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By Harold M. Smith

The data in this report were prepared to show how Bureau of Mines routine crude oil analyses could be used to evaluate crude oils in terms of common commercial products . The use of Bureau of Mines routine analyses to determine hydrocarbon - type relationships for the gasoline and gas - oil fractions is demonstrated . For this purpose the correlation index , the aromatic profile and the naphthene profile are used to establish reasonably acceptable values for hydrocarbontype relationships . The derivation and meaning of these indications are discussed . These analytical interpretations are applied to a group of high - sulfur crude oils from the Near East , the Permian basin of West Texas , Venezuela , Colombia , California , and other locations , and the resultant data for gasoline , gas oils , lubricating oils , and asphalt are compared by appropriate tables and graphs . Because the Near East crude oils contain higher quantities of paraffins in the gasoline and gas oil ranges , they will yield good , lowsolvency solvents and good kerosine , jet fuel , and diesel fuels , but straightrun gasoline of inferior quality compared to similar products from either West Texas or Venezuelan high - sulfur oils . The Near East oils also should be good sources of lubricating stock . However , when used as stock for catalytic cracking or reforming , the Near East oils suffer by comparison because they are deficient in naphthenes .

Jan 1, 1964

By William R. Wayment, David E. Nicholson

A modified percolation - rate test is proposed for use in determining flow rates through hydraulic backfill ; in contrast to the conventional test , a percolation- rate versus void - ratio relationship is established . requirements and a detailed test procedure are described . Equipment Results of a conventional test are compared with those of the proposed modified test . The proposed modified test method yields more accurate , realistic , and usable percolation- rate ( permeability ) data . The significance of obtaining accurate percolation rates for use in analyzing waterflow through hydraulic backfill is discussed .

Jan 1, 1964

By Henry M. Harris, John E. Kelley, Thomas D. Roberts

A penetrometer apparatus for measuring viscosity of glass at temperatures up to 1,450 ° C was developed for use in establishing the viscosity coefficients required for high- temperature forming of ceramic materials . The major advantage of the method is that it can be used with samples of almost any shape or size without the necessity of forming or measuring shapes to close dimensional tolerances . Also , it has proved accurate in the range of 106 to 109 poises , a gap between the normal limits of other methods . The device , which operates on a single penetrometer principle , was used to determine the absolute viscosity coefficient of substances in centimeter - gram- second units of poises instead of relative penetration - rate units as with other penetrometers . Penetration of the viscous sample was sensed with a linear , variable differential transformer . The output of this transformer was recorded versus time , and the penetration rate was used in calculating the viscosity coefficient . The general equation relating penetration rate and viscosity coefficient was found to be 11 = F ( ln L/a 0.72 ) 2 π UL · where is the viscosity coefficient in poises , F is the penetrator load in dynes , L is the penetration depth in centimeters, a is the penetrator radius in centimeters and U is the penetration rate in centimeters per second . The penetrometer was tested using a standard viscosity sample of sodalime - silica glass obtained from the National Bureau of Standards ( NBS ) . Values obtained at several temperatures all agreed within 10 percent with comparable data calculated from the Fulcher equation derived by NBS for this glass . Equivalent accuracy was obtained with other glasses used to evaluate the apparatus .

Jan 1, 1964

By A. E. Schwaneke

Plans and specifications are given for constructing a quartz composite oscillator designed to measure internal friction in metals and alloys . The characteristics of the system are listed , and detailed procedures for its operation are explained . Typical measurements on manganese - copper alloy , on single - crystal magnesium , and on polycrystalline magnesium are shown to illustrate applications of the system .

Jan 1, 1964

By John Nagy, Henry G. Dorsett, Murray Jacobson

Laboratory studies show that ignition of a dispersed combustible dust in an open vessel may be prevented by adequate inerting . Factors affecting the inerting requirements are -- dust concentration , spark energy , ignition temperature , composition of the substances used for inerting , fineness of dust and type of combustible . The oxygen concentration of the atmosphere and in some instances the proportion of admixed inert powder and moisture required to prevent ignition are given for 367 dust samples . Variations in inerting requirements with strength of igniting source are discussed .

Jan 1, 1964

By W. P. Haynes, J. W. Mulvihill, G. B. Taylor, S. Katell

Capital and operating costs have been estimated for separating methane and hydrogen in gas - separating plants designed to produce 90 million scf per day of product gas containing a minimum of 90 percent methane . After a preliminary literature review of various separation techniques , three different processes --moving - bed adsorption using active carbon , oil absorption , and liquefaction -- were chosen for the cost estimates . Three different methane feed gas concentrations , 5 , 20 , and 50 percent ( cases 1 , 2 , and 3 , respectively ) , were chosen as representative methane concentrations for the separation estimates . Capital and operating costs were lowest for the moving - bed adsorption process in all three cases investigated . Operating costs declined from $ 0.24 to $ 0.06 per 1,000 cu ft of product gas , and capital costs declined from $47,490,800 to $7,411,200 as the percentage of methane in the feed gas increased from 5 to 50 percent .

Jan 1, 1964

By J. H. Holden, G. R. Strimbeck, L. F. Willmott, W. R. Huff

A pilot - scale fluidized feeder was developed for continuously feeding up to 1 ton of pulverized coal per hour to a pressure gasifier . Fluidization in the 3 - foot - diameter by 34-1 / 2 - foot - high feeder is effected by two streams of inert gas , a technique called zone fluidization . A stream of inert gas through a drilled plate in the base of a central column near the bottom of the feeder fluidizes the coal . Another stream through a drilled plate in the annulus between the central column and feeder wall provides a source of semifluidized coal for the central column . Fluidized coal from the central column discharges through an extraction funnel and discharge line . Zone fluidization provided good fluidization with moderate requirement for fluidizing gas . Instruments were developed for metering and recording the flow rate of fluidized coal . A system was developed for storing , and weighing pulverized coal , and then delivering it in fluidized form at about 1 to 8 tons per hour .

Jan 1, 1964

By Henry M. Harris, George J. Carter, Karle G. Strandberg

Field and laboratory data were used to evaluate sand from 13 dune locali­ties along the Oregon coast between Fort Stevens and Coos Bay. Chemical and glass button analyses were used to classify the 65 samples into two geographic zones of decreasing iron concentration. These data and data from preliminary magnetic beneficiation tests indicated that the sands between the Umpqua River and Coos Bay contained fewer impurities and were easier to beneficiate than those from areas between Fort Stevens and the Umpqua River, In addition, the dunes in the Umpqua River-Coos Bay area are the largest along the Oregon coast and are most favorably located with respect to existing transportation facilities, A composite sample from the Rogers area on the west bank of the North Slough of Coos Bay was selected for detailed mineral dressing studies. Splits from this sample were treated by various processes including magnetic separa­tion, electrostatic separation, flotation, and acid leaching, Concentrates were evaluated in glass melting tests. Test results indicated that high intensity magnetic separation followed by acid leaching would produce a prod­uct that could be used in amber and clear container glass batches. Good glass sand concentrates were also prepared by froth flotation; however, recovery was low and reagent costs excessive.

Jan 1, 1964

By T. A. Henrie, J. D. Marchant, E. S. Shedd

Cerium metal was electrowon in a fluoride bath from cerous oxide and tapped from the cell during prolonged operation . Electrolyte constituents were CeF , BaF₂ , and LiF. Twenty- seven pounds of metal of 99.8 percent purity were produced at a rate of 3 pounds per hour and tapped from the cell . Principal impurities were molybdenum , aluminum , oxygen , and carbon . The operating parameters , such as electrode geometry , bath compositions , and oxide feed rate , were investigated . Anode reactions were found to be important factors in cell operation . Stable cerous oxide reacted more uniformly at the anode surface than ceric oxide . Electrowinning was conducted in crucible hearths consisting of both frozen electrolyte and molybdenum metal . Both materials proved satisfactory and did not react with the molten cerium . Stable cerous oxide was prepared by carbothermic reduction and used as a feed material . Cell design proved to be an important factor in continuous cell operation . Complementary to the investigations of electrowinning of cerium , the metal was purified by electrorefining in a chloride electrolyte .

Jan 1, 1964

By J. A. Ruppert, P. M. Sullivan

A study was made of filtration techniques for recovering the major part of the tin contained in iron - tin alloys known as hardhead . Special smallscale filtering apparatus and a three - stage cyclic process were developed . Eighty- seven percent of the tin contained in an alloy of 82 percent tin and 17 percent iron was recovered as pure metal by pressing at 975° C followed by a second pressing at 800 ° C and a final filtering at 250 ° C. Small amounts of Sb , Cu , and Fe impurities were removed by adding Al to the molten product and performing another filtration at 250 ° C.

Jan 1, 1964

By Wilbur I. Duvall, Thomas C. Atchison, Joseph M. Pugliese

Short cylindrical charges were detonated in drill holes in rock to determine the effect that decoupling ( defined as the ratio of the radius of the hole to the radius of the charge ) has on the strain - generating abilities of explosions in rock . The amplitude and period of the strain pulses produced in the rock were studied as a function of distance , size of charge , and decoupling . The main results of these studies were that , for a given distance and size of charge , the amplitude of the strain pulse decreases as decoupling increases and the period of the strain pulse decreases at first and then increases as decoupling increases . A simplified theory of decoupling is presented that satisfactorily explains the experimental results . The information presented makes it possible to predict the effect of decoupling on explosiongenerated strain pulses in rock and thus helps the explosives user evaluate the effect of decoupling on his blasting .

Jan 1, 1964

By James A. Wasson, Harry R. Johnson, Dean W. Boley

The Cow Run sand was cored and electrical and radioactivity surveys were made in C. E. Vandevender well 35 in the Burning Springs pool of the Burning Springs oilfield , Wirt County , W. Va . Laboratory tests , reservoir - fluid analysis , well - log interpretation , and available field data indicate that a substantial quantity of oil may be recovered from this pressure - depleted reservoir by waterflooding . Two formations erroneously believed to be the First and Second Cow Run sands were similarly evaluated in A. E. Mackintosh well 8 , Anns Run Pool , Wirt County , W. Va . , but were found unsuitable for secondary - recovery operations .

Jan 1, 1964

By Robert L. Rough, William E. Eckard

Laboratory data obtained from a Bureau of Mines rotary air core of a well near Sugar Grove , Warren County , Pa . , were instrumental in initiating hydraulic fracturing in the area to stimulate oil recovery from Glade sand oil reservoirs . This report outlines the general geology , lease development , reservoir- rock characteristics , and oil - production history of Glade and Clarendon sand reservoirs in Warren County . The methods of well completion for single- stage and multiple- stage hydraulic fracturing of old and new wells are discussed , and a range of hydraulic fracture treatment data from 29 Glade sand and 10 Clarendon sand wells is presented . A composite decline curve representing oil - production data from six wells shows probable results of hydraulic fracturing . Average cumulative oil production during the first 100 days after hydraulic fracturing with a sand - carrying liquid is compared with production after conventional shooting with liquid nitroglycerin .

Jan 1, 1964

By B. H. Eccleston, R. F. Kendall, D. E. Hirsch, Norman G. Foster

The mass spectra of 23 alkylthiophenes are presented , including 21 that have not been previously reported . Correlations between mass spectra and the structure of the thiophene homologs are discussed . Comparisons with , and corroboration of , earlier workers ' correlations and predictions are made . Several additional correlations are reported to enable the spectroscopist to identify the substituents on alkyl - substituted thiophenes , and the relationship of the mono - substituted and 2,5 - disubstituted alkylthiophenes is discussed in detail .

Jan 1, 1964

By R. E. Lindstrom, D. J. Bauer

Studies were conducted to assess the potential of naphthenic acid as a fractional extractant for rare- earth mixtures and yttrium in sulfate solution . Naphthenic acid was an effective extractant , and separation factors were favorable in the presence of aqueous phase chelating agents . Addition of EDTA to the naphthenic acid extraction system resulted in average separation factors of 2.2 between adjacent yttrium- group elements , whereas DTPA resulted in average separation factors of 3.5 between adjacent cerium- group elements . EDTA was of value in separating yttrium from the rare- earth elements . Thorium and uranium were preferentially extracted over the trivalent rare- earth elements by naphthenic acid .

Jan 1, 1964

By John Nagy, Austin R. Cooper, Murray Jacobson

Data obtained in the Bureau's study of dust explosions of 313 elemental metals , alloys , catalysts , and ores comprising 54 types of material are summarized . Information is given on ignition temperature , spark energy for ignition , minimum explosion concentration , explosion pressure , rate of pressure rise , and in some instances , the admixed inert dust and oxygen concentration in an atmosphere required to prevent ignition of dust dispersions . The effects of particle diameter on explosibility and pyrophoricity are also discussed .

Jan 1, 1964

By M. H. Stanczyk, I. L. Feld

Dewatering of typical Florida phosphate rock slime by electro - osmotic techniques was investigated to determine if a compacted , plastic solid product could be obtained with simultaneous recovery of the water for re - use . Tests with porous cathodes and rod - type anodes imbedded in dilute slime charges of up to 4 tons in weight showed that the slime could be dewatered to about 35 percent solids . The dewatered products had the consistency of modeling clay . In the large - scale tests using 2.5 - foot electrode spacings , about 21 kilowatthours of power were consumed per ton of water removed in thickening the slime from 17 to 25 percent solids , but the rate of water removal was so slow that the process was not considered commercially feasible . Other tests made with electrode spacings of from 2.5 to 8 feet showed that more rapid dewatering could be obtained but that the power required was excessive . However , for special uses such as stabilizing slime pond dikes where the cost of dewatering might not be a prime requisite , high voltages could be used to rapidly remove the water . Tests of 400 - pound slime charges using a combination of electroosmosis and vacuum filtration showed that the rate of dewatering could be expedited . The average power required to thicken a ton of slime from 15 to 35 percent solids was 5 and 50 kilowatt - hours when operating the electroosmotic filtration cell at potentials of 20 and 100 volts , respectively . calculated filtration area of about 10 square feet per ton of slime treated per day was required to thicken the slime from 15 to 35 percent solids .

Jan 1, 1964

By J. H. Holden, C. C. Shale, G. R. Strimbeck, W. S. Bowie

Electrical characteristics of positive corona are presented for air in a 2 - in - diam electrostatic precipitator operating under dynamic conditions at temperatures of 600 ° to 1,500 ° F and pressures of 0 to 80 psig . Results show that current - voltage relationships depend solely on air density . Comparison of data on positive corona with previously published data on negative corona demonstrates a higher sparkover voltage and a wider range of operability for positive corona at temperatures above 375 ° F. The possibility of achieving higher voltages with positive polarity as indicated by these experiments implies several advantages for the use of positive corona in precipitators to allow better removal of suspended material from hot gases . Based on the physics of an ion in an electrical field , a theoretical equation is derived to define current - voltage characteristics of positive corona in terms of air density . Constants for the equation are evaluated from Calculated current - voltage values at different air densities agree reasonably well with experimental data .

Jan 1, 1964

By F. D. Everett

Thermoelectric and metal alloying applications have changed the status of tellurium from oversupply to under supply . In a search for new sources of this element in Arizona , Colorado , New Mexico , Utah , and neighboring states , the Bureau of Mines analyzed more than 200 samples and obtained the results of tellurium determinations by private companies on more than 500 samples from a wide variety of mineral - bearing deposits . The About 40 minerals containing tellurium have been reported , mainly tellu- rides of gold , silver , bismuth , mercury , lead , copper , iron , and nickel . minerals usually occur in small quantities and identification in ores is extremely difficult . Samples containing more than 0.1 percent tellurium were taken from the Hilltop and Memphis properties in Dona Ana County , N. Mex . , and the Silver King property in White Pine County , Nev . , where development was chiefly for base metals . The Lone Pine mine in Catron County , N. Mex . , and the Bambolla mine near Moctezuma , Sonora , Mexico are potential sources of native tellurium occurring in small but high- grade pods . Much of the production of tellurium has come as a byproduct of electro- lytic refining of copper and lead- zinc ores in Arizona , Colorado , New Mexico , and Utah . Base -metal ore deposits will continue to be the most important pri- mary source of tellurium , although the concentration in ores is nearly always less than 10 parts per million . Any significant increase in output of tellu- rium probably will be related to production and improved efficiency in smelt- ing and refining base - metal ores .

Jan 1, 1964

By J. B. Zink, M. J. Peterson

A semiquantitative spectrochemical method was developed and applied to the analysis of ash of U.S. coals . A low- temperature ashing procedure was used to minimize the loss of volatile elements . The analytical procedure provides for the estimation of 68 elements including major , minor , and trace constituents . Standards for the trace elements were prepared in a synthetic base mixture that approximates the average composition of U.S. coal ashes . Excitation was achieved with a d- c arc , spectra were recorded photographically , and interpretation was made by visual comparison of spectra of unknowns with spectra of graded standards series . Thirty- six trace elements were found in the analysis of 900 samples . Details of the procedure are presented , including sample and standards preparation , excitation and exposure conditions , spectral lines used , and approximate limits of detectability .

Jan 1, 1964