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By R. E. Pennington

My subject this morning is coal liquefaction technology. Actually, coal liquefaction involves a number of technologies in a very complex system. The first slide shows the major components of such a system with arrows to indicate appropriate flows. The components are the facilities for coal feed preparation and handling; the coal hydrogenation or base liquefaction section; facilities for product separation and recovery, and in addition, facilities for the production of hydrogen from coal-based sources. A very rough break- out of the investments involved in these areas is given at the bottom of the slide. Investment is spread about equally among the three areas of operations Another way of looking at it is that the investments in what might be called support facilities are of the same magnitude as the base investment in the hydrogen facilities. Therefore, it is appropriate in a discussion of coal liquefaction technology to treat it as a system composed of a number of technologies. The next slide lists the various functions in the feed preparation section along with an indication of technology status. Storage, crushing, grinding, drying of coal all have been in commercial practice for a number of years. The slurrying and pumping of coal at least in water slurries, is practiced commercially also. The heating of coal slurries in oil to high temperatures under pressure is not in commercial practice and development and testing is going on by a number of people in this area. Some rather complex phenomena occur when coal oil slurries are heated to high temperatures.

Jan 1, 1975

By D. Jepsen

Land access and tenure certainty for exploration and mine development is absolutely critical to the foundation of a healthy, sustainable and environmentally-sound mineral exploration and mining sector. Without certainty, mineral exploration will be severely eroded, resulting in reduced possibility of discovering and developing new mines. The development of positive relationships based on a shared commitment of understanding, mutual respect and trust by First Nations and the mineral sector can provide this increased business certainty and social and economic benefits for local First Nations. As a sector, we face many challenges in regard to building relationships with First Nations. The root solution to addressing these challenges lies in recognizing and understanding the unique cultural differences that exist between indigenous people and the business community. From the Canadian perspective, the First Nations culture differs vastly from non-Aboriginal culture. It is equally as imperative that cultural differences be acknowledged and respected at home as they are when seeking business opportunities in other countries. The traditional “business” approaches and relationships that one understands and incorporates with one’s contractors, legal counsel, investors and Board are generally not be the best approach for the introductory and subsequent meetings with indigenous peoples. This paper is written from the perspective of my experiences accumulated over the past ten years, first as Manager of Aboriginal Affairs for one of the largest forest companies in British Columbia and now, as President and CEO of the Association for Mineral Exploration BC (AME BC). My opinions are not necessarily endorsed by AME BC. Before the gritty issues of consultation and benefit sharing are dealt with, it is worthwhile to clear up the confusion surrounding terminology. “Indigenous Peoples” is used in a global context; “Aboriginal Peoples” is used in the Canadian context therefore includes Métis, Inuit and First Nations Peoples. The term “First Nations”, in the context of British Columbia, perhaps has its roots in the fact that treaties have largely not been settled. Therefore it is important to reaffirm that British Columbia was not discovered. First Nations have resided in British Columbia since time immemorial.

Jan 1, 2007

The Beginning ! The status quo simply isn?t sustainable ! Our social license is at risk ! The bar keeps rising ? We must improve our performance, both operational and social ? We must improve stakeholder judgement of our industry by taking action collectively Implementing TSM " TSM Guiding Principles " Performance Indicators " Crisis communications " External Outreach " Tailings management " Energy management " Performance manuals, guides " Reporting " Communities of Interest Advisory Panel

May 1, 2004

By P. D. R. Maltby

"The Canadian Institute of Mining and Metallurgy has undertaken to host the XIV International Mineral Processing Congress to be held in Toronto at the Royal York Hotel from October 10 to 16, 1982. The theme of the Congress will be ""Worldwide Industrial Application of Mineral Processing Technology."" The program will include 10 sessions and numerous field trips to the different mining areas of Canada.For prospective authors, the preliminary program includes sessions on,1. Flotation - plant practice, equipment design, simulation, control and economics.2. Comminution - plant practice, equipment, design, simulation, control, wear, energy consideration and economics.3. Round table seminar on large grinding mills.4. Round table seminar on modern and future plant design.5. Mineral processes to recover precious metals.6. Mineral processes to recover energy minerals (coal, uranium).7. Mineral processes to recover industrial minerals.8. Round table seminar on the environment and ecology and how the different countries cope with associated problems.9. Materials handling with an emphasis on agglomeration techniques ereconentration methods, solid-liquid separation.10. Open session to deal with topic emerging from general demand."

Jan 1, 1980

By Eduardo Cabral

A introdução da tecnologia intensiva de mistura nas plantas de sinterização de minério de ferro tem sido vital nos últimos 20 anos, dado o fato do progressivo afinamento do minério e a necessidade de manter ou até diminuir os custos operacionais das sinterizações. As características intrínsecas da mistura intensiva facilitam a incorporação de finos cada vez mais presentes nas formulações promovendo sua aglomeração de forma eficiente, sem perda de produtividade e com economia de coque, água e energia por tonelada produzida.

Aug 17, 2017

By Gustavo Henrique Bolognesi Donato

Frente ao crescente número de falhas por fadiga, o projeto considerando cargas cíclicas passou a ser uma fase natural da concepção e otimização de componentes, em especial de setores de responsabilidade, como aeronáutico, automobilístico e de óleo e gás. Em geral, as avaliações se baseiam em resultados de ensaios uniaxiais que empregam máquinas universais servo-controladas de tração-compressão ou tração-tração. Entretanto, embora precisos, tais equipamentos custam centenas de milhares de dólares, apresentam elevado custo operacional e de manutenção e exigem expressivo tempo para a realização dos ensaios. Como alternativas simples e baratas existem as máquinas do tipo flexão alternada (biela-manivela), as quais podem apresentar curvas de vida à fadiga comparáveis ao caso uniaxial se os campos de deformações e tensões nas amostras forem bem conhecidos. Dessa forma, buscando avançar nesse tópico e fazendo uso de refinados modelos não lineares de elementos finitos, este artigo apresenta uma metodologia de ensaios de flexão alternada controlada por deformação (curvas e-N), assim como uma análise crítica dos resultados experimentais. Foram ensaiados um aço SAE 1008 e um alumínio 1200 H14 e, além da geometria recomendada pela ASTM B593, uma nova geometria é proposta para menor dispersão dos resultados experimentais. A metodologia desenvolvida obteve sucesso na condução dos ensaios e a geometria proposta reduziu a dispersão dos resultados para o aço SAE 1008 que apresenta elevado encruamento. As curvas e-N obtidas, além de diretamente úteis para projetos mecânicos, apoiarão comparações futuras com resultados de fadiga uniaxial dos mesmos materiais.

Aug 17, 2017

By M. C. Malamphy

A general description of the activities and results of bauxite investigation by The Bureau of Mines at its bauxite project in Saline and Pulaski Counties, Ark., has been given in Report of Investigations No. 4251. The factual data obtained during the project are reported in a series of Reports of Investigation beginning with No. 4251, of which this is the fourth. The data are accompanied by maps showing the location of holes drilled and the deposits developed. Each area upon which work was done is reported by half townships. Each bauxite deposit investigated was assigned a name and a number for ready reference and identification, and its location and name are shown on the appropriate half-township map. The description of each half township is followed by a description of each deposit developed in that half township. The 14 half-township maps and 77 detail maps of the bauxite deposits in this series of reports give the locations and numbers of all the holes drilled on the project except the deep holes drilled to test the geophysical anomalies. The locations of those holes show on Figure 13 in Volume 1. The descriptions of the deposits developed are followed by complete detailed logs of the drill holes. Many of the widely spaced exploratory holes did not discover bauxite of minable thickness and grade. The pertinent information obtained from the widely spaced exploratory drill holes has been summarized and tabulated, and a table for each half township-is given with the discussion covering that area.

Jan 1, 1948

By Luís Carlos da Silva

Atualmente, uma das principais preocupações da humanidade está relacionada à questões ambientais, que motivam pesquisas para o desenvolvimento de materiais com recursos renováveis e amigáveis com o meio ambiente. No entanto, este estudo pretende comparar, à resistência dos compósitos reforçados com fibras naturais, portanto, favoráveis ao meio ambiente e compósitos reforçados com fibras de vidro, que por sua vez têm impactos ambientais desde a fabricação até à disposição. Treze compósitos foram confeccionados para essa pesquisa, contendo 0% de fibra, 30% de fibras de curauá e 30% de fibras de vidro em matriz epóxi e testados em uma máquina de tração. Os resultados mostraram valores mais altos para as amostras reforçadas com fibras de vidro, no entanto, para relacionar a tensão do compósito com à sua densidade de fibra, verificou-se que os compósitos reforçados com fibras naturais apresentaram resultados melhores do que os produzidos com fibras de vidro. Concluindo, pelo ponto de vista da propriedade mecânica, as fibras de vidro podem ser substituídas pelas fibras de curauá.

Oct 30, 2017

By J. Fogarty, J. Sofra

The mobile telecommunications sector is one of the fastest growing industries worldwide. However, increasingly stringent environmental regulations are placing pressure on manufacturers to accept responsibility for end of life products. The companies are therefore exploring avenues to recover the valuable components contained within the mobile telecommunications devices thus reducing the quantities of toxic components going to landfill. Batteries used to power the devices, are typically based on either nickel-cadmium, nickel metal hydride, or lithium ion cells. They contain toxic metals including nickel, cadmium, lithium, potassium, lead, and cobalt in a complicated arrangement of battery cells surrounded by a metals then plastic casing. The Ausmelt Catalytic Waste Converter (CWC) for waste treatment and recycling is well suited to processing all three mobile phone battery types for the recovery of valuable metals in marketable products that can be recycled to industry without turning out harmful levels of toxic emissions. Ausmelt recently demonstrated the capabilities of its CWC by continuously processing 4.5 tonnes of nickel-cadmium batteries. Using Ausmelt's pilot plant facility in Australia, the nickel-cadmium batteries were processed to produce a nickel iron sulphide (matte), a cadmium fume and a final slag which satisfied CS toxicity leach test criteria and was safe f<~r disposal to landfill. This paper explores the commercial development of the Ausmelt CWC for treating each of the three battery types in light of (a) the outcomes of the recent demonstration, and (b) the current and expected future availability of batteries for processing.

Jan 1, 2000

[Trans. No. Place Date Vol. Page 1. Wilkes-Barre, Pa May, &apos;71.. 1 3 2. Bethlehem, I&apos;s Aug., &apos;71.. 110 3. Troy, N. Y Nov., &apos;71.. 113 4. Philadelphia, PaFeb., &apos;72.. 117 5. New York, N. YMay, &apos;72120 6. Pittsburgh, Pa Oct., &apos;72.. 125 7. Boston, MassFeb., &apos;73.. 128 8. Philadelphia, Pa.*May, &apos;73.. 23 9. Easton, PaOct., &apos;73.. 27 10. New York, N. Y Feb., &apos;74211] [ ]

Jan 1, 1925

By George T. Faust, S. R. B. Cooke

"The Southern Experiment Station of the Bureau of Mines, United States Department of the Interior, in cooperation with the University of Alabama, is investigating the preparation of pulverized coal for fuel. In this study the relative amount of surface in various products and samples had to be assessed. Because of the familiarity with screens and because of the simplicity of using the inverse ratio of the opening for ascertaining the amount of relative surface in the respective sizes, screens down to and including 270-mesh were used. This choice was made in full cognizance of the irregularity of screens, but it seemed that if the same screens were used throughout all the tests the relative values would be satisfactory.In dealing with the subsieve sizes, pneumatic elutriation was used to make several fractions to extend the sizing analysis into the range of hypothetical screens. This kind of a sizing analysis was thought necessary because it is familiar to all operators, and, furthermore, it is amenable to several ways of plotting curves that bring out the characteristics of various coals and various methods of grinding.The method of obtaining the data from which to set up the hypothetical screen scale is the subject of this paper. It consists in determining the average projected area of the particles in the respective elutriated products. By extending the ""area method"" to sieve sizes, a factor is found that may be applied to the subsieve sizes, and thus the scale is projected in a regular manner. This method avoids contentions about specific surface and steers clear of ""average diameter"" except as material sized on screens may be said to have an average diameter."

Aug 1, 1939

By James J. Jessop, Richard E. Thill, Michael J. Friedel

As part of an investigation aimed at improving the health and safety and competitiveness of the mining industry, the U.S. Bureau of Mines evaluated the application of common offset radar profiling, using a 250-MHz ground-penetrating radar (GPR) system, for the detection of fractures in igneous rock. A series of radar reflection surveys were conducted to detect and delineate the extent of fracturing at various granodiorite and gabbro quarries and outcrops located in Minnesota. The application of radar profiling for detecting joints, sheeting fractures, shear zones, and depth to water table was demonstrated to be feasible with minimal processing. Radar reflection interpretations were verified by visual inspection of the rock mass and field mapping of local structure. The radar reflection section provides a simple, rapid, and cost-effective means for mapping of shallow (less than 10 m) small-scale fractures (greater than 0.25 cm) in igneous rock masses (characteristic of velocities between 0.061 m/ns for gabbro and 0.125 m/ns for granodiorite). Depth or distance estimates to fractures are within 10 pct of the actual, and time-shift compensation is necessary only when topographic irregularities exceed 30 cm.

Jan 1, 1992

By Vernon O. Markworth

This report contains the results of tests performed on three large diesel engines to determine their ability to meet selected criteria of the Mining Enforcement and Safety Administration Regulations for equipment used in gassy, non-coal mines. Study efforts were first directed toward determining the types of equipment expected to be used in underground oil shale mines. Three typical engines in the 800-1200 horsepower range were then selected for testing. Intake flame arresters, exhaust scrubbers, and water jacketed exhaust system were designed and built for each engine. During testing, each engine was evaluated for its gaseous emissions output, adequacy of the exhaust gas cooling system, ability to withstand internal explosions, and adequacy of the flame arresters. Surface temperatures of the engine and exhaust cooling system were determined under full load operation.

Jan 1, 1978

By N. Manopulo, J. Maier, L. Tong, C. Becker, P. Hora

The contribution presents a new finite element approach in which the common updated Lagrangian formulation is replaced by a spatial flow formulation applying a special arbitrary Lagrangian-Eulerian for-mulation (ALE). The description separates spatially the process in a die inside zone and in a profile zone. For the description of the inside zone, where the filling process occurs, a special Euler time independent mesh is applied. By this formulation the mesh has to be generated only once, which simplifies the generation of spatially optimized meshes. For mapping of the material flow during the filling process the method uses a flow surface traction method as applied in casting simulations. A further strength of the new method is the computational efficiency which allows the modelling of extrusion process with the highest complexity with a response time of 12 hours, which is important for the industrial optimization process.

Jan 1, 2015

By P. N. Mohan Das, K. Harikrishna Bhat

"The major ilmenite reserves are located in India at Chavara (CH), Manavalakurichi ( MK) and Chatrapur, Orissa (OR). India stands first in terms of ilmenite reserves, which are estimated to be 278 million tonnes out of which, 142 million tonnes are processable. Mineralo-chemical analysis shows that Chavara ilmenite is the most weathered one with about 60% TiO2 while Chatrapur is the least weathered with about 50% TiO2. Co-existence of ilmenite with pseudorutile, rutile and haematite is observed in substantially varying amounts in the three deposits. It is observed that the tropical weathering rather than the source rock difference has apparently played an important role in imparting major compositional and structural dissimilarities among ilmenites in different places.In processing of ilmenite through the Becher process, aeration rusting of pre-reduced ilmenite is found to be the rate limiting step thus, affecting the productivity of the process. Investigations have proved that the addition of some organic compounds such as glyoxal, sucrose etc., to the system accelerates the reaction to such an extent that the rusting time has been reduced to less than half.A new route of processing ilmenite for synthetic rutile has also been developed in which, ilmenite is carbothermally reduced and then processed through plasma route. The slag thus obtained is processed further to get high-grade synthetic rutile, metallic iron and high purity iron oxide. The process has been scaled up in a continuous moving bed plasma reactor. It is technologically and economically more viable where, all the iron values are recovered as salable byproducts. This paper describes the salient features of the technologies developed for the beneficiation of ilmenite to synthetic rutile."

Jan 1, 2003

By Paul Juárez, Eduardo Albuquerque, Elves Matiolo

Este trabajo tiene por objetivo evaluar el efecto del reactivo Tiourea (TU) como depresor de calcopirita en la separación selectiva de la molibdenita por flotación diferencial empleando potencial zeta, medidas de ángulo de contacto y pruebas de flotación en celda Partridge Smith (PS).

Sep 1, 2017

By D. R. Nagaraj, Napoleon Tercero, Raymond Farinato

"Dialkyl dithiophosphinates are a unique class of collectors used in the flotation processing of Cu- Au, complex polymetallic, and precious metal ores. They are known to exhibit higher selectivity and flotation rates for Cu sulfides, galena, and precious metal values in the presence of other gangue sulfides, than the traditionally used collectors such as dialkyl dithiophosphates and xanthates. They also have an attractive HSE profile. Historically, for most reagents used in flotation, practical methods of chemical usage have preceded detailed scientific understanding of how they work; this applies also to dithiophosphinates. Recently, however, the research community has shown significant interest in this chemistry, and numerous studies have been conducted to understand the fundamentals of interactions of dithiophosphinates with several base metal sulfides and precious metals. A critical overview of fundamental studies, laboratory ore flotation, and plant practice of dithiophosphinates is given in this paper. The findings from these studies are rationalized by drawing on concepts and insights from coordination chemistry. A comparison between the interactions of dithiophosphinates and dithiophosphate analogues with various minerals and metals is also made throughout. We believe that such a critical analysis/overview will be invaluable in identifying gaps in knowledge regarding this important set of compounds, which in turn may provide a basis for the design of studies that can advance understanding of their flotation performance. INTRODUCTIONDialkyl dithiophosphinates are an important member of the class of thiophosphorus compounds that are widely used in flotation beneficiation of base metal sulfide and precious metals ores. Ore flotation studies and plant practice experience have demonstrated their unique properties compared to the traditionally used sulfide collectors such as dialkyl dithiophosphates (their closest analogues) and xanthates. The predominant dialkyl dithiophosphinate used in the industry today is sodium diisobutyl dithiophosphinate (a.k.a. DIBDTPi; AEROPHINE® 3418A1 introduced by American Cyanamid in the late 1970s; Figure 1). The widest application of AEROPHINE 3418A is found in complex polymetallic ores of Cu-Pb-Zn-Ag, Pb-Zn-Ag, and Cu-Zn where it has demonstrated improved recoveries (and flotation rates) of sulfide minerals of Cu, Pb and Ag and selectivity against sphalerite, iron sulfides, and penalty elements (Mingione, 1991). More recently, it has also been used as a collector in the processing of Cu, Cu-Ni, and Ni ores (Guitard et al., 2015) and Cu-Au ores (Dunne, 2005). In general, it is considered to possess the collecting power of xanthates together with the selectivity (against pyrite) of dithiophosphates (Hope et al., 2003a, 2003b), while requiring lower dosages than those reagents (Guitard et al., 2015). AEROPHINE® 3418A has also found an important place in several targeted formulations to improve flotation performance. Other benefits of this reagent include higher flotation rates, having a better HSE (health, safety and environmental) profile2 compared to xanthate, and exhibiting resistance to hydrolysis and oxidation (Guitard et al., 2015). Compared to diisobutyl dithiophosphate (DIBDTP), which is known to contribute significantly to frothing (often leading to over-frothing), AEROPHINE® 3418A is observed to be froth neutral (i.e. it does not alter the existing froth characteristics). As is the case for other flotation reagents, the design and application of AEROPHINE® 3418A has preceded understanding of its behavior at a fundamental level. Recently, there have been numerous fundamental and application studies designed to develop a better understanding of its interaction with sulfide minerals and precious metals. This should help in optimizing its application in flotation and provide a basis to better rationalize its unique selectivity and activity characteristics. Past studies on the interacti"

Jan 1, 2016

By Z Li, Z Yan, T Htet, S Zhang

During the pyrometallurgical processes, a substantial quantity of high-temperature ironmaking and steelmaking slags, generated at temperatures ranging from 1400 to 1600°C, is wasted, as the heat contained in these slags is released into the environment during the tapping process without effective utilisation. On the other hand, a significant amount of energy is required to reheat the cold materials for the manufacturing of glass and mineral-wool, often necessitating the addition of high-silica materials to facilitate the production process. In this study, an innovative approach is presented to harness the heat present in molten metallurgical slags to directly produce new raw materials for glass and mineral-wool manufacturing while simultaneously reducing energy consumption and mitigating CO2 emissions. The theoretical amount of waste glass that can be effectively added in the process has been estimated via thermodynamic calculation. Experimental assessments were conducted to examine the impact of high-silica waste materials on the dissolution, melting and fluidity. Potential recipes for glass and mineral-wool manufacturing were suggested and an assessment of the energy savings, and reduction in CO2 emissions with manufacturing of glass and mineral-wool using this innovative approach were included. It was determined that the processes could lead to a reduction of over 26 kg of CO2 emissions per 100 kg of new material used, primarily due to the utilisation of heat from slag and the accelerated smelting process.

Aug 21, 2024

By Cezar Henrique Gonzalez

Processos de conformação plástica têm sido aplicados nas ligas com memória de forma (LMF) para melhorar suas propriedades mecânicas. No entanto, estes processos provocam alterações das suas propriedades termoelásticas (temperaturas e entalpias de transformação, cargas críticas de indução da martensita, deformação termoelástica reversível e outras). Para aplicações tecnológicas destas ligas, por exemplo como atuadores termomecânicos, elas devem manter suas características constantes ao longo de sua utilização (propriedades termoelásticas). Neste trabalho são analisadas estas propriedades das ligas de Ni-Ti com memória de forma que foram conformadas termomecanicamente pelos processos de laminação convencional e de extrusão angular (Equal Channel Angular Extrusion - ECAE). As analises foram realizadas por calorimetria diferencial de varredura, microscopia eletrônica de varredura e teste de tração sob carga constante (simulação do efeito memória de forma para determinar a propriedades termoelásticas). Os resultados mostraram que os processos de conformação alteram drasticamente as propriedades, principalmente para aquelas amostras submetidas ao ECAE que chegam a bloquear a transformação martensítica. Tratamentos térmicos foram aplicados com o objetivo de melhorar ou restabelecer as propriedades do efeito memória de forma. Resultados das difrações de raios-X e das micrografias indicam que cada tipo de processo de conformação plástica e a formação de precipitados influenciam de forma preponderante nos comportamentos das propriedades termoelásticas. Estas análises são relevantes para aplicações tecnológicas destas ligas, pois requerem boa resistência mecânica combinada com as propriedades funcionais dos fenômenos de memória de forma.

Aug 16, 2017

By S. T. Wlodek

The surface and subscale oxidation reactions were followed by means of continuous weight-gain and metallographic techniques over the range 1600" to 2200°F (871° to 1204 °C) for up to 400 hr. Full identification of all scale and subscale reaction products was obtained by electron and X-ray diffraction. At or below 1800°F (982°C) a linear rate of reaction (QL = 46.0 kcal per mole) governed the oxidation process, extending for up to 100 hr at 1600°F (871 "C). During linear oxidation the surface scale consisted of an amorphous SiO2 film overgrown with Cr 2O 3 and NiCr204. This initial linear process was followed, and above 1800°F completely replaced, by two successive parabolic rate laws (Qp = 60 and 57 kcal per mole). This parabolic reaction involved the formation of a complex scale consisting of Cr2 O3 and smaller amounts of NiCr2O4. Parabolic oxidation appeared to coincide with the disruplion of the silica film present during linear oxidation and was followed by subscale (internal) oxidation of crystobalite and NiCr2O4. The balance between the subscale and surface oxidation reactions controls the oxidation of this commercial alloy. The amorphous silica film appears to result in the linear rate and diffusion through Cr2O3 is the more likely rate-limiting step during parabolic oxidation. THE oxidation of a multicomponent composition is a complex phenomenon not presently amenable to a rigorous classical interpretation. Nevertheless, even a qualitative understanding of the scaling and subscale reactions that occur in a commercial composition can illuminate the reactions that limit its high-temperature stability in an oxidizing environment. This study of the oxidation of Hastelloy Alloy X presents the first of a series of studies with the above approach in mind. Hastelloy X exhibits one of the best combinations of strength and oxidation resistance available in a wrought, solution-strengthened, nickel-base alloy. Although during long time exposure some precipitation of M6C and M23C8 carbides as well as a complex Laves phase occurs, the amounts are probably small enough to have no appreciable effect on the chemistry of the matrix. Radavich has identified the oxidation products on Hastelloy X oxidized for 5 min to 10 hr at 1115°F as NiO and the NiCr2O4 spinel. Oxidation for 5 to 15 min at 1500°F produced a scale of spinel, NiO, and a rhombohedra1 phase, probably Cr2Os. Sannier et 2. have reported continuous weight-gain data for Hastelloy X at 1650" and 2010°F and internal-oxidation measurements after 150 hr at 2010°F. In addition, much of the data on binary Ni-Cr alloys recently reviewed by Kubaschewski and okins&apos; and Ignatov and Shamgunova4 as well as studies of binary Ni-Mo alloys5 are also pertinent to the oxidation of this composition. EXPERIMENTAL Continuous weight-gain measurements and metallographic measurements of subscale reactions were the main experimental techniques used in this study. X-ray and electron diffraction backed up by a limited amount of electron-microprobe analysis served to characterize the nature of the scale- and subscale-reaction products. Two heats of commercial sheet of the composition given in Table I and identified as A and B were used in the bulk of this study. Internal-oxidation measurements were made on a third heat of material in the form of a 0.5-in.-diam bar. In order to assure homogeneity, all heats were reannealed 4 hr at 2175°F prior to sample preparation. weight-Gain Measurement. All specimens (1.5 by 0.4 by 0.03 in.) were abraded through 600 paper, electropolished, and lightly etched in an alcohol-10 pct HCl solution. An electrolyte of 150 cu cm H,O, 500 cu cm HsPO4 (85 pct conc), and 3 g CrO3 at a current density of 0.9 amp per sq cm or a solution of 10 pct HaW4 in alcohol used at 4 v and 0.3 amp per sq cm was used for electropolishing. The resultant surface exhibited a finish of 3 ± 1 p rms. Continuous weight-gain tests were made at 1600°, 1700°, 1800°, 1900°, 2000", and 2200°F on auer&apos; type balances capable of recording a total weight change of 110 mg with an accuracy of k0.1 mg. All tests were made in air dried to a dew point of -70°F and metered into the 2-in.-diam reaction

Jan 1, 1964