C25C3/36

MnAl alloy and manufacturing method therefor
11293085 · 2022-04-05 · ·

A MnAl alloy according to the present invention exhibits metamagnetism and has crystal grains containing a τ-MnAl phase and crystal grains containing a γ2-MnAl phase and a β-MnAl phase. When the ratio of the τ-MnAl phase is A, 75%≤A≤99% is preferably satisfied, and when the ratios of the γ2-MnAl phase and β-MnAl phase are B and C, respectively, B<C is preferably satisfied. Thus, it is possible to obtain metamagnetism over a wide temperature range, particularly, over a temperature range of −100° C. to 200° C. and to enhance saturation magnetization.

IMPROVED TIN PRODUCTION, WHICH INCLUDES A COMPOSITION COMPRISING TIN, LEAD, SILVER AND ANTIMONY

Metal compositions and processes for fractional crystallization of a molten crude tin mixture containing lead and silver are described. A process includes separating the molten crude tin mixture into a first silver-enriched liquid drain product at the liquid end of a crystallization step and a first tin-enriched product at the crystal end of the crystallization step whereby the first silver-enriched liquid drain product comprises on a dry weight basis 6.0-30.0% wt of lead, 70.0-91% wt of tin, 95.0-99.0% wt of lead and tin together, 0.75-5.00% wt of silver, and ≥0.24% wt of antimony. The first silver enriched liquid drain product also includes at least one of: 0.05-0.5% wt of arsenic; 0.05-0.6% wt of copper, 0.0030-0.0500% wt of nickel, at least 0.0010-0.40% wt of bismuth, at most 1.0% wt of iron, or at least 0.0005% wt of gold, the balance being impurities.

IMPROVED TIN PRODUCTION, WHICH INCLUDES A COMPOSITION COMPRISING TIN, LEAD, SILVER AND ANTIMONY

Metal compositions and processes for fractional crystallization of a molten crude tin mixture containing lead and silver are described. A process includes separating the molten crude tin mixture into a first silver-enriched liquid drain product at the liquid end of a crystallization step and a first tin-enriched product at the crystal end of the crystallization step whereby the first silver-enriched liquid drain product comprises on a dry weight basis 6.0-30.0% wt of lead, 70.0-91% wt of tin, 95.0-99.0% wt of lead and tin together, 0.75-5.00% wt of silver, and ≥0.24% wt of antimony. The first silver enriched liquid drain product also includes at least one of: 0.05-0.5% wt of arsenic; 0.05-0.6% wt of copper, 0.0030-0.0500% wt of nickel, at least 0.0010-0.40% wt of bismuth, at most 1.0% wt of iron, or at least 0.0005% wt of gold, the balance being impurities.

ANODES COMPRISING TRANSITION METAL AND PLATINUM GROUP METAL AS ALLOYS, AND RELATED METHODS AND SYSTEMS
20220042189 · 2022-02-10 ·

Disclosed are anodes for an electrochemical reduction system, such as for the electrochemical reduction of oxides in systems using molten salt electrolytes. The anodes comprise a rod or plate formed of and include at least one alloy of at least one transition metal and at least one platinum group metal. The alloy anodes may be less expensive than anodes formed solely from platinum group metals and may exhibit less material attrition than anodes formed solely from transition metals. Related methods and electrochemical reduction systems are also disclosed.

Device and method for preparing pure titanium by electrolysis-chlorination-electrolysis

A device and a method for preparing pure titanium by electrolysis-chlorination-electrolysis, wherein the device includes a first electrolytic cell, a second electrolytic cell, a chlorination reactor and guide tubes. The Cl.sub.2 generated at the anode of the first electrolytic cell is introduced into a chlorination reactor containing the TiC.sub.xO.sub.y or TiC.sub.xO.sub.yN.sub.z raw materials via a guide tube, and a chlorination is carried out to generate TiCl.sub.4 gas at a temperature of 200° C.-600° C. The TiCl.sub.4 gas passes through a guide tube into a cathode of the second electrolytic cell, and then an electrolysis is performed to obtain the high-purity titanium in the second electrolytic cell. At the same time, the Cl.sub.2 generated at the anode of the second electrolytic cell is recycled into the chlorination reactor in the first electrolytic cell to continue to participate in the chlorination of TiC.sub.xO.sub.y or TiC.sub.xO.sub.yN.sub.z.

ELECTROCHEMICAL CELLS FOR DIRECT OXIDE REDUCTION, AND RELATED METHODS
20210118585 · 2021-04-22 ·

A method of direct oxide reduction includes forming a molten salt electrolyte in an electrochemical cell, disposing at least one metal oxide in the electrochemical cell, disposing a counter electrode comprising a material selected from the group consisting of osmium, ruthenium, rhodium, iridium, palladium, platinum, silver, gold, lithium iridate, lithium ruthenate, a lithium rhodate, a lithium tin oxygen compound, a lithium manganese compound, strontium ruthenium ternary compounds, calcium iridate, strontium iridate, calcium platinate, strontium platinate, magnesium ruthenate, magnesium iridate, sodium ruthenate, sodium iridate, potassium iridate, and potassium ruthenate in the electrochemical cell, and applying a current between the counter electrode and the at least one metal oxide to reduce the at least one metal oxide. Related methods of direct oxide reduction and related electrochemical cells are also disclosed.

ELECTROCHEMICAL CELLS FOR DIRECT OXIDE REDUCTION, AND RELATED METHODS
20210118585 · 2021-04-22 ·

A method of direct oxide reduction includes forming a molten salt electrolyte in an electrochemical cell, disposing at least one metal oxide in the electrochemical cell, disposing a counter electrode comprising a material selected from the group consisting of osmium, ruthenium, rhodium, iridium, palladium, platinum, silver, gold, lithium iridate, lithium ruthenate, a lithium rhodate, a lithium tin oxygen compound, a lithium manganese compound, strontium ruthenium ternary compounds, calcium iridate, strontium iridate, calcium platinate, strontium platinate, magnesium ruthenate, magnesium iridate, sodium ruthenate, sodium iridate, potassium iridate, and potassium ruthenate in the electrochemical cell, and applying a current between the counter electrode and the at least one metal oxide to reduce the at least one metal oxide. Related methods of direct oxide reduction and related electrochemical cells are also disclosed.

METHOD FOR PREPARING GRID ALLOY OF LEAD BATTERY

A method for preparing a grid alloy of a lead battery, comprising the following steps: (1) preparing an aluminum-lanthanum-cerium rare earth mother alloy by using a molten salt electrolysis method; (2) melting the aluminum-lanthanum-cerium rare earth mother alloy with sodium and partial lead and uniformly stirring same to prepare an intermediate alloy; and (3) melting the intermediate alloy with calcium, tin and remaining lead and uniformly stirring same to form a grid alloy of a lead battery.

METHOD FOR PREPARING GRID ALLOY OF LEAD BATTERY

A method for preparing a grid alloy of a lead battery, comprising the following steps: (1) preparing an aluminum-lanthanum-cerium rare earth mother alloy by using a molten salt electrolysis method; (2) melting the aluminum-lanthanum-cerium rare earth mother alloy with sodium and partial lead and uniformly stirring same to prepare an intermediate alloy; and (3) melting the intermediate alloy with calcium, tin and remaining lead and uniformly stirring same to form a grid alloy of a lead battery.

Method and Apparatus for Efficient Metal Distillation and Related Primary Production Process

Method and apparatus are provided for efficient metal distillation, and for related primary product process. Vertically stacked and gravity-driven evaporators and condensers are employed to distill metals, such metals having different volatilities. A multiple-effect thermal system of magnesium and other volatile metals is used to efficiently distill and separate metals from multiple metal alloys.