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By Marvin W. Wilson

The Federal Bureau of Mines has conducted laboratory experiments simulating underground gasification of coal to study the feasibility and mechanism of the process and determine the chemical and physical characteristics of a coal-bed during gasification. Laboratory and small-scale field experiments also were made to investigate the properties of coal and other factors affecting the electrolinking-carbonization method of preparing a path through a coalbed before gasification. Laboratory experiments simulating underground gasification of coal: Experiments with a laboratory retort indicated that bituminous-coal deposits could be gasified in place to produce a combustible gas.

Jan 1, 1960

By Theodore L. Turner, Joseph H. Swift

A study on a small laboratory scale was made of the use of ammoniacalammonium carbonate for batch leaching Mn from low- grade manganiferous materials ( 6 to 16 pct Mn) obtained from deposits in the southern district of Aroostook County , Maine . These materials were partially reduced at 500 ° to 700 ° C with H₂ or CO and then leached with solutions of NH and CO₂ dissolved in water . Extraction of 80 to 90 pct of the Mn was obtained from some sample materials , but 10 to 34 pct of the iron was also extracted . Material from the Littleton Ridge deposit contained manganese intimately associated with Fe , a condition which contributed to difficulties in obtaining a commercially acceptable product . Extensive investigations of the leach and reduction processes with various mixtures of H₂ and water vapor , and CO and CO₂ , failed to disclose a set of conditions for selectively leaching the manganese . Finely divided metallic Fe was probably produced during the reduction steps so that Fe was leached with the Mn in the subsequent extractions .

Jan 1, 1964

By E. P. Youngman

The rapidly growing demand for titanium pigments has aroused new interest in actual and potential sources of supply of titanium- bearing ores , which only a comparatively few years ago were almost unmarketable . This paper , which supplements a general circular entitled " Titanium" ( Information Circular 6365 ) , represents a summary of current trade literature and Government reports , together with some hitherto unpublished material that has accumulated in the files of the Bureau of Mines . The purpose of this pamphlet is simply to indicate the commercial possibilities of the deposits , and the discussion is confined almost entirely to the three commercial ores , ilmenite , rutile , and magnetite ( titaniferous iron ore ) .

Oct 1, 1930

By Wilson Blake

Rock preconditioning in advance of mining was shown to be an effective means of rock-burst control based on the results of a field demonstration carried out on the 7700 level of the Hecla Mining Company's Star mine. Mining through the preconditioned zone was characterized by greatly reduced rates of released seismic energy and no bumping or rock bursting occurred within the preconditioned zone. Mining above the preconditioned zone was characterized by greatly increased rates of released seismic energy and rock bursting, particularly where the vein became very narrow in waste zones. This increased incidence of rock bursting points out the need for stope preconditioning to be carried out on an entire stope block basis. The data obtained from the monitoring of the mining above the preconditioned zone on the 7700 level will be extremely useful in evaluating any future stope block preconditioning experiments on the lower levels or the Star mine.

Jan 1, 1980

By James W. Martin

This user?s manual analyzes the application, selection and performance of hopper/crusher/conveyor systems used with front-end loaders in surface mining operations. It is designed to be used in conjunction with its companion manual: "Guideline Manual for Front-End Loader Load-and-Carry Applications" Aspects of the application are covered as well as design considerations of the hopper/crusher/conveyor units. Lists of equipment manufacturers, crusher specifications, together with a series of checklists, are included for preliminary analysis.

Jan 1, 1982

By GJ Hundman

The Multiple Unit Continuous Haulage (MUCH) System was designed to provide the capacity to continuously convey coal from the mining machine to the main haulage belt. The MUCH System has an operator who steers the lead vehicle, ever following the mining machine. All the remaining vehicles follow the path of the lead vehicle, with their conveyors automatically lining up between the lead vehicle and mine section panel belt. This is accomplished by mechanical linkages on the vehicles which are interconnected by steering bars between vehicles (patent pending). The MUCH System has an operator who steers the discharge vehicle when outby travel is required. Outby travel is just like inby, with each vehicle following the path of the preceding vehicle. Surface tests overwhelmingly indicate the "UCH System should track/retrack successfully in square pillar underground room and pillar coal mines with 18 ft. wide entries and slopes up to 10 percent. For 60 degree pillar plans the minimum entry width required is 15 ft. Surface tests also indicate the MUCH System will convey over 8 TPM of coal around 90 degree corners without excessive spillage.

Jan 1, 1983

By Anthony W. Sparks

The Bureau of Mines conducted tests designed to compare its breathing metabolic simulator (BMS) with other methods that are currently used to evaluate the performance of respiratory protective equipment. The BMS is a commercially developed device that uses a piston cylinder to simulate breath movement. Using a propane furnace that consumes oxygen and forms CO2, the BMS also simulates the respiratory metabolism of humans. The breathing and metabolic subsystems of the BMS are described in detail in this report. Results are compared from tests that used the BMS to evaluate respiratory equipment and from tests that used human subjects for the same purpose. The BMS was also tested against a pulsatile breathing machine (PBM) previously designed by the Bureau. Both machines were used to test respiratory equipment, and the test results are compared in this report. To illustrate typical applications of the BMS, the report briefly describes how the BMS was used to test two different types of closed-circuit respiratory apparatus, and the test results are presented. This research showed that BMS test results compared more closely to the results of tests that used human subjects than did results obtained using the PBM.

Jan 1, 1980

By M. D. Aldridge

The results of designing, constructing, installing and operating a ventilation monitoring system throughout an entire commercial coal mine is presented. Measured parameters were airflow, methane, carbon monoxide, temperature, relative humidity and differential pressure. A central computer provided for automatic system operation. Preliminary tests of two remotely controlled ventilation regulators were performed in conjunction with the monitoring system.

Jan 1, 1977

By A. J. Kauffman

The alluvial deposits of the Pacific Northwest have been investigated and worked with varying degrees of intensity since about the middle of the 19th century. Earlier efforts, of course, were centered about the placer-gold content of the deposits; later, the Oregon beach sands were exploited for their chrome content, and, still more recently, deposits in Idaho were worked for their content of monazite, a rare-earth mineral which also contains significant quantities of thorium. The composition of alluvial deposits seems to depend mainly upon the nature of the source rock from which the detrital material was derived and upon the resistance of the individual mineral grains to the agencies of weathering and transportation. The processes of crushing and concentration used in ore dressing are applied in a leisurely but nonetheless effective manner when exposed rock masses are eroded by natural forces. Weathering effects a continuous disintegration and chemical decomposition, wherein resistant minerals are set free as individual grains and new minerals are formed. Erosion carries these detrital products down the slopes into natural waterways, where a mechanical separation of heavy particles from light is accomplished by the running water. The accumulation of such resistant, heavy particles through the ages has resulted in formation of the black-sand deposits. In addition to the associated gangue minerals, heavy sand deposits in the Pacific Northwest may contain the following constituents of possible economic value: Gold, platinum, chromite, ilmenite, magnetite, garnet, zircon, monazite, columbite-tantalite, and radioactive blacks.

Jan 1, 1956

By G. L. Gates

The Bureau of Mines in cooperation with the City of Long Beach) Calif.) studied some physical factors effecting the deposition of barium sulfate scale in oil-well rotary pumps. Freshly formed barium sulfate was obtained by combining sulfate in sea water with barium from a barium chloride solution. The rate of scale deposition was measured quantitatively by weighing the pump impellers and diffusers. The results of the tests showed that coating the impellers with plastic significantly reduced the rate of barium sulfate deposition.

Jan 1, 1967

The mine surveillance and communication system hereafter described provides continuous local and remote monitoring of several parameters critical to normal mine operation at each of ten underground sites in the Bruceton Research Mine. The techniques employed are well proven and have been care-fully chosen to provide the best solution to the technical problems involved while giving special attention to economic considerations.

Jan 1, 1973

By J. L. Eakin

Systematic flooding was introduced into Nowata County, Okla., in May 1931. The results of this means of stimulating the nearly depleted Bartlesville reservoir in the county has been the subject of four Bureau of Mines Reports of Investigations.2-5/ This report presents a discussion of four full-scale water-flooding projects in the Delaware-Childers field and 1 pilot project in the Curl Creek field (fig. 1). All five plants have been in operation for only a few months. Although substantial increases in the rates of oil production have been obtained 1 by the injection of water, the projects are of particular interest at this time because of the novel methods of operation and new equipment that are being employed. One project utilizes a portable "package" plant designed for a pilot operation. All of the controls for this project are centrally located. The design makes it possible to remove the test plant to another location if the project is unsuccessful or if the unit is to be replaced by a larger plant. This project also utilizes diatomaceous-earth filters successfully for the first time and makes use of plastic pipe. Another novel feature of the operation is the aeration of Arbuckle limestone water through an airlift in the supply well.

Jan 1, 1955

By H. J. Heinen

To maximize productivity through improved minerals processing technology, the U.S. Department of the Interior, Bureau of Mines, is investigating particle agglomeration techniques as a means of increasing the percolation rates of leach solutions in heap leaching of clayey gold-silver ores. Simulated heap leach experiments were conducted on 50-pound charges of ore that were contained in 5.5-inch-diameter columns, 5 feet in height. Results indicated that the percolation rate of cyanide leach solution could be enhanced markedly by mixing the ore with controlled amounts of lime, flocculants, and water, and then aging the mixture prior to the column leach step. Experimental results obtained on 20-mesh silver tailings and gold ore crushed to 3/8 inch and to 1 inch showed that it was possible to increase percolation rates as much as 100-fold without sacrificing silver-gold extraction. Larger scale tests conducted in 24-inch-diameter, 16-foot-high columns closely paralleled bench-scale results. By improving percolation leaching, these techniques have the potential of helping to solve environmental problems associated with tailings disposal as well as making an important economic impact on gold-silver recovery operations. Investigations are continuing to develop binders superior to lime for particle agglomeration pretreatment.

Jan 1, 1979

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

This report is in fulfillment of Contract H0230031 awarded to Bituminous Coal Research, Inc., on May 23, 1973. The scope of work to be performed under this contract was divided into four phases: Phase I - Design, Phase II - Construction, Phase III - Field Demonstration, and Phase IV - Analysis and Final Report. During Phase I, an agreement was finalized with the Rochester and Pittsburgh Coal Co. for conducting field tests of the proposed shearer spray systems on a longwall panel in the company's Jane Mine in Indiana County, Pa. A drum was then designed which could be used on the Eickhoff shearer, Model EW170-L, being used on this longwall and which would utilize the following spray systems: 1. One spray nozzle located in front of each cutter bit with the jet directed at the cutting surface. 2. One spray nozzle located in back of each cutter bit with the jet directed at the back of the bit. 3. Standard Eickhoff nozzles located in a header along the drum scrolls. 4. A fixed header mounted on the shearer directly behind the drum to simulate the spray system originally used on the Eickhoff shearer.

Jan 1, 1976

By Avery H. Reed

RECORD production of crude petroleum, lime, crushed marble, and talc highlighted the mineral industry of Alabama in 1963. Among the States, Alabama ranked second in the production of bauxite, third in the production of scrap mica and native asphalt, and fifth in iron ore. The mineral industry of Alabama was dominated by mining and processing coal and stone, the manufacture of cement, and the production of crude petroleum, which together comprised 86 percent of the total value of production, compared with 82 percent in 1962. The iron-ore industry continued to decline; in 1959 the value of iron ore produced was 12 percent of the total State production value; in 1960, 11 percent; in 1961, 10 percent; in 1962t 8 percent; and in 1963, 5 percent.

Jan 1, 1964

By J. M. WADSWORTH

The purpose of this bulletin is to describe the methods of constructing and operating representative types of plants in the United States used for removing the light hydrocarbons from petroleum by continuous distillation, such plants being commonly known in the trade as topping or skimming plants. In the discussion of each plant an endeavor has been made to arrange the text similarly in order to facilitate comparison and to emphasize the important features. The various experimental values for the specific and the latent heats of the oils apply approximately to the oil treated. Careful experiments with each oil and its commercial fractions were not justifiable in view of the purpose of this report. It is regretted that limitations for recording data at the different plants made impossible the determination of a heat balance for each, which would have provided an equitable method of comparing efficiencies. The writer has confined himself to a comparison of the relative efficiencies of the distilling apparatus alone by the following method: Effi . f till d tt" _ Heat theoretically required. ciency 0 SIS an se mgs - Heat content of fuel consumed. The plants described are all in California where the topping industry has had its growth accentuated by the character and the use of the oil handled. The scarcity of suitable coal made the adoption of other fuel necessary, and the heavy oil of California supplied the need. To raise the flash point and to dehydrate this oil, various plants have been developed. However, the topping industry is represented in other fields; the Roxana Petroleum Co. of Cushing, Okla., and the Warner-Quinlan Asphalt Co. of New Jersey, are operating Trumble plants, and Texas and Oklahoma operators have been experimenting with different pipe retorts for continuous running. In addition to the reasons for topping cited above, in California topping has other purposes which give the plants practically a universal field in the oil industry. These additional purposes are (1) to remove the lighter constituents of the oil prior to storage for a long period, thus reducing the losses from evaporation, (2) to dehydrate and clean the oil, and (3) in conjunction with a complete refinery, to remove the lighter fractions cheaply and quickly, leaving a residue to be rerun for lubricants, coke, and other products. The reader in studying a plant for possible adaption to his own use should note that local considerations enter into the design and size of a plant. Several questions present themselves, as follows: 1. What type is suitable for the oil? 2. How much money is available for construction? 3. Will the volume of residuum be large enough for heat exchange with the crude? 4. Can the heat content of the vapors be used to reduce the cooling-water requirements? 5. What method will best recover the heat from stack gases? 6. Are the various pieces of apparatus adequate in size and best adapted to their purpose? 7. Is every possible provision made for the recovery of waste heat? 8. What products will be made, and what volume of each? 9. Is there provision for the recovery of light vapors? 10. Will the saving of fuel justify the capital and maintenance charges on the regenerative apparatus contemplated? It is regretted that information concerning the operation of topping plants with eastern and Middle West oils is not available. The writer carefully canvassed the Middle West, but did not find a plant where operation had progressed beyond the early experimental stages and reliable figures could be furnished. The reader will find fuel economy and heat recovery emphasized throughout the descriptions. The conservation of the available petroleum supply is of the utmost importance, and the Bureau of Mines presents this paper to encourage the hearty cooperation of operators to that end. The Baume gravity scale used throughout the report is that of Tagliabue with a modulus of 141.5 for conversion to specific gravity.

Jan 1, 1919

By R. F. Zaffarano

Intergrated energy balances and energy flows were constructed and quantified for State, regional, and national levels from four separate supply and demand commodity balances for coal, dry natural gas, petroleum and natural gas liquids, and utility electricity. These commodity balances were integrated by source and sectors through conversion and aggregation of their components to energy equivalents expressed in British thermal units (Btu). A summarization of the total gross energy components of supply and demand for commercial energy derived from direct fuels, hydropower and nuclear power, based on individual States and regions, is tabulated for 1960 and 1965. Pertinent computerization details and more than 500 individual State and regional printout tables, in both original commodity units and Btu's, are shown. Using these data, energy flows between States and regions were calculated to identify surplus and deficit energy areas. Report emphasis is on the conceptual aspects of integrated energy balances, rather than on the development of missing State energy data.

Jan 1, 1969

By Gary L. Hundley

The Bureau of Mines has devised and demonstrated a process for recovering Ni and Co from low-grade domestic laterites. The process consists of four major steps: (1) reduction roast, (2) ammoniacal leach, (3) solvent extraction, and (4) electrowinning. Several solid-liquid separation steps are required that affect the economics of the overall pro-cess. In this study, two techniques for solid-liquid separation, centrifugation and thickening, were investigated. This report presents the results of (1) laboratory and pilot plant studies to determine parameters for sizing centrifuges and thickeners and (2) an economic study of the two techniques, based on the requirements of a commercial-size (5,OOO-tpd) laterite processing plant. Sizing and other equipment-related recommendations, based on data from the Bureau's studies, were obtained from commercial manufacturers. The costs of thickening and centrifugation, including all the unit operations affected, were determined by the Bureau's process evaluation group. The total operating costs ~or separation using the two techniques (including depreciation on the capital cost of equipment) were found to be quite close: $17.26 per ton of laterite for centrifugation and $18.15 per ton of laterite for thickening. For centrifugal separation, the greatest cost was found to be the initial capital cost for the separation equipment; using thickeners, the greatest cost was for re-agent recovery.

Jan 1, 1984

By Frank A. Peters

The Bayer process treating Jamaican bauxite was evaluated from an economic standpoint, using standard estimating methods and published data, to present a reference point for cost estimates for nonbauxite alumina processes. The estimated operating cost for a plant producing 1,000 tons of alumina a day is $47.96 per ton of alumina when charging $8 per ton for bauxite and $2.30 per hour for direct labor. The estimated fixed capital cost is $46 million.

Jan 1, 1966