

"A number of Reports of Investigations pertaining to the extraction of potash from cal¬cined polyhalite have been made by various members of the Nonmetallic Minerals Experiment Station of the United States Bureau of Mines. These reports describe results obtained in the study of samples of polyhalite (2CaS04.K2S04.MgS04.2H20) from deposits of possible com¬mercial importance in Texas and New Mexico.3Storch and Clarke6 in their initial paper presenting data on the properties of Texas polyhalite demonstrated the desirability of calcination and subsequent hot extraction with water as a satisfactory pronedure for treatment of this potash-bearing salt. Their preliminary data have been supplemented by an additional report7 dealing more particularly with the leaching of raw and calcined polyhalite with water and with saturated sodium chloride solu¬tions. Further data8 have been reported as a result of experiments made in a small labora¬tory rotary-tube furnace under various calcination and extraction conditions. Hot water was used as the leaching solution in all of these tests.In addition to the data on calcination and extraction, two processes as proposed by Storch and Clarke have been published by Wroth,9 and more recently a number of very promising processes have been proposed by Storoh and Fragen.10"

Apr 1, 1932

By Robert W. Metcalf

The feldspars are a series of related aluminum silicates containing varying proportions of potash, soda, rind lime; smaller amounts of other minerals arc likely to be present as impurities. They comprise three principal types: Potash spars, microline and orthoclase (KA12Si208); soda feldspar or albite (NaA1Si308); and soda-lime e (plagioclase) fellspars. The last-named is an intermediate group ranging from albite through oligoclase, andesine, labradorite, and bytownite to anorthite or line feldspar (CnA12Si2O8), Minor varieties are barium feldspar or celsian and a potash-barium feldspar. Perthite is a mixture of orthoclase end albite in alternate layers. Graphic granite or "corduroy spar" is an intergrowth of feldspar and quartz characteristically in the ratio of 3:1. Cornwall stone is a natural mixture of feldspar, quartz, end kaolinite imported in former years in sizable quantity from Cornwall, England. (A similar synthetic mixture, including some fluorspar, has been blended and marketed in the United States as "Carolina stone".)

Jan 1, 1941

By I. L. Nichols

Volatilization of cesium from pollucite ore was investigated as an initial step in the production of purified cesium metal or cesium salts. High recovery of cesium and rubidium as chloride sublimates was accomplished by 2-hour roasts in a tube furnace using charges containing 1 part ore, 2 parts limestone, and 0.23 part calcium chloride. Recoveries of cesium in the sublimate product were 89.1, 92.9, and 95.2 pct, respectively, using 1,100° C and vacuum, 1,250° C with an air sweep, and 1,250° C without an air sweep. Most of the lithium, sodium, and potassium sublimed with the cesium and rubidium, but virtually none of the calcium, aluminum, and silicon in the charges was volatilized.

Jan 1, 1966

By Allen S. Smith

Analysis of the helium content of a natural gas presents more than the usual difficulties encountered in applying the thermal-conductivity method because of the relatively small amounts of this inert as present and the wide variation in the other constituents. However, the numerous advantages of this method and its adaptability to Continuously recording and control instruments make it worthy of consideration. A specific application of the method described yields quantitative results only when used with gas mixtures of known qualitative compositions which Vary within predetermined limits. Periodic analyses for the helium content of a producing gas well may be conveniently made by an absorption method, and a continuums analytical method is not necessary for this purpose. Natural gas containing 1.75 to 1.90 percent of helium produced from Government-owned wells is processed in the Amarillo (Texas) Helium Plant of the Bureau of lanes. The helium extracted in the plant is supplied to the Army and Navy, and the processed natural gas is sold to a commercial gas company. As complete recovery of the helium in the raw material is not economically practicable, the processed gas contains 0.1 to 0.3 percent of helium, depending upon conditions of operation. Production is checked against the helium removed from the gas, which before the installation of the thermal-conductivity apparatus was calculated from the analysis of a cumulative sample of the processed gas. As conditions of operation affect the residual helium content to a large extent, a composite sample was an uncertain index of the efficiency of the process.

Jan 1, 1934

By G. D. Bakulev

Economic Importance of Gasification of Fuel and Brief Outline of Development of Underground Gasification of Coal in the U.S.S.R. The underground gasification of fuel offers a number of economic and social advantages, principally the following: 1. Full automation of labor-consuming coal-mining processes, which resist complex mechanization and automation, particularly shaft mining. 2. Elimination of hard, dangerous, and often unhealthful mining work. 3. Creation of hygienic conditions for personnel employed in gas production, as well as for those in boiler rooms using the gas. 4. Possibility of automation of complex production processes of thermal-electric powerplants using underground gas with economic installations for steam production. 5. Economic operation of thermal-electric powerplants constructed in the areas of underground-gas production. 6. Release of railroads from the burden of transporting fuel. 7. Extension of the power base of some areas in need of fuel and of the economy as a whole due to use of fuel deposits not amenable to normal mining practices. 8. Reduction of capital investments per unit of energy produced in the form of fuel. 9. Substantial increase in general labor productivity. 10. Possibility of substantial reduction in the cost of fuel produced and of electric power produced from underground gas.

Jan 1, 1962

By A. T. Coumbe, I. F. Avery

The Bureau of Mines has completed a survey of petroleum pipe - lines by direct correspondence with the oil companies and the use of the records of the Interstate Commerce Commission in order to cover both interstate and intrastate systems . The review shows that crude petroleum and product pipe -lines in the United States had a total length of 152,814 miles on January 1 , 1950 , an increase of 25,463 miles since May 1 , 1941 , the time of the last previous survey . The expansion in pipe -line systems was due largely to new trunk-line construction , as the mileage built to carry refined products increased by 11,880 miles , and those intended for crude -oil transportation gained 6,193 miles . Trunk lines represented 60 percent of all pipe -line mileage on January 1 , 1950 , compared with 58 percent in 1941 . The average diameter of trunk -lines for crude oil , as calculated on the various sizes and weighted according to their respective lengths , increased to 9.8 inches on January 1 , 1950 , compared with 8.4 inches on May 1 , 1941. The mileage for lines up to 8 inches used in crude trunklines has decreased since the 1941 survey , while those of larger sizes have increased . The extensive use of large- diameter oil pipe -lines has developed since the construction of two major lines from Texas to the East Coast at government expense as a World War II emergency measure . The successful operation of these lines proved their economic advantages over smallerdiameter lines as well as their effectiveness in moving unprecedented volumes of oil during the period when tanker movements were restricted by submarine action in the Atlantic Ocean . The 24-inch diameter " Big Inch " line carries over 300,000 barrels daily of crude oil , and the 20 -inch " Little Big Inch " carried over 230,000 barrels daily of gasoline and light fuel oils to destinations where they were urgently needed . Hence , Although these lines were sold and converted to natural -gas service in December 1946 , after fulfilling their wartime mission , their record proved to the industry that significantly lower operating and investment costs per barrel -mile of oil moved could be achieved than were possible with the comparatively small lines in general use up to that time . the several major oil pipe -line projects that have been constructed since the late war are of large diameter pipe . To assure supplies and market outlets of sufficient magnitude to support such lines and provide adequate flexibility , ownership is often shared by several large companies whose transport needs are served in common . The principal recent expansion in facilities has been from supply points in Southwestern States toward markets in the North and East and to Gulf tidewater .

Dec 1, 1950

By Sol Weller

The Fischer-Tropsch synthesis consists of the formation of long-chain hydrocarbons by passage of carbon monoxide-hydrogen mixtures over metal catalysts, usually based on iron, cobalt, nickel, or ruthenium, at temperatures in the range 180°-300° C., and at pressures of 1-15 atmospheres. Although the reaction has been known and studied for more than 20 years, the mechanism by which it occurs is still poorly understood. One approach to understanding is to consider the effect upon the course of the synthesis of variations in each of the important operating variables. Consideration of the experimental data pertaining to these variables may suggest an over-all picture describing the synthesis - a picture which, in turn, would have to be consistent with all the known facts. The first part of this paper will be concerned with such a consideration of operating variables; the second portion will discuss recent work pertaining to the role of metal carbides as intermediates in the synthesis.

Jan 1, 1949

By Larry R. Wilson

The development effort described herein was directed toward the design and development of a flexible communication system to provide two-way section communications between any telephone on an MCM-101 telephone FDM exchange and a miner provided with a uhf walkie-talkie transceiver. The system also provides normal communication between miners within a working section through the uhf coupler interface repeater.

Jan 1, 1976

By R. L. Benner

A compound stability diagram was constructed by the Bureau of Mines for the Zn-Fe-S-O system to show the phases that should be thermodynamically stable at various temperatures, oxygen pressures, and SO2 pressures. The diagram was demonstrated to have good qualitative value for predicting stable phases that may, in turn, be related to the recovery of zinc in the leaching phase of the electrolytic zinc process. The study showed that roasting temperature is the most Significant variable in preventing roaster formation of zinc ferrite, which is directly related to subsequent extraction of zinc in the leaching step.

Jan 1, 1966