| METALLURGICAL AND MATERIALS TRANSACTIONS B | |
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Volume 27B, No. 4, August 1996 This Month Featuring: The 1994 Howe Memorial Lecture; Hydrometallurgy; Pyrometallurgy; Electrometallurgy; Transport Phenonema; Physical Chemistry; Solidification; Mathematical Modeling. View August 1996 Table of Contents.
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The Mineralogical Deportment of Germanium in the Clarksville Electrolytic Zinc Plant of Savage Zinc Inc.
J.E. DUTRIZAC, T.T. CHEN, and R.J. LONGTON
A mineralogical study was carried out on the neutral leach residue and weak acid leach residue generated from Gordonsville zinc concentrate at the Clarksville Electrolytic Zinc Plant of Savage Zinc Inc. The intent was to characterize the mineral forms and associations of germanium. The Gordonsville zinc concentrate consists mostly of sphalerite which has a solid solution Ge content of ~400 ppm; the sphalerite is the dominant, if not only, Ge carrier in the concentrate. The neutral leach residue consists principally of iron gel-silica gel, ZnO, and basic zinc sulfate, (Zn,Cu)4(SO4)(OH)6·4H2O, together with minor amounts of ZnFe2O4, sphalerite, Zn2SiO4, Zn-Fe-Pb silicate, and PbSO4, as well as traces of quartz, silicates, Pb-K jarosite solid solution, Fe2O3, and FeO·OH. The major Ge carrier is the iron gel-silica gel phase, but modest amounts of Ge are present in the ZnO, ZnFe2O4, sphalerite, and Zn-Fe-Pb silicate phases. The weak acid leach residue consists mostly of iron gel-silica gel, ZnFe2O4, PbSO4, Pb-K jarosite, Zn-Fe-Pb silicate, and quartz. The major Ge carrier is the iron gel-silica gel phase which contains up to 1.7 pct Ge and accounts for ~70 pct of the total Ge content of this residue. The remaining Ge is carried by the Zn-Fe-Pb silicate, ZnFe2O4, and some of the rare Mn-Pb-Fe oxide phases.
Preparation of Fine Copper Powders from Organic Media by Reaction with Hydrogen under Pressure: Part I. Experimental Study
R. SARRAF-MAMOORY, G.P. DEMOPOULOS, and R.A.L. DREW
In this work, a novel method of preparing copper powder having the required properties for thick film applications was investigated. This method involves the precipitation of copper powder by hydrogen reduction under pressure from Kelex 100-decanol-Versatic 10-kerosene media. The parameters studied were temperature (453 to 573 K), hydrogen pressure (1.03 to 3.79 MPa) time, use of additives, solvent composition, etc. Powders with the following excellent properties were produced: d50=1 µm; 80 pct spread - 1.3 + 0.7 µm; specific surface area = 1 ± 0.2 m2/g, spheroidal shape; and 0.056 wt pct oxygen content.
Preparation of Fine Copper Powders from Organic Media by Reaction with Hydrogen under Pressure: Part II. The Kinetics of Particle Nucleation, Growth, and Dispersion
R. SARRAF-MAMOORY, G.P. DEMOPOULOS, and R.A.L. DREW
The kinetics of very fine copper powder (1 to 2 µm) production by hydrogen reduction of solvent extracted copper chelates have been determined. The Avrami-Erafeer model for nucleation growth processes has been found to best describe the precipitation kinetics. The model parameters were correlated with reasonable success to the morphology of the copper powder. The chemically controlled particle formation process was found to exhibit 30 to 58 kJ/mol activation energy depending on the temperature range and a complex dependency (from first order to fractional/zero order) on hydrogen pressure. A steric stabilization model has been advanced to interpret the cooperative action of decanol and Versatic 10 in stabilizing the very fine copper powder dispersion.
at 1673K in order to obtain the activities of FexO in CaO+P2O5+FexO ternary slags. By using the Gibbs-Duhem integration, the activities of P2O5 and CaO were also obtained.
Formation of Aluminum-Silicon Alloys from Feldspars--Determination of Silicon, Light, and Heavy Elements in Silumin by Scanning Electron Microscopy
A. OLSEN, J.R. STUBERGH, and T. VINSAND
Silumin has directly been deposited from feldspars by thermal reduction with aluminum metal at 1000°C. The six analyzed samples of silumin alloys contained 10.8 to 15.3 mass pct silicon in aluminum. The amount of iron deposited was 0.17 to 0.40 mass pct, magnesium was in the range of 0 to 1.8 mass pct, and sodium was 0.35 to 0.55 mass pct. The amounts of titanium, calcium, and potassium were quite close to the detection limit for these elements, which is proposed to be 0.0 to 0.1 mass pct. The sulfur and phosphorous concentrations were too low to be measured by scanning electron microscopy. Analyses were made by scan plot and spot tests of both the aluminum matrix and silicon crystals.
Experimental Study of Splash Generation in a Flash Smelting Furnace
LIOW JONG-LENG and NEIL B. GRAY
A survey of previous studies of splash formation in metallurgical vessels revealed that little information is available to characterize and describe the processes involved in splash formation. An experimental study of splash formation by top submerged gas injection was carried out in the settler region of the nickel flash smelting furnace at the Kalgoorlie Nickel Smelter (KNS) both to obtain some visualization of the splash mechanisms that occur on a plant scale and to measure the amount of splash being formed. Video images taken of the splashing showed that large sheets of melt were formed by the escaping gas and subsequently thinned into ligaments which then broke up into large splash drops. The video could only resolve a minimum size of 2 cm. The large splash drops visible on video have an initial velocity between 1 and 2 m/s, are unstable, and fall back into the bath after traveling a short distance. The analysis identified two major splash forming mechanisms. First, the gas injected resulted in the bulk movement of the melt to form a cavity and large sheets of melts being thrown around the point of injection. The area affected by this splash mechanism can be predicted successfully by using an energy balance between the removal of the melt in the cavity and the energy of the gas being injected. Second, the slag free surface within the cavity is highly unstable, and through the Kelvin-Helmholtz instability mechanism, small splash droplets are generated which are carried into the furnace's top space. A model proposed for the formation of the smaller splash droplets predicted that the splash collected decreases exponentially with increasing height above the slag free surface from the point of splashing, and this is in agreement with the experimental results obtained.
Communication: Cold Model Study of the Surface Profile in a Continuous Slab Casting Mold: Effect of Second Phase
DHARMENDRA GUPTA and A.K. LAHIRI
Communication: A Unified Representation of the Two-Phase Plume Characteristics in Gas-Stirred Ladle Systems
VELURU SUDHAKAR and DIPAK MAZUMDAR
MgO+CaF2
G° = -68,050 - 2.47 T (±100) J mol-1
SrF2+CaO
G° = -35,010 + 6.39 T (±80) J mol-1The standard free energy changes associated with cell reactions agree with data in standard compilations within ±4 kJ mol-1. The results of this study do not support recent suggestions for a major revision in thermodynamic data for CaO.
Thermodynamics of Sulfur in the BaO-MnO-SiO2 Flux System
TATSUO KOBAYASHI, KAZUKI MORITA, and NOBUO SANO
The sulfide capacity of the molten BaO-MnO-SiO2 system was determined by measuring the sulfur partition ratio between the oxide and an Ag-S alloy in a controlled CO-CO2-Ar gas mixture at 1573K for two purposes. One is to develop highly basic fluxes which can extensively desulfurize manganese-based alloys, and the other is to examine the effect of BaO addition on thermodynamic properties of sulfur in the MnO-SiO2 melts from which MnS precipitates functioning as the nucleus for subsequent
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transformation of steel. The sulfide capacity of the BaO-MnO-SiO2 system strongly depends on the composition, and MnO has been found to enhance sulfide capacity to a greater extent than BaO at less basic compositions.
Use of Solid-Electrolyte Galvanic Cells to Determine the Activity of CaO in the CaO-ZrO2 System and the Standard Gibbs Free Energies of Formation of CaZrO3 from CaO and ZrO2
JUN TANABE and KAZUHIRO NAGATA
The activity of CaO in the CaO-ZrO2 system has been measured at 1572 to 1877K with a Galvanic cell composed of 4CaO·P2O5 as the solid electrolyte. The activity ZrO2 was calculated from the activity of CaO by integrating the Gibbs--Duhem relation. From the activities of CaO and ZrO2, the standard Gibbs free energy of formation of CaO·ZrO2 was determined as follows:
Gf0/J mol-1 = -25,200 (±150) - 17.58 (±0.085) T (1633 to 1873K)
Communication: Discussion of "Representation of Mixed Reactive Gases on Free Energy (Ellingham-Richardson) Diagrams"
D.R. GASKELL
Communication: Author's Reply
C.V. ROBINO
Communication: Viscosity of Superalloy 718 by the Oscillating Vessel Technique
R.A. OVERFELT, C.A. MATLOCK, and M.E. WELLS
Communication: M23C6 Carbide Equilibria in the Fe-Cr-C System
J. SOPOUSEK and J. VRESTAL
Communication: Radioscopic Visualization of Isothermal Solidification of Eutectic Ga-In Alloy
R. DEREBAIL and J.N. KOSTER
Communication: Prediction of Dendrite Arm Spacing for Low Alloy Steel Casting Processes
M. EL-BEALY and B.G. THOMAS
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