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Control respirable dust in underground coal mines through selection of optimum water spray pressures. Approach Through underground trials at longwall and continuous mining operations, the relationship between operating water spray pressure and respirable dust levels at the machine operator's location was determined. Defining the Application Water sprays are used for two significantly different control applications. On longwall mining machines, sprays are commonly installed both on the body of the machine and on the cutting drum. Sprays on the body of the machine are used to redirect dust which has already become airborne away from the machine operator. Each spray acts as a small fan, directing the primary airflow over and around the machine and towards the face, away from the operator. The energy of this system is directly related to the spray pressure. Higher pressures move more air, but care must be taken not to cause turbulence and boilout into the walkway. Sprays mounted on the drum are, effective at suppressing the respirable dust at the bit/coal interface and preventing it from becoming airborne. Again, these sprays must not impart excessive energy to the dust particles thus stirring up more dust than they suppress. While mounting sprays on the shearer drum is standard industry practice, there is no reliable technology available to successfully mount water sprays on the cutting drum of continuous miners. Instead, sprays are mounted on the machine body, close to the drum, and directed at the cutting head. This allows the water to reach the bit/coal interface and mix with the cut material. Here again, care must be exercised to prevent these sprays from imparting excessive energy to the dust particles and stirring up more dust than they suppress. These sprays can also cause dust "rollback" from the face, toward the operator, if operated at too high pressures.

Jan 1, 1986

By Forrest T. Moyer

THIS CHAPTER of the Minerals Yearbook contains injury experience and related employment information for the coal-mining, coking, oil and gas, peat, and native asphalt industries in the United States for 1962. Injury experience is measured by the number of injuries sustained per million man-hours of exposure in each industry. No attempt has been made to combine these data and present rates reflecting the mineral-fuel industries because the hazards of the separate industries are not comparable. Tabulations showing the trend of injuries and employment for all mineral industries are presented in volume III of the Minerals Yearbook. COAL The injury-frequency rate for the coal-mining industry of the United States increased less than 2 percent, according to reports received by the Bureau of Mines. The number of fatal and nonfatal injuries per million man-hours in 1962 was 45.86, based on final data for anthracite mines and preliminary data for bituminous coal and lignite mines.

Jan 1, 1963

By Joseph Grumer

In addition to nine powder and gaseous extinguishants of propagating Pittsburgh seam coal dust-air explosions earlier evaluated,6 10 other powders have similarly been evaluated under like conditions such that wall quenching of the coal dust-air flames was virtually absent and the dust concentration was temporally and spatially uniform to within about ±5 percent. None of the newly examined extinguishants was better than Purple-K (potassium bicarbonate); the 10 of this report are anhydrite (calcium sulfate), monobasic (4 types) and dibasic ammonium phosphate, natural and synthetic cryolite (sodium fluoalumi-nate), sodium sulfate, and tricalcium phosphate. Except for anhydrite, sodium sulfate, tricalcium phosphate, and the cryolites, these materials were about equally effective, when present in relatively low concentrations (weight-percent of the coal dust-extinguishant mixture). The maximum oxygen concentration for the extinguishment of otherwise uninhibited coal dust explosions and the influence of coal dust particle size and the volatile content of the coal were also explored. For the present, the choice of the inhibitor among the good ones evaluated is not as critical as the system to be used to deploy the extinguishant against a coal dust explosion.

Jan 1, 1973

Develop a simple and practical technique to measure in situ rock mass properties for realistic design and stability evaluation of underground structures. Background The Bureau of Mines has developed basic principles and techniques to determine in situ rock mass properties including Poisson's ratio, deformation modulus, and yield and failure strengths. An instrumentation package consisting of three pressure cells is installed in a single drill hole. Cell pressure response data are acquired and used to calculate and determine the rock mass properties. How It Works A test hole of BX size (approximately 5.7 cm) or larger is drilled to the approximate depth of the measuring point. The last portion of the test hole is drilled with precision bits to EX size (approximately 3.8 cm). The instrumentation package, which consists of one 3.8-cm-diameter cylindrical pressure cell (CPC) and two 5.7-cm-diameter cement-capsulated, flat borehole pressure cells (BPC's), is then installed. A complete history of cell response to changing strata loads is acquired on a continuous basis with a chart-type hydraulic pressure recorder. From these cell pressure data, Poisson's ratios, deformation moduli, and yield and failure strengths are calculated and determined.

Jan 1, 1990

Lower the respirable dust exposure of longwall shearer operators by use of a modified head to tail cutting sequence. Approach Modify the cutting sequence of double-drum shearer operations cutting unidirectionally head to tail, so that the tailgate drum is used to mine the entire coal face except when cutting out at the head. This approach would place the primary dust generating source, the cutting action of the drum, on the return air side of both shearer operators. How It Works Currently, 75% of the double-drum shearers in operation employ a unidirectional cutting sequence. On half of these operations, the primary cut is taken as the shearer travels from the headgate to tailgate ends of the face, with roof support to be advanced on the intake air side of the shearer. Typically, the leading (tailgate) drum is taking a full cut during the head to tail pass and the trailing (headgate) drum is cutting bottom coal. In this mode of operation, the dust generated by the trailing (headgate) drum can spread out into the walkway, and increase the respirable dust exposure of both head and taildrum operators. As an alternative, if the trailing drum is "free wheeling" or cutting minimal coal during the head to tail cut, and bottom coal taken by the tailgate drum during the tail to head clean-up pass, both operators are able to work on the intake air side of the primary dust generating source (drum) except when cutting out at the head. This modified cutting sequence would save wear on the conveyor and help to eliminate overloads, as well as reduce the respirable dust exposure of both shearer operators. This modifcation is only applicable to long-wail operations currently cutting unidirectional head to tail, and to those operations where this unidirectional cut would not produce operating constraints.

Jan 1, 1981

Reduce dust at the auger mine face by modifying airflow patterns, around the minim machine. Approach Limited clearance between an auger miner and the mine root restricts airflow across the face and causes dust rollback. Directional sprays arc used to direct air across the face, thereby reducing dust rollback and increasing dust dilution (fig. 1). Laboratory and underground studies were used to test and optimize effectiveness of the directional sprays. Results of Laboratory Study Laboratory experiments were conducted in a simulated auger gallery equipped with a full-scale mock auger miner and bridge conveyor. A dual curtain configuration was used to direct the, ventilation, which averaged 2,700 cfm throughout the experiment. Testing variables included spray location, pressure, spacing, orientation, and number. Figure 2 shows the optimized directional spray system, also called the auger clearer spray system. The system consists of three sprays mounted alone the intake side of the miner. Sprays arc spaced 16 to 24 inches apart, and angled 30° toward the return side of the miner. The 24-inch spacing moved about 7% more air across the face than the 16-inch spacing; however, it resulted in some additional misting on the return side of the miner. A 30° orientation was more effective than a 60° orientation for moving air across the face and minimizing misting on the return side of the miner. Flat fan sprays arc used because their spray paths arc not obstructed by the top of the miner and mine roof, A 50° fan angle is used to minimize misting on the intake side of the miner.

Jan 1, 1989

By J. F. Barkley

"In trying various coals at one of the Government power plants, comparison was made of the ash softening temperature of each coal, with the clinkering tendencies of the coal when burned in the furnace. The proximate analyses, ash softening temperature and plant reports as to clinkering were tabulated. It was desired to bring out any correlation that might appear between the ash softening temperature found in the laboratory, and the clinkering of the ash as found in the boiler furnace.Each coal used was sampled and analyzed, and the standard ash fusion test made. The clinkerring of the coal in the furnace was observed by the furnace operator. The furnace equipment consisted of the ""V"" or Murphy type of stoker with the ordinary fire-brick arch roof. With such arrangement very high furnace temperatures are apt to be produced at the ratings carried at this plant.The softening temperature of ash is defined as the temperature at which small cone of the ash, as tested in the laboratory furnace, has fused down to a spherical lump, The softening interval is the difference between the softening temperature and the temperature at which the first rounding, or bending, of the apex of the cone takes piece. The flowing interval is the difference between the softening temperature and the temperature at which the ash has reached a fluid condition as shown by spreading out over the base in a flat layer.While the analyses of the different samples of the some coal did not vary appreciably, the ash softening temperatures were not always so consistent. It will be noted from the following examples that the ash softening temperatures of different samples of the same coal differ as much as 290° F, Hence, in order to judge this property of a coal, many samples ore desirable, taken from many different shipment."

Aug 1, 1924

Provide mine safety personnel, MSHA inspectors, and original-equipment manufacturers with guidelines and a check list for inspecting rollover protection structures (ROPS) being used in mining operations. The Problem ROPS are provided on mobile surface mining equipment to protect operators from such safety hazards as machine rollovers, falling objects, and collisions. However, the protective capability of a ROPS can be greatly reduced if it is damaged. Certain kinds of damage, such as hair- line cracks, corrosion, and loosened bolts, may occur as a result of normal machine use but may not be recognized as unsafe by untrained personnel. Therefore, the Bureau of Mmes designed a manual which can be used by mine personnel when inspecting ROPS equipment. The Manual The manual was prepared to help acquaint mine safety personnel and MSHA inspectors with typical ROPS deficiencies and their causes. It provides a systematic means for inspecting ROPS so that the identified deficiencies and their causes can be corrected. It is suggested that an inspection of the ROPS be conducted after every 1,000 h of equipment operation, or sooner if the structure has been subjected to any unusual loads which could cause damage, such as a rollover, highwall caving, or collision. The manual also details common deficiencies in the structure and attachment hardware which may affect the service life. The checklist, when used as instructed in the manual, provides a means for systematically inspecting the structure to ensure maximum protective capability and conformance with applicable Federal regulations.

Jan 1, 1986

By Fred N. Kissell

In this report the importance of diffusion in controlling the emission of methane in mines is examined. An in-situ diffusion parameter is defined and calculated for a hypothetical unfractured lump of coal in the Pittsburgh and Pocahontas No. 3 coalbeds. The values obtained are similar to those obtained with lump coal in laboratory experiments.

Jan 1, 1972

By M. J. Ankeny

The expression "firing open, unconfined shots," as used in this circular, means the firing of explosive charges not confined in boreholes. Examples are the so-called mudcap shots, adobe or dobe shots, or bulldozing shots consisting of explosive charges placed on, under, or between rocks for the purpose of breaking them. The practice of firing open, unconfined shots is not uncommon in coal mines, despite the fact that numerous mine explosions and dust ignitions have resulted from this practice. The usual method of preparing such shots is to place the explosive with its detonator on top of a piece of rock or coal and cover it with clay, loam, sand, or road dust; frequently no covering of any kind is used. In some mines, an open charge of explosive is placed on timbers to dislodge them or in crevices in the roof to break down loose rock that cannot be dislodged with a bar or pick. The explosive charges may be made and fired singly, although sometimes several charges are placed on one large piece of rock with a detonator in each charge, and all charges are fired simultaneously. Although it is general practice to use permissible shot-firing devices, which will not ignite gas or dust to fire these charges, electric power from the regular mine circuits is sometimes used. When the shot is fired, any coal dust that may be present is thrown into suspension by the blast and may be ignited by the intense hot flame of the explosive or by an arc or spark at the leg wires or the end of the firing leads if power from the regular mine circuit is used to fire the shot. Even if there is not enough coal dust present to form a dust cloud, open, unconfined shots can readily ignite methane.

Jan 1, 1952

By Oliver Bowles

"In a previous report of the Bureau of Mines (Serial No. 2080 reference was made to a fatal accident from falling rock in a quarry in Utah, and ways of avoiding such accidents were pointed out. A fatal accident similar to it in some respects recently occurred in a limestone quarry in Maryland. All operators of stone quarries are desirous of reducing accidents to a minimum, and almost without exception they welcome any suggestions having in view the establishment of safer quarry practice. It is believed, therefore, that a brief outline of the cir-cumstances surrounding this later accident may be of practical advantage to quarry-men, as it may serve as a guide to them in so conducting operations that such unfortunate occurrences may be reduced in number.The quarry where the accident occurred is in form a circular pit 500 to 600 feet across an 80 to 100 feet deep. The rock is a dense limestone with the beds dipping at an angle of 35 to 45 degrees from the horizontal. Numerous erosion cavities in the form of pockets or narrow spaces following joint planes are filled with red sand and clay. They are confined largely to the upper 20 or 30 feet of the deposit. Open bedding planes are 4 to 10 feet apart toward the surface, and are spaced at wider intervals toward the base of the quarry. The open bedding planes present smooth uniform rock surfaces that dip steeply into the pit at the northeast side of the quarry opening. These smooth surfaces constitute a source of danger, as they may permit loose material to slide into the pit.In this particular instance a blast had been discharged, throwing down a mass of rock for steam-shovel loading. Three men wore employed thereafter for a period of about two days in cleaning down all loose material that might be dangerous to workmen luring the loading process. A mass of red sand and clay in which several large bowlders were embedded was left on one of these slanting surfaces, for the material seemed to be sufficiently secure to be quite safe. The lower edge of the slanting surface was about 25 feet above the quarry floor. The quarry conditions are illustrated in fig. 1, where (a) represents the quarry floor, (b) the vertical quarry (c) the slanting joint plane surface, and (d) the rock and earth resting on the surface."

Dec 1, 1921

By Thomas J. Fisher, John J. Sammarco

This report (System Safety 2.1) is the second in a nine-part series of recommendations addressing the functional safety of processor-controlled mining equipment. It is part of a risk-based system safety process encompassing hardware, software, humans, and the operating environment for the equipment’s life cycle. Figure 1 shows a safety framework containing these recommendations. The reports in this series address the various life cycle stages of inception, design, approval and certification, commissioning, operation, maintenance, and decommissioning. These recommendations were developed as a joint project between the National Institute for Occupational Safety and Health and the Mine Safety and Health Administration. They are intended for use by mining companies, original equipment manufacturers, and aftermarket suppliers to these mining companies. Users of these reports are expected to consider the set in total during the design cycle. • 1.0 Safety Introduction.—This is an introductory report for the general mining industry. It provides basic system/software safety concepts, discusses the need for mining to address the functional safety of programmable electronics, and includes the benefits of implementing a system/software safety program. • 2.1 System Safety and 2.2 Software Safety.—These reports draw heavily from International Electrotechnical Commission (IEC) standard 61508 [IEC 1998a,b,c,d,e,f,g] and other recognized standards. The scope is “surface and underground safety mining systems employing embedded, networked, and nonnetworked programmable electronics.” System safety seeks to design safety into all phases of the entire system. Software is a subsystem; thus, software safety is a part of the system’s safety. • 3.0 Safety File.—This report contains the documentation that demonstrates the level of safety built into the system and identifies limitations for the system’s use and operation. In essence, it is a “proof of safety” that the system and its operation meet the appropriate level of safety for the intended application. It starts from the beginning of the design, is maintained during the full lifecycle of the system, and provides administrative support for the safety program of the full system.

Jan 4, 2001

By Joseph A. DeCarlo

This information circular presents data for 1960 on individual coke plants in the United States. All oven-coke plants in existence, whether active or idle at the close of the year, are listed in this report. With two exceptions, only beehive plants on which reports were submitted to the Bureau of Mines are included. Although the Bureau was unable to obtain reports from these two active plants in 1960, the number of ovens and annual coke capacity are estimates, based on previous reports filed with the Bureau of Mines. Accordingly, there were 73 oven-coke plants in existence at the end of 1960 of which 70 were active. Reports were received on 44 beehive plants of which only 13 were in operation at year end. Oven-coke plants are listed alphabetically by States in table 1 which shows the name and address of the company, location of plant, classification or type of ownership, number and type of ovens, annual coke capacity, and coal-chemical materials produced. The terms "furnace" and "merchant" plants used in this and all other reports of the Bureau of Mines designate the type of ownership. Furnace plants are those owned by iron and steel companies whose main business is production of coke for use in their own blast furnaces. Merchant plants are those associated with chemical companies, gas utilities, as well as those that produce for sale on the open market metallurgical, industrial, and residential-heating grades of coke and coal-chemical materials. The annual coke capacity shown for each plant in this table is based on the minimum coking time necessary to produce coke with qualities suitable for its intended use. Therefore, the annual capacity of a plant may change from year to year, depending on age and condition of ovens, the character and quality of coal carbonized, the grade of coke required, and other factors. For example, annual coke capacity of a coke plant primarily making foundry coke with longer coking cycles would be lower than one making blast-furnace coke. Also some ovens must be operated at slightly lower than normal flue temperature because of the condition of the refractories and maximum capacity would be somewhat lower than designed capacity. For this reason, the capacity reported to the Bureau of Mines may differ from the designed or rated capacity estimated by the coke-oven builders at the time of construction. For example, if the generally accepted standard coking rate of one inch per hour were used on all ovens to calculate total annual capacity, it would have been 80.4 million tons or 2 percent higher than the capacity reported to the Bureau. Because of the factors mentioned above, the annual coke capacity shown in this table is believed to be a reliable measure of the practical operating capacity of the industry.

Jan 1, 1961

By Clyde E. Williams

The Northwest experiment station of the Federal Bureau of Mines , at Seattle , Wash . , was established in December , 1916 , and is one of 13 mining experiment stations maintained by Act of Congress , under the direction of the bureau , in the various sections of the country . Under the terms of the organic Act (March 3 , 1915 ) , the province and duty of these experiment stations is to cake investigations and disseminate information with a view to decreasing waste and improving the efficiency in the production , treatment , and utilization of mineral substances . The investigations carried on at the Northwest experiment station attempt to cover the needs of the mineral industry of the States of the Pacific Northwest and of the coastal regions of Alaska . The most in ortant needs of this district are for work on coal washing , electrometallurgy , and ceramics . The electrometallurgical investigations are not necessarily limited to the Problems of the Northwest , but may be of general application . Problems other than those specified above are referred to other stations of the Bureau that specialize on the particular type of investigation required . The Northwest station closely cooperates with the State of Washington through the University of Washington and with the State of Oregon through the Oregon Bureau of Mines and Geology . The University of Washington at Seattle has donated the use of an entire building , which houses the station's administrative offices and chemical laboratory , and parts of two other buildings which are usea in conducting the experimental avestigations . Twenty-five thousand dollars is expended annually by the Federal Government , while the State of Washington each biennium appropriates $ 20,000 , and the State of Oregon from time to time appropriates various amounts for the conduct of work along cooperative lines . Also , the station cooperates with private organizations tht have problems similar to those in which the station is interested . For example , the Washington Electrochemical Co. is cooperating in the electrometallurgical research, and furnishes part of the supplies and technical assistance required .

Mar 1, 1922

By Harry Dobroski, Larry G. Stolarczyk

Medium-frequency (MF) techniques have been successfully .[pplied] to the problem of radio voice communications in both coal and metal and nonmental mines. Long range is achieved by taking advantage of existing mine conductors that carry and propagate the signal over vast areas. It is very likely that in the near future such systems will become the referred method for general mine communications. MF techniques can also be applied to the areas of in-mine control and monitoring. Preliminary work in this area is described. In a western mine, locomotives are being operated under MF remote control in a loading operation. In several eastern mines, MF has been evaluated as a method for monitoring the status of devices in remote areas of the mines. All control and monitor information uses existing mine conductors.

By Dana Reinke, Launa Mallett

Interest in training evaluation in the mining industry was piqued with the promulgation of Title 30, Part 46, of the Code of Federal Regulations. Under Part 46.3, a training plan is considered to be approved if it contains certain information, including “The evaluation procedures used to determine the effectiveness of training.” The present paper is a broad overview of training evaluation and is intended to give trainers and decision-makers a framework for planning or assessing training evaluation strategies. It discusses questions to consider when starting an evaluation plan, Kirkpatrick’s model of evaluation categories, and various ways to collect data. It does not provide detailed instructions on how to develop evaluation methodologies, but reviews topics to consider when creating an evaluation plan. Training evaluation is a term that has many different meanings: assessing the quality of a course, effectiveness of materials used, teaching style of an instructor, or the comfort of a classroom. An evaluation can be done informally over lunch or with highly structured data-gathering tools. It can produce results that are useful to trainers, program administrators, corporate decision-makers, or no one. The key to a worthwhile evaluation is clearly defining why the evaluation is being conducted. Once the purpose is defined, planning the evaluation strategy can begin. For an evaluation to be effective, it should be incorporated into the development of the training activity itself. The training evaluation worksheet at the end of this paper can be used to guide evaluation planning.

Jan 1, 2002

Predict the spontaneous combustion potential of a mining operation using an expert system computer program.

Jan 1, 1994

By Sabri Ergun

The method of constant compositions involves the determination of the time required for the attainment of a given conversion at various temperatures. Heretofore, it has been used in evaluating the energy of activation only. A development of the method, made in the present study, makes possible the evaluation of the functional dependence upon composition and the frequency factor in addition to the energy of activation. INTRODUCTION Kinetics of reactions are best analyzed in the light of the mechanism, energy requirements, and forces involved in the reaction. Such physico-chemical information is not often available in solid state phase transformations. The reaction rates are followed by changes in a physical property during the course of the reaction, and repeating the experiment at different temperatures permits the determination of activation energy only. The possibility of a complete kinetic analysis by such a purely "phenomenological" approach has been questioned.4/ In this report a method is developed making possible the evaluation of the functional dependence upon composition and frequency factor in addition to the energy of activation. The application of the method to a study of solid state order-disorder changes is demonstrated.

Jan 1, 1960

By Ivette E. Torres

Table 8 provides data for the estimated value of world export trade of all mineral commodities from 1980 through 1991. It also provides a breakdown of the total into mineral fuels and non fuel minerals. These data have been developed from UN export trade data presented in table 9. The percent distribution and growth of the value of world export by major commodity groups are presented in tables 9, 10, and 11, respectively. In terms of industrial minerals (nonmetals), data in tables 10 and 11 include crude industrial minerals only, while table 8 includes an estimate for other industrial minerals. The 1991 estimates that appeared in the 1991 issues of this publication have been revised. It is typical for this section to review the year prior to the year of review because of the unavailability of data at the time of publication. The aggregated value of export trade in mineral commodities for 1992 was not available at the time of publication. The total value of nonfuel and fuel mineral exports for 1991 was about $616 billion in current (1991) dollars. The value of mineral fuel export trade accounted for about 53 % of the total mineral export trade. In 1980, the contribution of mineral fuel to the value of mineral commodity export trade had been almost 68%. The 1991 world mineral commodity export trade represents a 5.3% decrease (table 8) from that of 1990. The largest decrease was attributed to the decrease of export trade of fuel minerals (5%). The value of non fuel mineral export trade decreased by 4 %. Because the value export trade of all commodities increased by 1.2 %, the share of mineral commodities decreased from 19.2 % to 17.9 % of the total.

Jan 1, 1994

By E. G. Valdez

Iron foundries that melt automobile scrap produce flue dusts averaging about 32 percent zinc and 6 percent lead. Some is sold to smelters, but because of the meager return and difficulty in handling, most of the dust is discarded. As part of the Bureau of Mines program to find uses for mineral wastes, research was initiated to develop an economical process to recover zinc and lead from the flue dust. Research encompassed the extraction of zinc and lead by fuming, leaching, and agglomeration. Controlled vacuum fuming of zinc to produce Prime Western zinc and a lead-rich residue was the most effective method for treating the dust. This process involved two distillations, or fumings, with carbon and methane as reductants, and resulted in recovery of 91.4 percent of the zinc in a Prime Western grade product, and 98 percent of the lead. Hydrometallurgical techniques involved several leaching methods, but the simultaneous extraction of iron, manganese, and copper resulted in contamination of the solution and made the zinc recovery processes too complicated. Agglomeration was done by pelletizing or briquetting the dust for possible use as feed to a zinc smelter.

Jan 1, 1975