Abstract: A method in treating aqueous feedstream in diverse plant site environments is disclosed for improving filter flux rates, cleaning filter media and prolonging useful operative life of media. In preferred embodiments the method is provided with steps for contacting, reacting, pressurizing and equalizing ozone and feedstream within a central area or multiple areas and sustaining high pressure throughout the system to achieve qualitatively and quantitatively improved permeate products, and reject for recycle. The method and system provide an improved cleaning and processing system characterized by an ozone-concentrated, homogeneous single phase liquid conversion of a generated ozone gas mixture and a feedstream source containing organic and inorganic pollutants. The method improves and monitors ozone oxidizing power and reflecting ORP values, and provides further media cleaning and improved oxidation reactions for attack on pollutants on each cycle/recycle operation.

Abstract: A method in treating aqueous feedstream in diverse plant site environments is disclosed for improving filter flux rates, cleaning filter media and prolonging useful operative life of media. In preferred embodiments the method is provided with steps for contacting, reacting, pressurizing and equalizing ozone and feedstream within a central area or multiple areas and sustaining high pressure throughout the system to achieve qualitatively and quantitatively improved permeate products, and reject for recycle. The method and system provide an improved cleaning and processing system characterized by an ozone-concentrated, homogeneous single phase liquid conversion of a generated ozone gas mixture and a feedstream source containing organic and inorganic pollutants. The method improves and monitors ozone oxidizing power and reflecting ORP values, and provides further media cleaning and improved oxidation reactions for attack on pollutants on each cycle/recycle operation.

Abstract: A rotating filter apparatus (10) has a stack of porous filter disks (22) attached to a vertical, rotatable hollow shaft (24) and located within a chamber (32), the shaft (24) having a plurality of openings (26) therein to the hollow bore of the shaft (24). Unfiltered fluid is introduced to the chamber (32) under pressure in a tangential entry port (34) in the same direction as disk (22) rotation. Clarified fluid passes through the disks (22) to form a filtrate that flows down the shaft (24), while the unfiltered fluid and the solid particles, or sludge, descend in the chamber (32) to a tapered section (18). Non-fluid transfer and fluid transfer seal assemblies (14, 20) comprise bearings (54, 102, 108), seals, and associated parts upon which the shaft is properly aligned, balanced, and centered. The seal assemblies (14, 20) include seals positioned about the shaft (24) to form a boundary that isolates the bearings (54, 102, 108) from the unfiltered fluid or filtrate.

Abstract: An apparatus for multiple fluid phase separation (10) includes a housing (12) having a second chamber (21) positioned above a first chamber (19). A plurality of filter disks (22) are mounted upon a rotatable vertical shaft assembly (24) in spaced stacked relation within the first chamber (19). The shaft assembly (24) includes a first interior channel (30) and a second interior channel (32). A bulk solution including two immiscible phases is introducted, under pressure, into the first chamber (19) through an entry pipe (33). The heavier phase is filtrated through the disks (22), enters the first interior channel (30), and is channelled to an exit port (32). Bulk solution having a reduced proportion of heavier fluid phase flows through radial openings (96) in the shaft assembly (24) located between the disks (22) into the second interior channel (32) and up into the second chamber (21).

Abstract: An apparatus for separating multiple phases of solids or fluids includes an exterior housing having an interior chamber. A plurality of porous filter disks is positioned within the interior chamber and have a common central passage. The disks are capable of rotating around the central passage. An inlet introduces at least one fluid phase with or without a solid phase into the interior chamber near the central passage of the disks. A centrifugal force is created within the interior chamber to form a pressure differential across the disks to draw the fluid through the disks away from the central passage, while propelling any solids present in the interior from the central passage toward the exterior housing. The fluid drawn through the disks is collected at the periphery of the disks.

Abstract: A process for beneficiating ilmenite ore using electrolytic reduction. The ilmenite ore is admixed with an acidic solution to form a mixture. The mixture is electrolytically reduced to convert at least a portion of any ferric iron that is present to ferrous iron. The acidic solution dissolves the ferrous iron in the ilmenite ore and yields beneficiated ilmenite having a relatively high titanium dioxide content.

Abstract: A process for oxidizing a metal of variable valence to a higher valence state by electrochemical means. More particularly, a process for oxidizing a metal of variable valence, such as, for example, uranium or vanadium contained in wet process phosphoric acid to a higher valence state for extraction by subsequent contact with complex organic extractants. The wet process phosphoric acid is oxidized in an electrolytic cell operated at a controlled potential via use of a reference electrode. The cell comprises a tank having at least one anode and at least one cathode, said anode and cathode having a ratio of surface areas exposed to the electrolyte in said cell of from at least about 100:1.

Abstract: The present invention provides a process for rapidly and efficiently oxidizing either or both vanadium and uranium from the trivalent and guadrivalent oxidation states, respectively, to the pentavelent and hexavalent oxidation states, respectively, through the use of a special electrode. The electrode is produced by anodically treating a substrate material selected from the group of titanium, zirconium, niobium, hafnium and alloys thereof in an aqueous electrolyte. The electrolyte comprises an aqueous solution of manganous ion in a concentration of from about 15 to 50 gm/l and from about 10 to 40 gm/l sulfuric acid. Manganese dioxide is electrodeposited on the substrate to form the electrode. The manganese dioxide coated electrode then is placed in an oxidation cell as an anode wherein it is potentiostaticly controlled to oxidize either or both vanadium and uranium without significant anode deterioration and without oxygen generation at the anode.