Abstract: A process for producing lithium hypochlorite which admixes an aqueous hypochlorous acid solution, having a concentration of 35 percent or greater by weight of HOCl, with an aqueous slurry of lithium hydroxide at a temperature in the range of from about 0.degree. to about 20.degree. to produce a solution of substantially pure lithium hypochlorite. The lithium hypochlorite solutions produced can be dried directly or concentrated by cooling. The solid lithium hypochlorite produced is a highly pure source of available chlorine.

Abstract: A process for producing lithium hypochlorite comprises admixing an aqueous hypochlorous acid solution having a concentration of 35 percent of greater by weight of HOCl with an aqueous slurry of lithium hydroxide at a temperature in the range of from about 0.degree. to about 20.degree. C. to produce a solution of lithium hypochlorite. The solution is concentrated by evaporation at temperatures in the range of from about 30.degree. to about 60.degree. C. and at subatmospheric pressures to form a paste of lithium hypochlorite. After separating the paste into a cake of lithium hypochlorite and a mother liquor, a potassium compound is admixed with the mother liquor. The process produces a highly pure solid lithium hypochlorite product having a concentration of at least 80 percent available chlorine.

Abstract: A process for preparing doped barium and strontium hexaferrite compounds having the formula (I):Afe.sub.12-r-s M.sub.r N.sub.s O.sub.19 (I)wherein A is barium or strontium; M is cobalt, zinc, nickel; N is titanium or ruthenium and r and s are individually in the range from about 0.1 to about 1.2, said process comprising:(a) forming particles of a doped Fe.sub.3 O.sub.4 /ACO.sub.3 co-precipitate wherein A is defined above from (i) a ferric compound, (ii) a ferrous compound, (iii) a barium or strontium compound, (iv) a cobalt, zinc or nickel compound, (v) a titanium or ruthenium compound and (vi) alkali metal carbonate;(b) suspending the doped Fe.sub.3 O.sub.4 /ACO.sub.3 particles in a concentrated aqueous solution of an alkali halide;(c) spray drying said suspension to form a dried powder comprising said doped Fe.sub.3 O.sub.4 /ACO.sub.3 particles distributed onto the surfaces of the high temperature-melting alkali halide crystals;(d) calcining said dried powder at a temperature from about 700.degree. C.

Abstract: Doped co-precipitates of magnetite (Fe.sub.3 O.sub.4) and ACO.sub.3, wherein A is barium, are prepared by a simplified process. This process involves reacting together, in an aqueous medium containing dopant ions, a ferric compound, a ferrous compound, a barium compound and an alkali metal carbonate.

Abstract: A process for the electrolytic production of a chloride-free mixture consisting essentially of sodium and potassium nitrates is disclosed. In this process, an anolyte brine comprised of a mixture of sodium and potassium chlorides dissolved therein is electrolyzed in a membrane type electrolysis type cell to produce a mixed alkali metal hydroxide catholyte solution. The catholyte is reacted with nitric acid to form a mixed potassium-sodium nitrate solution. By properly adjusting the ratio of potassium chloride to sodium chloride concentration in the anolyte brine, a final nitrate product containing about from about 40% to about 80% NaNO.sub.3 and from about 60% to about 20% KNO.sub.3 by weight can be produced. The resulting product, after drying is suitable for use in many solar panel heat transfer applications.

Abstract: An improved process is described for the electrodeposition of both a low overvoltage metal and a sacrificial metal onto an electrically conductive substrate. The sacrificial metal is later removed by leaching the electrodeposited substrate with alkali metal hydroxide. The improvement comprises adding a sacrificial metal to the electroplating solution after electrodeposition is initiated. The amount of electric current supplied to the electroplating solution during electrodeposition may be increased or decreased over time intervals to increase the surface area and the electrochemical activity of the electroplated substrate.

Abstract: An improved process is described for the electrodeposition of both a low overvoltage metal and a sacrificial metal onto an electrically conductive substrate. The sacrificial metal is later removed by leaching the electroplated substrate with sodium hydroxide. The improvement comprises adding a sacrificial metal to the electroplating solution after electrodeposition is initiated. The amount of electric current supplied to the electroplating solution during electrodeposition may be increased or decreased to increase the surface area and the electrochemical activity of the electroplated substrate.