Abstract: A process for producing potassium hypochlorite solutions by admixing a hypochlorous acid solution having a concentration of 35 percent or greater by weight of HOCl with an aqueous slurry of potassium hydroxide containing 35 percent by weight or greater of KOH at a temperature below about 45.degree. C. The potassium hypochlorite solution produced has a concentration of at least 25 percent to about 60 percent by weight of KOCl.

Abstract: A process for producing hypochlorous acid by reacting an aqueous solution of an alkali metal hydroxide in droplet form with gaseous chlorine to produce hypochlorous acid vapor and solid alkali metal chloride particles in which the improvement comprises employing molar ratios of gaseous chlorine to the alkali metal hydroxide of at least about 22:1.The process achieves high yields of hypochlorous acid by minimizing side reactions including the formation of chlorate as an impurity in the alkali metal chloride particles produced.The hypochlorous acid solution produced contains from about 35 to about 60 percent by weight of HOCl, a dissolved chlorine concentration of less than about 2 percent by weight, and is substantially free of alkali metal ions and chloride ions.

Abstract: Transparent, electrically conductive and infrared-reflective films of zinc oxyfluoride are produced by chemical vapor deposition from vapor mixtures of zinc, oxygen and fluorine-containing compounds. The substitution of fluorine for some of the oxygen in zinc oxide results in dramatic increases in the electrical conductivity. For example, diethyl zinc, ethyl alcohol and hexafluoropropene vapors are reacted over a glass surface at 400.degree. C. to form a visibly transparent, electrically conductive, infrared reflective and ultraviolet absorptive film of zinc oxyfluoride. Such films are useful in liquid crystal display devices, solar cells, electrochromic absorbers and reflectors, energy-conserving heat mirrors, and antistatic coatings.

Abstract: A catalyst for decomposing an oxidising agent, such as hypochlorite ions, in an effluent comprises an intimate mixture of at least one finely divided Group IIA oxide and finely divided nickel oxide, and/or hydrates thereof, supported on pieces of a non-porous substantially inert material. Some of the nickel may be replaced by cobalt. The Group IIA oxide forms 0.5 to 50% by weight of said intimate mixture. The nickel and Group IIA oxides may be applied by contacting the support with a solution of a suitable salt, eg nitrates. Where the support is a Group IIA compound, eg magnesia, the Group IIA oxide may be incorporated into the intimate mixture by contacting the support with an acid solution of the nickel salt. In use the nickel oxide as oxidised to a higher oxidation state than NiO.

Abstract: An aqueous sodium hypochlorite solution (3) is added, in a quantity which is deficient relative to that required to decompose the entire amount of calcium chloride, to an aqueous calcium chloride solution (2), the sodium chloride which precipitates (6) is separated and the remaining amount (9) of the sodium hypochlorite solution is then added to the resulting mother-liquor (7). Single FIGURE.

Abstract: A reaction product of at least one of magnesium carbonate and magnesium silicate, with a metal chloride at a temperature exceeding 300.degree. C. Such a product, when mixed with water, sets to be an immensely strong magnesium cement. It may have aggregates of various types mixed with it.

Abstract: A process to decolorize and stabilize nitro compounds by contacting the nitro compound with an alkaline earth metal hypochlorite particulate material.

Abstract: Processes for the continuous preparation of high concentration sodium hypochlorite which controls sodium chloride formed to prevent fouling of heat exchanger equipment and to provide sodium chloride particle sizes on the order of 400 microns or greater to facilitate filtration and reduce the mother liquor retention in the salt, which processes comprise reacting in two stages pure chlorine or chlorine diluted with inert gases with a sodium hydroxide having a concentration of from about 20 to about 50 weight percent, in which the first stage of chloration of the sodium hydroxide is carried out in an absorption column wherein the concentration of sodium hypochlorite and sodium hydroxide are respectively limited to 15% and 4.5% by weight, and in the second stage of chloration, the sodium hypochlorite solution leaving the absorption column is treated with pure chlorine or chlorine diluted with inert gases in a crystallizer equipped with suitable agitation.

Abstract: A continuous system, process and associated apparatus are disclosed for reacting a gas with a liquid to manufacture a gaseous or liquid product. The preferred system comprises a reactive gas, such as chlorine and an aqueous solution, such as caustic soda, which are continuously combined and reacted under largely superatmospheric pressure and in turbulent cocurrent flow in very compact reactor equipment. Liquid bleach solutions such as aqueous solutions of hypochlorites or hypochlorous acid are among the products of major interest. The main reactor equipment consists of a fluid pressure energized, in-line mixing device followed by a low slip (closely fitted) regenerative turbine pumping unit. The fluid ports in the closely fitted stator elements of said pumping unit should have a radial dimension equal to at least about half that of the vanes.

Abstract: Waste containing sulfur and nickel sulfide is heated to volatilize sulfur and reacted with hydrogen chloride to form nickel chloride.

Abstract: Residual hypochlorite contained in chlorinated slurries of either carbonaceous gold-containing ores or mixtures of carbonaceous and oxide gold-containing ores are reduced by reaction with sulfide ion-providing chemical compounds preferably sodium hydrosulfide, sodium sulfide or hydrogen sulfide. The hypochlorite "kill" step enables subsequent cyanide leach operations to be conducted more efficiently.

Abstract: A novel method for synthesizing pentafluorotellurium hypofluorite by effecting a reaction between B(OTeF.sub.5).sub.3 and elemental fluorine.

Abstract: A process for destroying waste alkali metal hypochlorite such as sodium hypochlorite is disclosed. The process involves reacting 50-90% and preferably 70-90% of the alkali metal hypochlorite with urea at from 20.degree.-60.degree. C. and pH 6-8 with pH 7-8 being preferred. The remaining alkali metal hypochlorite can be destroyed with a reactant such as sulfur dioxide, sodium sulfite, or sodium thiosulfate.

Abstract: A process and apparatus for the manufacture of chloride-free hypochlorous acid using hydrolyzing of chlorine with steam and water vapor, solid-gas stripping of the co-generated hydrochloric acid vapor in a fluidized bed reactor, equilibrium discharge of chloride particulate from the bed of the reactor, selective dissolving of the hypochlorous acid vapor into aqueous product solution in a packed bed absorber, and closed-loop recycling of the stripped product stream.

Abstract: An electrolytic cell for the electrolysis of a sodium chloride solution includes a cathode compartment having therein a cathode for producing hydrogen during electrolysis and an anode compartment having therein an anode for producing chlorine gas during electrolysis. A single conduit is at the bottom of the cell for charging sodium chloride solution into the compartments and for discharging therefrom solutions resulting from electrolysis. A porous partition substantially separates the compartments and has a lower end terminating above the bottom of the cell at the single conduit, such that the lower ends of the compartments are in free communication. A mixing chamber is connected to the upper ends of the two compartments to mix the hydrogen and chlorine gas and to dynamically balance the pressures in the two compartments, thereby preventing mixing of the products of electrolysis from the two compartments.

Abstract: A process for the production of chlorine dioxide comprises feeding an inert gas to a reaction zone and applying an electrical discharge to the inert gas to produce a high temperature plasma. Chlorine gas and oxygen gas are supplied simultaneously to the reaction zone and reacted in the plasma to produce a gaseous mixture comprised of chlorine dioxide, chlorine, oxygen and inert gas, the molar ratio of oxygen to chlorine in the reaction zone being at least about 2.5:1. The gaseous mixture is recovered from the reaction zone. Chlorine dioxide, which may be recovered as a gas or reacted to produce an alkali metal chlorite, is employed as a bleaching agent and a water treatment agent.

Abstract: Crystalline 2-layer lithium aluminate, especially when carried in an ion exchange resin, is regenerated for use as an extractor for Li.sup.+ values in aqueous solution, said regeneration being done by using an aqueous wash containing at least about 800 ppm Li.sup.+ ion.

Abstract: The present invention concerns itself with a method for synthesizing hypofluorite compounds by utilizing fluorine fluorosulfate as a fluorinating agent and to a novel pentafluorotellurium hypofluorite compound prepared thereby.

Abstract: Process and plant for the preparation of concentrated aqueous solutions of alkali metal hypochlorite, in which a suspension of crystals of alkali metal chloride in an aqueous solution of alkali metal hypochlorite is circulated from bottom to top in a tubular reaction chamber located in an enclosure, chlorine and an aqueous solution of alkali metal hydroxide are reacted in this suspension in the chamber, a fraction of the resulting suspension leaving the open upper part of the chamber, overflows out of the enclosure and is filtered to separate the crystals, and the remaining fraction of the suspension is kept in the enclosure where it is recycled to the base of the reaction chamber.

Abstract: Process for destruction of hypochlorite, e.g. sodium hypochlorite, in an apparatus comprising a nozzle connected to one end of a desorption tube the other end of which is connected to a vessel, in the process pressurized acidified liquid issues from the nozzle in the form of a jet which contacts the wall of the desorption tube, hypochlorite solution is mixed with the acidified liquid before the liquid issues from the nozzle, and gaseous chlorine, produced by reaction of the hypochlorite and acid, and liquid are removed from the vessel.

Abstract: A process is described for the production of dibasic magnesium hypochlorite which comprises reacting a magnesium salt with an aqueous slurry of a crystalline hypochlorite salt in a reaction mixture containing a chloride ion source. The aqueous slurry has a solids content of from about 10 to about 90 percent by weight of a hypochlorite salt such as an alkali metal hypochlorite or calcium hypochlorite. The process provides a dibasic magnesium hypochlorite product which is readily separated.Dibasic magnesium hypochlorite, Mg(OCl).sub.2.2Mg(OH).sub.2 is useful in bleaching and sanitizing applications.

Abstract: The invention concerns a process and an apparatus for the manufacture of aqueous solutions of alkali metal hypochlorite.The apparatus comprises a reaction vessel in which chlorine is caused to react with a solution of alkali metal hydroxide and a control device adapted so as to regulate the relative weights of chlorine and alkali metal hydroxide for the reaction, as a function of the derivative, with respect to time, of the redox potential of the reaction, modulated by an instantaneous value of this potential.

Abstract: A fluorinating agent having an empirical formula which comprises FOIF.sub.4 O whereby said fluorinating agent is prepared by a metathetical reaction of solutions of NF.sub.4 SbF.sub.6 and CsIF.sub.4 O.sub.2 in anhydrous HF, removing the precipitated CsSbF.sub.6 and HF solvent, followed by thermal decomposition of the filtrate residue.

Abstract: Disclosed is a hypochlorite decomposition catalyst of nickel (II) oxide and NiCo.sub.2 O.sub.4 spinel, a hypochlorite destruction process using the catalyst, and a method of synthesizing the catalyst on a porous support.

Abstract: A gas containing bad smell substances and a washing solution for deodorization are fed into a wash tower so as to carry out the deodorization by the gas-liquid contact. An aqueous solution of an alkali bromide and an ozone-containing gas are fed into a bubbling vessel to produce in active bromine oxide compound. The solution containing the active bromine oxide compound is added to the washing solution and the bad smell gas is washed with the washing solution in the wash tower. The effect of deodorization is improved by the function of the bromine oxide compound and an amount of ozone discharged out of the system is decreased.

Abstract: An aqueous hypochlorous acid production process is disclosed wherein the precipitate formed upon carbonating electrolytic cathode cell liquor is contacted in a fluidized bed with a mixture of gaseous chlorine and water vapor and the exit gas from the fluidized bed is absorbed in water.

Abstract: A process for preparing hypochlorous acid in a sweep reactor is described in which gaseous chlorine is passed rapidly across the surface of an agitated aqueous solution of alkali metal hydroxide at a reduced temperature. The resulting gaseous product mixture of hypochlorous acid, chlorine monoxide, and unreacted chlorine is conveyed from the reactor to a suitable scrubber to produce an aqueous hypochlorous acid solution.The aqueous reaction product of the sweep reactor is a suspension of alkali metal chloride in alkali metal hypochlorite, which is withdrawn and filtered to separate the solid. The clarified aqueous solution of alkali metal hypochlorite is reacted with the aqueous hypochlorous acid solution from the scrubber, chlorine and lime to form an aqueous slurry of calcium hypochlorite. This slurry may be granulated by the spray graining technique, for example, to produce strong rounded granules of calcium hypochlorite.

Abstract: A process for preparing hypochlorous acid is described in which gaseous chlorine is reacted with an aqueous solution of alkali metal hydroxide in a finely divided mist form at an elevated temperature sufficient to prevent condensation of the gaseous product. Gaseous hypochlorous acid product is immediately separated from the resulting solid alkali metal chloride as it is formed and is then scrubbed with water to form an aqueous hypochlorous acid solution. This solution may be reacted with lime to produce calcium hypochlorite.

Abstract: A particulate detergent composition containing dibasic magnesium hypochlorite having a specific small particle size as the bleaching agent.

Abstract: A process for the production of dibasic magnesium hypochlorite comprises the reaction of a solid magnesium salt and a solid hypochlorite where one of the solid reactants is in the hydrate form. The process produces dibasic magnesium hypochlorite with excellent recovery of chlorine values and with reduced requirements for the disposal of solutions containing available chlorine.Dibasic magnesium hypochlorite, Mg(OCl).sub.2 . 2 Mg(OH).sub.2 is useful in bleaching and sanitizing applications.

Abstract: An aqueous hypochlorite solution containing a stabilizing amount of periodate ions, preferably an amount in the range 0.05 to 1000 parts per million (ppm) by weight based on the volume of the solution, the solution optionally containing silicate ions.

Abstract: Reactions in heterogeneous systems containing reactants in gaseous, liquid and solid phases are carried out in a tower composed of a series of superimposed reaction compartments mutually separated by horizontal shelves, through which the gaseous phase moves countercurrent to the liquid and solid phases and at the same time effects turbulent mixing with the liquid phase. The liquid and solid phases are introduced into the top compartment. The shelves are suitably perforated for upflow of the gas through bodies of mixed liquid and solids which are held on the shelves at levels determined by the heights of overflow pipes which conduct excess reaction mixture from each reaction compartment into the mixture in the compartment next below. Reaction products are taken off from the bottom compartment.

Abstract: Hypochlorite is produced by mixing chlorine and a strong alkali solution within a completely closed region filled with solution to eliminate the presence of any air pockets, thereby assuring that the gaseous chlorine will not escape from the solution during the mixing process. In carrying out the mixing step, the alkali solution and chlorine are introduced through relatively closely-spaced small streams into an enlarged chamber so that, effectively, mixing occurs by small amounts at the point of introduction of the two streams, instead of simply introducing a small amount of chlorine into a large volume of alkali solution. Mixing is further enhanced by the fact that the two streams are introduced tangentially into the chamber at diametrically opposed locations so that they swirl upwardly through the chamber in laminar flow relationship.

Abstract: The method of treating a chlorine-based total bleachery effluent in which only a chlorine and sodium salts are used in the bleach sequence comprising the steps of adding aluminum ion to said effluent in an amount sufficient to precipitate substantially all of the organics and suspended solids therein, separating the solids from said effluent, electrodialyzing the treated effluent to provide two effluent streams, one containing 200 to 600 parts per million sodium chloride which can be returned to the bleachery, and a second concentrated stream containing 5 to 10% by weight sodium chloride, evaporating said concentrated stream to a concentration of about 25% sodium chloride by weight, and electrolyzing said concentrated sodium chloride solution to produce chlorine gas, sodium hydroxide, and sodium hypochlorite.

Abstract: In a process for the dechlorination of gas mixtures containing carbon dioxide and chlorine, wherein in several absorption stages the chlorine is converted with stoichiometric alkali metal hydroxide solution into a carbonate-free alkali metal chloride-alkali metal hypochlorite solution and wherein the required stoichiometric amount of alkali metal hydroxide is introduced countercurrent to the gas stream via the last absorption stage, the improvement which comprises operating the last absorption stage in such a manner that due to free alkali metal hydroxide no alkali metal hydrogen-carbonate is present in said stage.

Abstract: A continuous process for the manufacture of calcium hypochlorite in which an aqueous slurry of lime and sodium hypochlorite is chlorinated in a mixing zone to form a sodium chloride solution containing large crystals of calcium hypochlorite which are readily separated and dried. The resulting solution containing some dissolved calcium hypochlorite is reacted with an alkali metal hydroxide to precipitate lime, which is separated and recycled to the mixing zone slurry. The lime-free solution may be used as bleach liquor or processed to precipitate solid salt useful in the preparation of brine. The remaining solution is recycled to the mixing zone slurry. Purification of fresh lime is also disclosed.The process provides an improved separation of calcium hypochlorite and sodium chloride, and recycles all solutions to minimize pollution of water resources.

Abstract: The pollutants are oxidized with oxygen atoms obtained from catalytic decomposition of hypochlorite ions and are filtered out and entrapped on the catalytic material of the filter bed as the waste water flows through the bed. The catalytic material catalyzes the incineration of the trapped pollutants by an oxidizing gas which flows through the bed of the catalyst and which regenerates the catalyst.

Abstract: A process for preparing hypochlorous acid in a sweep reactor is described in which gaseous chlorine is passed rapidly across the surface of an agitated aqueous solution of .[.alkali metal.]. .Iadd.sodium .Iaddend.hydroxide at a reduced temperature. The resulting gaseous product mixture of hypochlorous acid, chlorine monoxide, and unreacted chlorine is conveyed from the reactor to a suitable scrubber to produce an aqueous hypochlorous acid solution.The aqueous reaction product of the sweep reactor is a suspension of .[.alkali metal.]. .Iadd.sodium .Iaddend.chloride in .[.alkali metal.]. .Iadd.sodium .Iaddend.hypochlorite, which is withdrawn and filtered to separate the solid. The clarified aqueous solution of .[.alkali metal.]. .Iadd.sodium .Iaddend.hypochlorite is reacted with the aqueous hypochlorous acid solution from the scrubber, chlorine and lime to form an aqueous slurry of calcium hypochlorite.