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By C. Flores

The direct cementation of copper from a loaded D2EHPA 20 % vol. in kerosene using zinc, zinc-lead alloy and iron metallic powders was studied. Copper was loaded into the organic solvent from an aqueous copper sulfate solution. Results indicated that copper is reduced spontaneously with relatively fast reaction rates. The effects of several operating parameters such as water content in the organic system, initial copper concentration, reductant surface area, oxygen and nitrogen atmosphere, intensity of the agitation and temperature on the galvanic stripping of copper were studied. For a better understanding of the electrochemical reactions involved in the galvanic stripping, the dissolution of metallic copper in the organic solvent was also studied. Copper did not dissolve unless a small amount of water was present in the organic system. The results and possible reaction mechanisms are discussed.

Jan 1, 1999

By Nord L. Gale

Lead, zinc, copper, silver, cadmium and many other heavy metals which are potentially hazardous if released into the environment in wastewater discharges have been of considerable concern to governmental agencies, industry and the general public. In response to this concern, an interdisciplinary research team at the University of Missouri has been funded by the National Science Foundation-RANN program to study trace contaminants associated with the production of lead for the past eight years. Seven modern mines in close proximity to two lead smelters in the forested Ozarks of Southeast Missouri are the largest source of lead in the world and in 1976 alone produced 504,095 short tons of lead, 82% of the United States total production. This new and rapid industrial development in a sparsely populated. rural forest region has offered a unique opportunity for studying the impact of trace metals and for developing improved techniques to control detrimental effects. Research on the wastewater discharges and two methods of biological and recycle control are discussed in this paper. Although the two mine-mill complexes investigated in this study have many similarities, the differences between the two are substantive and warrant separate examination.

Jan 1, 1977

By Michael G. Li

Prediction of acid rock drainage (ARD) for low-sulphide, low-neutralisation potential (LSLNP) mine wastes is methodologically different from that for normal sulphidic mining wastes. In this paper. LSLNP wastes are conveniently defined as those with S2 < 1% and ABA-NP2 < 20 kg CaCO3 eq/t. The distinctiveness of ARD prediction for LSLNP materials originates from their frequently low oxidation rates and is mainly attributable to two reasons. First, the utilisation efficiency of available carbonate neutralisation potential (CNP2) rapidly deteriorates when the sulphide oxidation rate per unit mass of waste drops below a certain level. Reducing the flushing rate of a waste has the same effect as increasing the oxidation rate. Second, silicate neutralisation becomes increasingly important as oxidation rates diminish, and can no longer be ignored in LSLNP materials as it often is for normal sulphidic mine wastes. In this paper, the effects of oxidation rate, pore gas CO2 partial pressure, and flushing rate on ARD prediction for LSLNP materials are theoretically demonstrated with the help of modelling using the computer program MINTEQA2. A new methodology for ARD prediction for LSLNP materials is presented in terms of a prediction procedure. Finally, a case study is given to validate some of theoretical aspects discussed and to illustrate the use of the newly proposed ARD prediction procedure.

Jan 1, 2000

By Short KC

The Hunter Region, with a major part of the coal resources of New South Wales and a long history of coal mining, has experienced a rapid expansion of coal resource development in recent years. While there are inevitable conflicts between mining, urban development and related infrastructure, and between mining and other resources, the application of sound planning practices, and improved co-operation and co-ordination among the various parties, helps to reduce such conflicts. The planning process involves consideration of factors such as transport- ation (including port facilities), mine subsidence, provision for surface facilities, a,iC the need for buffer &apos;ones. In addition, provision must be made for urban expansion, often co-existing or in close proximity to present or future coal mining development. Approval of coal mining developments takes place within the legislative framework of the Environmental Planning and Assessment Act, 1979 (EPA Act), the Coal Mining Act, 1973 (CM Act) and the Mining Act, 1973. Considerable effort has gone into stream- lining and co-ordinating the procedures under these Acts. The EPA Act provides for regional and local environmental plans, as well as a linked process of development control and environmental impact assessment. The CM Act provides for the grant of exploration and coal mining titles and mechanisms for the responsible management of Mining.

Jan 1, 1987

MR. GERALD ALLEY (C 11 i e f Draftsman, C. F. & I. Co.) : This invention is primarily intended to correct anything that goes wrong with the fan and any conditions in your air current underground which do not produce a change in your fan water gauge

Jan 1, 1925

The development and distribution of gold placers in Otago û Southland is related primarily to the evolution and architecture of three distinctly different drainage networks that developed during and since Gondwana breakup: +&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp; Late-Gondwana û Pre-marine; +&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp; Middle Tertiary Post-marine; and +&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp;&nbsp; Modern. Late Gondwana û Pre-marine drainage was dominantly recti-linear and controlled by normal faults and sedimentary basins formed before or during Gondwana breakup. Placers formed dominantly in 2nd order transverse drainages with primary sources in their catchments. This drainage network was progressively destroyed by inundation and burial by marine strata during Late Cretaceous û Middle Tertiary marine transgression that ultimately covered most of New Zealand. Middle Tertiary Post-marine drainage evolved on and incised the newly emergent low-relief landscape during regional marine regression driven by development of the present plate boundary through South Island. Most of Central Otago was drained into Southland and to the southern coast via a large braided river system with an extensive network of tributaries in its Central Otago reach. East Otago was drained by several smaller systems. Placers formed dominantly in proximal and medial reaches of 1st and 2nd order drainages with primary or pre-existing placers in their catchments. This drainage network was destroyed by inundation and burial of the Central Otago reach of the major system by lacustrine strata following tectonic damning of its middle reach by range uplift and development of a lake complex that covered &gt;5000km2 of Central Otago. The Modern drainage network evolved from the Middle Tertiary network through complex response, firstly to uplift of NW-trending and NE-trending ranges throughout the region since the Late Miocene, and secondly to the effects of major Pleistocene glacial advances in West Otago. Placers formed in alluvial fans at range margins, proximal and medial pre-glacial fluvial systems and glacial outwash sequences. Evolution of each of these drainage networks has been accompanied by widespread sedimentary recycling of alluvial gold from older to younger placers, augmented locally by input of first-cycle gold derived from erosion of primary sources in the repeatedly exhumed basement rocks.

Jan 1, 2006

By F. F. Roberto

Sulfuric acid has been demonstrated to be an efficient lixiviant for in situ extraction of copper in the past. It has also been proposed that microbial production (by iron-oxidizing acidophilic bacteria) of acidic ferric solution either in situ or ex situ could provide an economic strategy to generate an effective lixiviant for secondary copper sulfides like chalcocite and covellite. Copper heap bioleaching also takes advantage of this approach. One of the major environmental challenges for in situ copper recovery projects is the containment of acidic solution within the ore deposit, and ultimate restoration of the depleted ore body to its original state. A perhaps overlooked aspect of projected site operations is the possibility that transient acidic conditions and pumping of solutions from surface reservoirs into the subsurface could stimulate the growth of iron- or sulfur-oxidizing species of acidophilic microbes in the ore body, leading to additional generation of sulfate, acid, and ferric iron. This outcome would benefit extraction of copper in mixed oxide/sulfide deposits in the near term, but could complicate restoration activities. Possible impacts of pumping acidic solutions into the subsurface on microbes resident in, or introduced into the extraction zone will be discussed in the context of our understanding of copper heap bioleaching and acid rock drainage. INTRODUCTION As high-grade deposits of metals such as copper continue to decline, conventional mining methods have evolved to mine and process larger and larger quantities of ore. What is currently defined as ore today often contains less metal than the tailings of past operations. The throughput of current-day mines also leads to tremendous amounts of waste rock and tailings that may threaten the environment and communities around the mines, as has recently been experienced by 3 major tailings disposal facility (TSF) dam failures in the past 5 years. Community acceptance of large mine operations thus becomes more difficult to achieve—loss of the social license to operate. In response, the mining industry urgently pursues innovations that can fundamentally change the way in which metals are mined. In situ recovery (ISR) of metals represents one approach to a more sustainable mining industry, by virtually eliminating the need for a pit or underground excavation, eliminating the excavation and transportation of ore to a process plant and the ensuing noise and dust that is generated, and any need for waste rock dumps or TSFs. An ISR mine could have very little visible footprint beyond a network of wells, pumps, and piping to transport pregnant solution to a recovery facility, such as a solvent extraction- electrowinning (SX-EW) plant for copper. Some solid waste streams and/or storage ponds may still be necessary to treat and store bleed streams, PLS and raffinate, or as part of groundwater restoration activities. Thus capital and operating investments would be potentially much lower than that required for a conventional mine. In theory production could also be controlled to adjust to subsurface ore grade and match market demand. A not insignificant challenge of in situ recovery is the requirement for an efficient, low-toxicity, and ideally selective lixiviant for the metal that is targeted.

Jan 1, 2019

By Loren R. Anderson

This is an Appendix of Volume I. It contains the results of the electric cone penetrometer soundings from the first phase of the testing program.

Jan 1, 1982

By Robert D. Schmidt

This Bureau of Mines report describes the development and application of a computer model for simulating the hydrological activity associated with in situ leaching. The model is intended to provide uranium resource developers with a description of the flow behavior of leachants and ground water during the development, production, and restoration phases of a leaching operation involving an arbitrary pattern of injection and recovery wells. Different aquifer environments are modeled, using a closed-form solution to the partial differential equation that describes three-dimensional changes in piezometric head as a result of pumping from leachant injection and recovery wells. The computer program can model a maximum of, 50 arbitarily located wells. Numerical techniques involving difference quotients and Taylor expansions about time points are used to derive time, velocity, areal sweep, and fluid volume parameters associated with leaching hydraulics. These parameters are output by the program in graphic and tabular formats. Other numeric methods insure that the program running time is minimized without significantly affect-ing the accuracy of results.

Jan 1, 1980

By Michael W. Neill, O&apos

This presentation addresses some of the problems encountered in estimating the capacity of drilled shafts and augered, cast-in-place piles in soft rock. Methods to quantify side and base resistance are suggested. However, the methods that are described should always be verified locally by performing load tests.

Jan 1, 2001

Within the Business Process Improvement Program initiated at Placer Dome during 2003 was the Business Performance Management Project (BPM).BPMÆ s aim has been to extract productivity improvements from individual business units by providing a model for implementing leading practice based management process within the Placer Dome Group, sharing management best practice, injecting new management techniques and instilling a continuous improvement culture. The installation of an underground dispatch system has been a key component of the BPM project at Osborne Mine.Information capture and analysis allows for corrective action to be planned and executed before there is a material impact on the performance of a business unit. This paper briefly describes the principles and practices of effective business performance management, the four processes of a management operating system namely; strategic and tactical planning, implementation and reporting. The identification of business drivers, their measures and associated key performance indicators is discussed. The benefits of an underground dispatch system at Osborne with respect to safety, production and maintenance is described along with the installation process within the mining department that included its configuration, resourcing and roll out.

Jan 1, 2005

By Thomas Foster

One of the most dreaded things which mining men sometimes have to contend with is underground mine fires, which are both dangerous and expensive. In the Reliance mines we have had considerable trouble with mine fires. We have at the present time five different fire zones, three of these zones give us considerable trouble and the other two have not given any trouble since they have been walled off. Fire Zone No. 1 comprises No. 2, 3 and 4 South Entries, about 50 acres are enclosed in this zone. Fire Zone No. 2 comprises the main drift entry from the mouth to the Old Boundary Plane and extends to the crop line, about 10 acres are enclosed in this zone. Fire Zone No. 3 comprises 1 and 2 North Entries from the main slope to the Old Boundary Plane, a distance of about 1,200 feet, about 15 acres are enclosed in this zone. Fire Zone No. 4 comprises 11/2 and 2 North Entries, a distance of 1,100 feet between New Slope and Old Boundary Plane, about 15 acres are enclosed in this zone. Fire Zone No. 5 comprises the inside end of No. 11/2 and 2 North Entries and 3 North Entry from the New Slope to 30 room, a distance of about 2,600 feet along No. 3 North Entry, about 20 acres are enclosed in this zone. The first mine fire started in No. 2 South Entry in No. 1 zone in 1914. Inside of No. 7 room on the high side of the entry, there was a soft piece of coal. There were no rooms driven in this coal and one day a fire was discovered in the solid pillar on the high side of the entry, work was started at once to load out this fire. and several places was driven into the pillar and cribs built where the coal was taken out, but this method proved a failure and a sand pack was put up along the entry between the track and the high rib. This consisted of timber set about 3 feet from the rib and 2-inch boards put behind the timber and sand or adobe put in between the boards and the ribs, and this method gave very good results except that it required close watching as the sand would settle and let the smoke out between the roof and the sand. Fire broke out in No. 3 South Entry in No. 1 zone in the summer of 1919. We sealed this fire off by building 36 fire stoppings, which also enclosed the fire in No. 2 South Entry and we have never had any trouble with fires in this zone since it was walled off. The fire started in No. 2 -zone in 1919 and has been very active ever since. When this fire was first discovered we built new stoppings in front of the old one in the room necks; we also opened up some of the room necks and loaded out part of the burning coal and rock but this did not help any, the fire, would burn out around the stoppings also burn along the roof between the top coal and the roof sometimes nearly across the entry. Several holes were drilled from the surface to the fire area and flushing the fire was tried but this was also a:\, failure, the rock above the coal was so hot that the mud would dry in the hole and fill it. In 1921 we started to take down the top coal along this entry, timber the entry and put 2-inch boards behind the timber and fill in between the coal and the boards with sand or adobe. We have at present over 1,000 feet of this work done and it has given us better results than any other method that we have tried. As the coal burns out behind the timber the weight breaks the timber and it is necessary to renew some of it. Fire broke out in No. 1 North Entry in No. 3 zone in 1922. There was a stopping in this entry that had been put in when the entry was finished some few years before. The fire burned around the stopping on the low rib of the entry, we built another stopping in front of the old one taking down the top coal and extending it up to the roof also digging in both ribs and setting the stoppings into the coal about 18 inches. This fire did not cause any trouble until June, 1924, when we discovered this fire was very active on the inside

Jan 1, 1924

By M. M. C Jiménez, J. A. S Ténorio

For the recovery of valuable materials and for the protection of environment, recycling process of printed circuit board is an important subject of study. Moreover, the popularization of the computers and its technological evolution has generated a large number of waste electrical and electronic equipment. This paper presents a study of synergistic solvent extraction of copper, nickel and zinc from a sulfuric leaching liquor of printed circuit boards (PCB’s). The percent extraction of copper, nickel and zinc from dilute aqueous sulfate media besides synergistic effect of mixture of the .extractants Cyanex 272 and D2EHPA have been studied. Furthermore, different conditions such as temperature, pH of the feed solution have been examined. The results suggest that the synergistic effect of the .extractants mixture enhance the extraction efficiency of nickel.

Jan 1, 2014

By Georges Ranque

THIS paper by. Georges Ranque is an attempt to reason out the conditions of formation and stability of inclusions and to establish an operative process capable of eliminating or minimizing them. The paper consists of two parts; one in which the author considers the laws of physical chemistry and physics that apply to liquid slag-metal systems and one in which he describes a practice based on the theoretical considerations. Such a paper is bound to contain controversial points and it is therefore your speaker&apos;s intention to present Mr. Ranque&apos;s side of the picture to the best of his ability without regard for any thoughts or criticisms of his own. RISING VELOCITIES OF INCLUSIONS Most nonmetallic inclusions have densities ranging from about 1.7 to s, while liquid steel has a density of about 7. Under these conditions, ferrostatic pressure should cause the inclusions, being lighter, to rise from the bath and be eliminated. This rising tendency is expressed by Stokes&apos; law, from which may be calculated the rising velocity of a spherical particle in a liquid medium whose density and viscosity are known.

Jan 1, 1947

By Maxwell Pereira Cangani

Com a expansão da produção de minério de ferro no quadrilátero ferrífero em Minas Gerais, a litologia e o perfil de qualidade dos minérios foram alterados significativamente nos últimos anos, para o minério recebido na Ternium Brasil notadamente a partir do segundo semestre de 2014, gerando forte impacto sobre os processos Sinterização e Altos Fornos. Houve uma redução da participação de minérios hematíticos e uma elevação de minérios itabiríticos. Como conseqüência, houve uma elevação significativa dos teores de sílica, fósforo e alumina no sinter feed e minério granulado. Nesse contexto, surgiu a necessidade de tornar a especificação do sínter produto mais abrangente qualitativamente e mais restritiva do ponto de vista quantitativo, com o objetivo de melhorar a performance e estabilidade dos Altos Fornos, frente ao novo perfil de qualidade dos minérios de ferro.

Oct 30, 2017

By M. B. Bever, A. B. Michael

The solidification of aluminum-rich aluminum-copper alloys was investigated for different solidification rates. The measured amounts of nonequilibrium eutectic were compared with the amounts calculated on the assumption of no diffusion in the solid. The morphology of the eutectic was studied and dendritic spacings were measured. Compositions of the cored primary solid solutions were determined by quantitative autoradiography after activation of the solute copper by neutron irradiation. CONSIDERABLE progress has been made in recent years toward an understanding of the solidification of metals. This is especially true for the factors involved in nucleation, the controlled growth of metal crystals from melts, and various aspects of the freezing of ingots and castings. Many features of the solidification process, however, are not understood adequately and much further work is required. In the research reported here the solidification of a series of aluminum-rich aluminum-copper alloys was investigated. Different degrees of deviation from the idealized case of equilibrium solidification were attained by varying the rate of solidification. Thermal analysis and microscopic examination were supplemented by lineal analysis and autoradiography. The latter required the use of radioactive tracers and was adapted to the quantitative determination on a microscale of concentrations of copper dissolved in aluminum. The tracers were produced in situ by activating the copper with neutrons. These techniques permitted a correlated interpretation of the temperature-time history, the amounts of nonequilibrium eutectic and the general morphology of the alloys, and yielded quantitative data on microsegregation. Nonequilibrium Solidification In the general case of the solidification of a solid solution in accordance with the phase diagram, the composition of the coexisting liquid and solid must change continuously. This change requires diffusion, which at best remains incomplete in the solid during solidification. The resulting inhomogeneity of the solid solution crystals is well-known as coring, dendritic segregation, or microsegregation. The generally accepted analysis of coring assumes that, 1—no diffusion occurs in the solid, 2—diffusion is complete in the liquid, and 3—the composition of the solid formed on cooling through any infinitesimal temperature interval is given by the solidus of the phase diagram. On this basis, In this equation m designates mass, x designates the concentration of solute and the subscripts L and S refer to the liquid and solid phases, respectively; the subscript o indicates the initial state, in which the liquid is identical with the entire system. Eq. 1 or its equivalent has been derived repeatedly&apos;-7 and an analogous equation, known as Rayleigh&apos;s equation, has been used for distillation. The assumptions on which Eq. 1 is based do not include an infinitely fast cooling rate as sometimes stated. In fact, Olsen and Hultgren %ave shown by experiment that very high solidification rates suppress coring, presumably by preventing diffusion in the liquid and by the effect undercooling has on the composition of the nucleus. Coring thus occurs at rates of cooling which are too fast for a close approach to equilibrium in the solid and too slow to suppress diffusion in the liquid and to cause marked undercooling. If the liquidus and solidus approximate straight lines, Eq. 1 simplifies to The fraction of liquid present at any temperature during nonequilibrium solidification can be calculated from Eqs. 1 or 2. By the lever relation it is

Jan 1, 1955

By Takao Oishi, Go Ohara, Toru Kitazaki, Masahiro Tanaka

"The High Pressure Acid Leach (HPAL) plant for nickel-cobalt mixed sulphide production at Coral Bay Nickel Corporation (CBNC) in the Philippines has been in operation since 2005 with a capacity of 10,000 t/year of nickel. Subsequent to the commissioning of the second plant in 2008, the production capacity increased to 22,000 t/year of nickel (Llerin et al., 2011). CBNC’s annual nickel production reached more than 24,000 tons of nickel in 2014. The concepts to achieve this capacity are the high availability and the reciprocally flexible operation of both plants. The availability depends on some factors, such as the control of impurities in the process and the equipment condition, to mention a few. In the HPAL process, it is not only the autoclave operating conditions that affect nickel extraction but also the impurities in the ore greatly influence it. The major element in the ore is iron and most of this iron is precipitated as Fe2O3, while the rest remains as Fe2+ or Fe3+ sulphate in solution. These ions in solution reduce the availability, so it is important to control the formation of iron ions by controlling the impurities in feed ore as well as the HPAL conditions. This paper presents the general HPAL process and the behaviour of impurities, focusing on iron behaviour in the HPAL process.INTRODUCTIONCoral Bay Nickel Corporation ProfileCoral Bay Nickel Corporation (CBNC) was founded on April 2002, as a joint venture of four companies; namely, Mitsui Corporation (18%), Sojitz Corporation (18%), Nickel Asia Corporation (10%) and Sumitomo Metal Mining Corporation (SMM) with a controlling stake of 54%. Aside from its capital share, Nickel Asia Corporation also supplies the ore and limestone for the High Pressure Acid Leach (HPAL) plant located in Rio Tuba, Philippines, as shown in Figure 1 (Tsuchida, 2008). The objective of the CBNC project is to produce 22,000 t/year (original design) of nickel and 1,500 t/year of cobalt, as sulphide, by the treatment of nickel laterite ore which is a low grade nickel oxide ore in the Philippines (Mines and Geosciences Bureau, 2014). The sulphide product has been exported as a raw material to the SMM Nickel Refinery in Japan for 30 years. The product of this plant, a mixed (Ni/Co) sulphide, is shipped to the SMM’s Nickel Refinery in Niihama, Japan. SMM Corporation provides the technology and management personnel to the plant. SMM Corporation also supplies the sulphuric acid, which is the main reagent for the HPAL process."

Jan 1, 2016

By B. M. Larsen

IN spite of the great amount of operating experience and of studies directed toward elucidation of the interrelation of the several processes going on in the blast furnace, the present picture of its operation is based largely on indirect evidence and on speculation. The reason for this unsatisfactory situation is the extreme difficulty of making direct observations and significant measurements while the furnace is operating, and of translating laboratory experience to the conditions obtaining in the smelting process. Yet there are questions that can be investigated with some promise of a definitive answer; and it is the purpose of the present paper to set forth some of these questions, as a basis for discussion, which may, it is hoped, lead to active work on some of them. In order to provide a starting point for this discussion, some views held tentatively by the writer are outlined, along with a certain amount of evidence gathered from operating records and interpreted on the basis of the ideas expressed. These opinions may prove not to be pertinent, and may well not be in accord with the opinions of others; they have been included to encourage others to do likewise and on purpose to provoke informal discussion. In this way it should be possible to transcend the limitations of formal papers; to bring forth suggestions of new hypotheses or new methods of investigation; and to promote better understanding between investigators and operators in this difficult field. The statements made express the present views of one physical chemist who is not too familiar with all the difficulties of maintaining these enormous reaction vessels in reasonably smooth and economical operation; who, however, is persuaded that some of these difficulties would be less formidable if surer knowledge of the several interrelated and concurrent processes were available and made use of. For these difficulties arise largely, it is believed, from variation in conditions which the operator must meet as best be can, and should lessen as these conditions can be brought under control so that they are either made substantially constant or the variations are neutralized by compensating methods. A. VARIATION IN BURDEN AND IN MIXING OF CHARGE To the scientific investigator, who aims to control the conditions of experiment and to limit the number of variable factors, the most perplexing aspect of the blast-furnace process is that nothing seems to remain constant for long. Variations of burden seem to be unnecessarily frequent; and, even if the charge were constant from hour to hour, its constituents usually are not mixed as intimately as they might well be. It is understandable that separate layers of coke and of ore, also separate layers according to size, promote permeability and the

Jan 1, 1947

By R. D. Leitch

"INTRODUCTION This report is another of the series on the effect of drouth and low water on the pollution of streams by coalmine drainage. A previous report3 dealt with work on Bennett Branch of Sinnanahoning Creek, Pa. This report deals with the results obtained during a similar study of Black Lick Creek, Two Lick Creek, and Yellow Creek. All of these belong to the same drainage system. Two Lick Creek is a tributary to Black Lick Creek, and in turn Yellow Creek is a tributary to Two Lick Creek, as shown in Figure 1.Black Lick Creek was of such a volume that a seasonal investigation was not entirely feasible. Yellow Creek was found to have mines only near the mouth, except a few of status unknown to the writer at the extreme head-waters, and the stream was also more or less inaccessible for regular and frequent sampling. Two Lick Creek was found to be most suitable of the three.ACKNOWLEDGMENTThe work reported has been carried on under the direction and with the advice of Dr. R. R. Sayers, chief, health and safety branch, and W. P. Yant, supervising engineer, Pittsburgh Experiment Station."

Jul 1, 1931

Mr. P. F. THOMPSON said this matter was one of very great importance to producers of lead. His association with the matter was that he happened to be the Institute representative on the Committee of the Standards Association of Australia charged with formulating a standard for chemical lead, that is, lead used in technical chemistry for acid chambers and the like. The British standard had this test incorporated in it, but those on the committee felt that it should not be included in the specification. The main objection was that in an accelerated corrosion test one was endeavouring to do in a few seconds what in natural conditions would take years; and it was now being recognised that such tests were of little value in assessing the corrosive properties of a metal.The flash point test was carried out with boiling hot strong sulphuric acid; but no chemical manufacturer would be likely to use such in contact with lead. There were many factors such as the formation of steam, the chemical reduction of sulphuric acid, the evolution of hydrogen, the catalytic effect of the surface lead, affecting this test, other than the presence of the segregated impurities upon which this test throws the onus of the whole imperfection of the lead. Mr. Russell had shown that lead which had stood the test of time often gave a low flash point. They were endeavouring to find rapid methods of estimating minute amounts of the more important impurities, which would eliminate the labour and expense of a full analysis.Mr. H. St. J. SOMERSET thanked Mr. Thompson for his remarks. He supposed some of those present knew that the Broken Hill Associated Smelters was responsible for Mr. Russell&apos;s investigations at the University, and he could only agree with Mr. Thompson that the flash point test, which had been accepted at the present time...

Jan 1, 1930