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By Kung-Ping Wang

This is the second installment of two-part article on the Far East. The mineral situation in Hong Kong, Indo-China, Thailand, Burma, Malaya, Indonesia, the Philippines, and British Borneo is covered.

Jan 12, 1951

By R. J. Blackwell

By R. A. Kinzie

In a conventional cement plant, the drying and heating of the raw material takes place in the upper section of a cylindrical kiln where the heat exchange is poor. In a Lepol kiln this part of the process is carried out on a traveling grate where the heat exchange is efficient. The increase in fuel economy justifies the greater complexity of the installation.

Jan 1, 1950

By Cyril Stanley Smith, Earl W. Palmer

A STUDY of the precipitation-hardening of copper steels1 led the authors to investigate malleable iron containing copper, for the low-carbon ferritic matrix in malleable iron should lend itself admirably to precipitation-hardening. It was soon found that in addition to rendering malleable iron susceptible to improvement by precipitation-hardening treatments, copper has another potentially useful effect as an accelerator of graphitization. Brief mention of these effects was given in a general paper by Lorig and one of the present authors2; the present paper gives further details on the graphitization and precipitation-hardening effects only. After the completion of this work a paper by L. Lykkin3 appeared, confirming the authors' conclusions regarding graphitization. MATERIAL USED After some preliminary heats had been made in the laboratory to determine the effect of copper, several castings from commercial air-furnace heats were obtained, and data from these alone are given here. Part of the metal was poured directly and part was treated in the ladle with the desired amount of copper before pouring. Green-sand molds were used, each holding two tensile test pieces of the form adopted by the Malleable Iron Research Institute, or two bars for graphitization studies, 5/8 in. in diameter and 9 in. long, fed through two enlarged sections equidistant from the middle and ends of the bars. Risers of suitable size insured sound castings. Tensile tests were made

Jan 1, 1935

By Lloyal O. Bacon

In the spring of 1952 Calumet and Hecla Inc. began a geophysical program near Shullsburg, Wis., in the Wisconsin-Illinois lead-zinc district, to assist the geological and drilling exploration programs. Sphalerite, the ore mineral in this area, occurs with a considerable amount of marcasite. In general the higher the percentage of sphalerite in the ore, the higher the percentage of marcasite; however, there may be mineralized zones high in marcasite but low in sphalerite. Orebodies in general are relatively narrow and elongated.

Feb 1, 1956

By O. Hyvärinen

The treatment of anode slimes at Outokumpu Pori Copper Refinery comprises the following process stages: copper leaching by air oxidation, nickel removal by digesting slimes in concentrated sulphuric acid at 200 °C, and dissolving of the formed nickel sulphate into water, roasting of the slimes in controlled gas atmosphere at 600 °C for selenium removal, smelting of slimes in a Doré furnace, electrolytic refining of silver, sulphuric acid and aqua regia leaching of slimes from the silver cells followed by the reduction of gold and platinum metals. The paper discusses operational experiences and recent developments of the process.

Jan 1, 1984

By J. H. Wernick

IN a study of the rate of decomposition of ½ -in. cubes of limestone, dolomitic limestone, and dolomite in a sweeping nitrogen atmosphere, Joseph, Beatty, and Bitsianesl found that the zone of calcination advanced at substantially a constant rate at a given temperature. The purpose of this paper is to show that their data indicate at least two processes occurring when the above carbonates decompose. It is suggested that there are two processes occurring temperature range and the other the limiting process over another temperature range. The data of Joseph and co-workers have been extended by use of the Arrhenius equation, Eq. 1, a relation beween the velocity constant k of a reaction and the absolute temperature T.

Jan 7, 1954

By William E. Ford, Edward Salisbury Dana

1. Normal Class (31) Axinite Type 2. Asymmetric Class (32) Calcium Thiosulphate Type Mathematical Relations of the Triclinic System 216. Crystallographic Axes. - The triclinic system includes all the forms which are referred to three unequal axes. with all their intersections oblique. When orientated in the customary manner one axis has a vertical posi-

Jan 1, 1922

By W. L. Zeigler

The Galena mill of the Callahan Zinc-Lead Co. is of 150 tons daily capacity and is situated at Lake Gulch, 2 miles west of Wallace, Idaho. (Fig. 1. It was constructed during the summer of 1926, work having been started late in June and the plant placed in operation Oct. 15, following.

Jan 1, 1928

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Jan 1, 1938

By F. Milton Lewis, James L. Coburn

In this paper the economics for a conventional comminution system, consisting of three stage crushing and one stage ball mill grinding, are compared to a semi-autogenous/ball mill comminution system. Capital and operating costs for a copper concentrator in Arizona at two levels of production, 20 and 40 thousand short tons of ore per day, are estimated. In order to minimize the investment and operating costs, large size equipment is selected for all four cases. These cost data are evaluated and conclusions are presented.

Jan 1, 1982

By J. Sajkiewicz

In a synthetic way discussed are certain results of papers realized at the Wroclaw Technical University in a field of the theory of exploitation of machine systems with conveyor-belt transport. The attention is paid to the two lines in these works which are concerned with the development of analytical as well as simulation methods, in both cases realized with the help of digilat computers.

Jan 1, 1977

By W. H. Nielson, L. S. Diaz

Several techniques are presented to adjust small errors inherent in data collected from material balance measurements on the flotation process. The basic technique used is a Lagrange multiplier adjustment of the filtered data taken from the equipment measurements. The raw data are adjusted such that material balances are closed. The adjustments to each data point is inversely proportional to the square of the standard error of measurement. Problem areas in equipment utilization are discussed. Typical results from on-line measurements are presented. This technique can be applied to either on-line process measurements or metallurgical test data.

Jan 1, 1973

By Ralph H. Sweetser

When a furnace-manager is '(blowing in," he generally has no time to consider the composition of the waste gas, and does not bother with it, except to take care that he does not get " gassed." Moreover, the analysis of the gases while the wood is still burning has not much to do with the economy of the normal working of the furnace; yet, on account of the deadly effects of the " blowing-in " gas when inhaled, and of its high explosive qualities, it is interesting to know its composition. In the Transactions there is no record of the analysis of the gas during an up-to-date " blowing-in." Even in Mr. Whiting's admirable paper (Trans., xx., 280) the reported analyses did

Jan 1, 1899

By Kwang K. Koh, Nicholas C. Nahas, Richard C. Neavel

Sodium, a relatively abundant element in Illinois coal, is reported to cause fouling of utility boiler heat exchange surfaces. Distilled water extraction of 22 Illinois coal samples resulted in average removal of more than 50% of their included sodium. Chlorine was the dominant anion. Extraction rate conformed to Fick's law of diffusion. Extraction with hot water increased both the rate and maximum amount removed. A commercial-scale countercurrent staged process can be envisioned as technically feasible.

Jan 1, 1978

By Horace Knerr

IT has been shown1 that the resistance to corrosion of duralumin sheet is greatly influenced by the quenching medium used in heat treatment, or, more specifically, by the rate of cooling during quenching. The severity of corrosive attack after exposure to salt-water spray increases in the following order: DEGREE OF CORROSION, BY INSPECTION, QUENCHING MEDIUM AFTER 30 DAYS OF SALT-WATER SPRAY TEST; Water, cold (60° F.) Very slight. Water boiling Slight, but more than with cold water. Oil (70° F.) Slight, but more than with cold water. Air, fan blast, 65° F Severe, scaled. Air, still, 65° F Deeply scaled. The tensile strength, yield point and elongation are only slightly affected by the quenching medium, as shown in Table 1.

Jan 1, 1930

By J. L. Hendrix, R. B. Dix

A study was made of the United States Bureau of Mines chlorine-oxygen leaching process for complex sulfide concentrates. The investigation sought to determine the kinetic order and mechanisms involved in the reactions between galena and sphalerite with chlorine. The influence of copper on the extraction rates was also studied. It has been shown that the rates of reaction of chlorine in aqueous solutions with sphalerite and galena are both zero order at 373 K with rate limiting step being the chemical reaction. Addition of cupric chloride increased the extractions of both lead and zinc.

Jan 1, 1981

By Erwin J. Durrer

The development of planning in the petroleum industry is de- scribed and the current status analyzed. Worldwide transportation networks led to corporate models which caused a differentiation between operations research and planning groups. Ranking of projects solely by ROI proved infeasible because of the diversified nature of the industry. Qualitative elements such as synergism with ongoing operations and the external socio-economic environment had to be included, leading to business plans based on scenarios of possible futures and stressing growth-opportunities over cash-flow rich mature product lines. In addition, decision analysis is finding applications in large capital, high uncertainty situations such as planning for synthetic fuel development.

Jan 1, 1977

By James K. Grunig

As the real price of uranium increases, deposits of lower and lower grade will be treated. The various occurrences of uranium ore are described and the chemical aspects of extraction are detailed.

Jan 1, 1981

By Jesse E. Wyrick

Gases and vapors are being safely stored in caverns constructed in salt formations. The storage of gas is cost competitive with other methods of gas storage and offers many advantages. Storage can be designed for high gas recovery rates and many operating caverns allow gas recovery rates in excess of 300 million cubic feet per day. Fenix & Scisson has constructed or consulted on many of these storage projects and presents some case histories beginning with the conversion of a bedded salt cavern to gas storage in 1961. Discussion includes basic considerations for storage construction, confirmation, and operation.

Jan 1, 1985