Abstract: A machine coolant recycling system has a holding tank in which machine coolant to be recycled is accumulated. The machine coolant in the holding tank is continuously filtered for a predetermined period of time and the surface of the machine coolant is continuously skimmed to remove undesired contaminants therefrom. The machine coolant from the holding tank is supplied to a centrifuge where it is centrifuged and is then pumped to a blending tank where it is chemically tested and reconstituted to its original composition. The machine coolant is then again continuously filtered until it is needed.

Abstract: This invention pertains to a multi-stage separator vessel through which the to-be-cleaned fluid flows. Aeration assemblies within the inner cells disperse micro-fine gas bubbles into the fluid for cleaning purposes. Additionally, the inlet piping contains a separator that begins the separation process before this fluid is discharged into the first cell. An L-shaped passageway interconnects the various flotation cells of this separator with the entrance of each such passageway being at an elevation below its exit. A weir is located within each flotation cell that is adjustable as needed. This weir empties into a channel alongside the separator vessel that collects the separated contaminants flowing over the weir for later disposal.

Abstract: This invention pertains to a multi-st vessel through which the to-be-cleaned fluid flows. Aeration assemblies within the inner cells disperse micro-fine gas bubbles into the fluid for cleaning purposes. Additionally, the inlet piping contains a separator that begins the separation process before this fluid is discharged into the first cell. An L-shaped passageway interconnects the various flotation cells of this separator with the entrance of each such passageway being at an elevation below its exit. A weir is located within each flotation cell that is adjustable as needed. This weir empties into a channel alongside the seprator vessel that collects the separated contaminants flowing over the weir for later disposal.

Abstract: An improved gas dissolving and releasing liquid treatment system involving the use of multi-stages gas dissolving pressure vessel and the use of a pressurized water release assembly and an open vessel is described. The gas dissolving and releasing liquid treatment system includes a liquid pressure pump, a pressure vessel, a gas injector, an inlet nozzle assembly, a gas compressor, gas regulators, gas flow meters, pressure gauges, a safety valve, a bleed-off point, feeders, pumps, a pressurized water release unit, a liquid flow meter, an open vessel, sludge removal means, and air emission control means. More than one gases introduced at different inlets are dissolved simultaneously and efficiently in the pressure vessel under controlled high pressure and high rotating velocity. The improved liquid treatment system is compact, simple and cost-effective, and is applied to ozonation, chlorination, recarbonation, oxygenation, bio-oxidation, nitrogenation, aeration, and flotation processes.

Abstract: This invention pertains to a multi-stage separator vessel through which the to-be-cleaned fluid flows. Aeration assemblies within the inner cells disperse micro-fine gas bubbles into the fluid for cleaning purposes. Additionally, the inlet piping contains a separator that begins the separation process before this fluid is discharged into the first cell. An L-shaped passageway interconnects the various flotation cells of this separator with the entrance of each such passageway being at an elevation below its exit. A weir is located within each flotation cell that is adjustable as needed. This weir empties into a channel alongside the separator vessel that collects the separated contaminants flowing over the weir for later disposal.

Abstract: A filter module (11) comprises a housing divided internally by a partition (14) into two compartments (15, 16). At least one hollow cylindrical filter element (12) is housed in one of the compartments, the or each filter element fitting about an opening (19) in the partition (14). A filter assembly (10) comprises a plurality of filter modules (11) mounted in a fluid flow line (13) such that incoming fluid enters one of the compartments, flows through the walls of the filter elements and filtered flow emerges from the other compartment.

Abstract: Apparatus for oil purification comprises a packed column for contacting sour oil with steam from a boiler, a gravity separator for separating the oil and water, a coalescer for coalescing the recovered oil, and a condenser for separating the lighter fraction from the column.

Abstract: A system for treating effluents such a sewage includes a mixing chamber and a separation chamber. In the mixing chamber various chemical additives are introduced in to the effluent and thoroughly mixed to act as a flocculent to extract the solid materials in the separating chamber. In the separating chamber the mixed materials are caused to flow longitudinally in a laminar flow condition to allow stratification of the liquid from the solid materials. In the mixing chamber there is provided a plurality of transverse baffles spaced longitudinally and rotated angularly relatively to a longitudinal axis of the tube. Each baffle has tapered holes to act as a venturi to mix the materials. In the separation chamber there is provided an auger flight rotating slowly which has holes through the flight thus generating a laminar flow to provide improved separation of the solid and the liquid components.

Abstract: A filter nozzle equipped with annular filter discs which establish flow paths (26, 28), serving to conduct the filter liquid and which paths are radial (28) and also penetrate through (26) the filter discs (18). These passages (26) through the filter discs (18) are in themselves formed as passages (26) that become narrow in the flow direction of the filtered water, and are distributed uniformly over the disc (18). The discs (18) have projections which ensure that the passages (26) of two adjacent discs are not in alignment. With such a filter nozzle, the danger of blockage is much less than with known nozzles, assuring a steady operation and requiring less frequent cleaning.

Abstract: In apparatus for mixing and then separating different flow streams, such as solvent extraction apparatus, a cascade of contactors and jet pumps are arranged in counter-current flow mode. The same one flow stream is applied to the drive port of each jet pump in the cascade and the other flow stream is applied to the suction port of each jet pump in the cascade. The jet pumps in the cascade increase in size from a high pressure to a low pressure end of the cascade so that the suction pressure required at successive jet pumps is reduced.

Abstract: A body fluid treating circuit comprising a block for collecting a body fluid from a human body, a body fluid treating block and a block for returning the treated body fluid to the human body, said body fluid treating block comprising a plurality of treating units for treating the body fluid by passing therethrough, the units being arranged in parallel flow relationship, body fluid feed and return lines connected to each of the treating units so as to selectively feed to and return from the units through line switching means, regenerating liquid feed lines connected to each of the units so as to selectively feed the regenerating liquid to the units through line switching means, washing liquid feed lines connected to each of the units so as to selectively feed the washing liquid to the units, discharge lines for discharging the regenerating liquid or washing liquid connected to each of the units so as to selectively discharge from the units through line switching means, and a means for measuring the salt concen

Abstract: An hydraulic spiral separator (10), for separating minerals, having at least one substantially helical trough (11) of a cross sectional shape comprising a base portion, an upwardly directed wall portion radially outwardly of the base portion and an upwardly directed lip radially inwardly of the base portion. The characterizing feature is that the wall portion is connected to a plurality of support members (12) positioned radially outwardly of the wall, and the lip is free and unconnected directly to any supporting means, which enables a number of spirals to be stacked coaxially thus saving floor space. Optionally the trough (11) is made of flexible material so that by varying the attachment to the support members (12) the trough may be flexed to change its pitch. Inlet pipes (16), and (18) are fitted as are conventional splitters (19) having moveable vanes (21).

Abstract: The invention relates to an air-controlled settling apparatus having an air vessel within which is a wall that divides the vessel into air supply and air exhaust ducts. Inlet and outlet valves are mounted within the air supply duct and establishes communication between the settling chambers and the air supply and exhaust ducts. The apparatus construction is distinguished by simple construction and low noise in operation.

Abstract: The invention provides a septic tank system of greatly improved effectiveness in maintaining optimum bacterial action for a maximum length of time by utilizing a plurality of serially-connected tanks with the water level in each successive tank being lower than that in the first tank so that gravity flow is established between the successive tanks. A unique transfer means is provided between each of the successive tanks comprising one or more horizontal pipes having their inlet ends closed, each horizontal pipe having a wide opening in the upper portion thereof at a level preferably above the centerline of the pipe in order to permit the removal of scum through said openings by entrainment and/or suction action of the fluid flowing through the transfer pipe, thereby permitting gases to freely escape through the scum from the effluent surface of each tank and preventing deleterious effects of trapped gases upon the biodegradation action normally produced in each successive septic tank.

Abstract: Contactor-separator units of a sub-assembly in which an isotopic exchange between two immiscible phases takes place are associated in m lines and n columns. One of the phases leaving a contactor-separator unit is directly directed to the adjacent contactor-separator unit in the same line, whereas the other phase leaving the same contactor-separator unit, is directed directly to the adjacent contactor-separator unit in the same column. Each of the m lines and n columns is provided with a single pump. The instantaneous flow rates of each phase are substantially equal at the input and the output of each of the contactor-separator units.

Abstract: A multi-turn labyrinth disk (10) is provided for a pressure reduction disk stack (12) which has an integral filter screen (34). The filter screen (34) comprises a series of small area passages (A.sub.2) located on the periphery of the disk (10) which lead to a common high capacity radial passage (32) used to supply a series of multi-turn labyrinth paths (18).

Abstract: A core extender and seal are provided which may be used in combination with cartridge filters. The core extender includes a body having first and second ends which are connected by longitudinal communication means through the core extender body. A radially extending shoulder extends from the body and is axially spaced from at least one end of the body, and preferably is a flange having on at least one lateral surface thereof an annular sealing ring. An external surface extends from at least one end to the radially extending shoulder. The portion of the body defined by an external surface may be inserted into the longitudinal bore of the filter cartridge in order to perform a sealing and connecting function between adjacent filters or a cartridge filter and the filter housing.

Abstract: An apparatus for countercurrent chromatography consisting of a coiled separation column which is rotated about the axis about which is it wound and the axis is also rotated about a main axis. The embodiments of the invention are based on the fact that the pattern of the centrifugal force field greatly changes with the ratio of the two radii of rotation and depending on the particular effect desired, the apparatus is configured to achieve the most effective force field to gain the effect. The separation column is a tube helix wound around a flexible core member which can be wound onto the coil holder in various orientations to further effect the desired results.

Abstract: Biological treating systems include a treating tank for receiving wastewater to be treated, and a wastewater contacting unit mounted for reciprocating movement into and out of wastewater retained within the tank. Movement of the unit out of the wastewater exposes it to oxygen that is needed to maintain an aerobic environment for biolgical slimes, and movement of the unit into the wastewater permits these slimes to feed upon and metabolize pollutants therein. Preferably the systems include a plurality of wastewater contacting units positioned in pairs on opposite sides of axles and connected thereto. These axles are mounted for reciprocating movement, and a drive mechanism is provided to reciprocate the axles and the connected pairs of contacting units.

Abstract: A process and apparatus for clarifying a liquid loaded with suspended solid substances by decanting said substances, wherein the liquid to be treated is caused to flow along a flow path at least one portion of which is an upwardly directed flow path portion having a geometrical axis inclined with respect to the horizontal, said flow path portion being defined within an enclosure in which said liquid flows between plates arranged in at least two groups, each group containing substantially equidistant positioned plates disposed parallel to said inclined axis, said plates of each one of said groups being parallel to each other, and the parallel plates of each group forming with the vertical plane comprising said inclined axis an angle different from 90 degrees, while forming with the plates of the other group an angle of between about 20 degrees and 75 degrees, whereby the suspended substances are deposited on said plates and then slide downwardly thereon toward the wall of said enclosure.

Abstract: A system is provided for continuously removing contaminants from a fluid stream on a high volume basis, such system being adapted particularly for use with contaminated lubricating oil found in industrial heavy equipment such as drop forges which requires large volumes of lubricating oil for effective, continuous operation.

Abstract: An improved lamella separator which reduces the contamination of the clear liquid output thereof in comparison with conventional lamella separators of the prior art. In a preferred embodiment thereof, the thickness of the feed liquid layer containing solid material is monitored at one or more regions in each of the channels of the separator so that when the thickness thereof approaches or exceeds about one half the channel depth in one or more channels, a control system responsive thereto maintains such thickness in such one or more channels at less than one half the channel depth.

Abstract: A device for separating a fluid system, having at least two phases of different specific gravities, including a lower preceding centrifugal separator; and an upper succeeding centrifugal separator, each of said separators having an axially upwardly extended centrifuging chamber providing an upper tangential inlet through which the fluid system enters the chamber to swirl therein, a lower outlet for drawing the heavier phase from the chamber, and a tubular vortex finder through which the lighter phase exits from the chamber mounted coaxially within the upper end of the chamber having a lower end in the chamber downwardly spaced from the inlet and an upper end upwardly of the chamber, said separators being substantially axially aligned, and a substantially cylindrical conduit circumscribing the upper separator having a lower end connected to the upper end of the vortex finder of the lower separator and to the inlet of the upper separator, the inlet of the lower separator being adapted for connection to a source

Abstract: Permanent magnetic separators for liquids to be purified which comprise one or more ferromagnetic catch and discharge bodies for the impurities contained in the liquid, which impurities are removed by means of at least one stripper from the effective adhesive surface, wherein said catch and discharge body or bodies is polarized from the outside, said catch and discharge body or bodies consisting of two bowl-shaped rotary bodies placed opposite each other and separated by an operating gap, and at least one of said catch and discharge bodies is positioned rotatably between two pole shoes placed opposite each other of at least one magnetic yoke. Additional features and particular embodiments include, among others, juxtaposed pairs of the catch and discharge bodies and switching units for effecting shorting of the magnetic lines of force.

Abstract: A gas transfer system adapted to dissolve a gas or other compressible fluid in a relatively non-compressible liquid such as waste water with a minimum expenditure of energy. The system makes use of a drum divided by radial vanes into liquid chambers. Rotation of the vanes causes the chambers to rotate about the central axis of the drum whereby in the course of every operating cycle, each chamber is brought into operative relation with the respective interfaces of an inflow station, a gas transfer station and an outflow station. At the inflow station, raw liquid to be treated is fed into the chamber then in operative relationship therewith to produce a liquid batch therein. Concurrently, at the transfer station another batch of raw liquid in the chamber then in operative relation therewith is subjected to pressurized gas to effect the absorption of the gas by the liquid.

Abstract: To provide only dry steam to a steam appliance, under controlled conditions, a housing block is formed with steam inlet and outlet flanges or the like, a filter being removably located in the housing immediately behind the inlet and a control valve located in the housing immediately behind the outlet; the housing forms a space between the filter and the control valve to dry admitted steam, including a condensate collecting region at the bottom thereof which terminates in an outwardly accessible drain opening. The drying chamber formed by the housing is separated or subdivided into compartments by at least one impact or deflection plate against which the steam is guided in order to separate the drying chamber into a pre-drying and a post-drying chamber and efficiently remove moisture and water droplets from the steam introduced into the system.

Abstract: A compound separation device including at least two separators each comprising a plurality of inclined separation passages defined between inclined corrugated plates or the like, connecting means being provided to interconnect said separators selectively in series or in parallel.

Abstract: Decantation tanks receive an oil-water mixture from a holding tank. These decantation tanks are set at varying elevations and are arranged to operate in series to drain off oil that has separated out. These tanks may have heat producing elements associated therewith to increase the efficiency of oil separation, and chemicals may be employed in these tanks also to increase such efficiency if necessary. Separator tanks are also provided in the system and receive oil-water mixture from the bottom of the decantation tanks for further separation of oil from the water. These separator tanks have a skimming apparatus therein and also have a pair of baffles under which the water must travel to accomplish further separation of the oil. The separator tanks have a cross partition, and water in a main portion of the tank flows over such partition to a rear compartment from where it is directed to an open top inspection tank and filtered. The pH of the effluent may be altered at this point if necessary.

Abstract: Process is disclosed for effecting phase separation of relatively high and low viscosity immiscible liquids comprising maintaining, between inner means in relative rotational movement with outer sleeve means, at least one zone of increased pressure constriction and of decreased pressure constriction; feeding a multiphase mixture of relatively low viscosity and relatively high viscosity liquids to the interior of said sleeve means between said zones of increased and decreased pressure constriction; and withdrawing said high viscosity liquid and said low viscosity liquid from the vicinities of said zones of increased and decreased pressure constriction, respectively.

Abstract: A sewage settling tank is provided with two or more banks of tube settlers to improve the settling rate. The tube settlers are spaced above the bottom of the settling tank and upstanding from about the periphery of each bank is a baffle member which defines a clear water zone directly above each bank. The baffle is provided with an opening which extends below the water level to permit the carriage of a floating siphon system to pass into the clear water zone, the inlet of the siphon extending down to the bottom of the settling tank in order to remove the sludge immediately beneath each bank of tube settlers. The opening in the baffle is provided with an air gate to permit the passage of the floating carriage through the opening while preventing the untreated water from flowing through the opening into the clear water zone.