Abstract: In-situ cleaning of the bilgewater processing plates of stacks within the tank chamber of an oil/water separator is performed by an injected chemical cleaning agent while being dispersed by diverted flow of pressurized air introduced into the tank chamber below the plate stacks in the form of air bubbles emerging from plural branches of an air sparging array positioned in underlying alignment with crest formations of the processing plates.

Abstract: A separation apparatus, in particular intended for separation of amalgam from water, includes a pre-settling chamber, a distribution chamber and a fine settling zone. The fine settling zone includes a plate package, with a plurality of plates fixed with spacing, forming settling channels. The plates can be machined so that they are provided with a large number of fine bumps and recesses.

Abstract: There is described a liquid treatment installation including a tank which defines a substantially vertical flow channel of circular cross section. Disposed coaxially in the flow channel there is a spiral separator plate pack 20 which comprises one or more conical helical plates which define at least one helical flow passage between axially facing surfaces of the plate or plates. The conical helical plate or plates of the separator plate pack 20 consist of a plurality of platelets 10, which have dimensions that allow them to pass through an opening 21 which runs axially through the centre of the spiral separator. The invention also relates to a method of constructing the above liquid treatment installation and to a method for assembling the spiral separator plate pack 20.

Abstract: A method and device for separating grease from waste water. The separator device includes a receptacle with an upper first part and a lower second part separated by a plate. The receptacle further has an inlet port for waste water, a discharge port for separated waste water, discharge means for grease and/or sludge, and an overflow pipe establishing a connection between the receptacle first part and the receptacle second part. Waste water is supplied through the inlet port to the upper first part, and the waste water is allowed to undergo a separation by gravity, whereby a grease layer is formed on a separated waste water layer and a sludge layer on the plate. In order to achieve a high degree of separation, separated waste water is allowed to flow through the overflow pipe to the receptacle lower second part. Grease is removed from the grease layer and/or sludge from the sludge layer through the discharge means, and separated waste water is discharged through the discharge port.

Abstract: A multi-directional flow gravity separator for separating a mixture of two immiscible fluids with different densities includes an elongated generally vertical tank, in which the mixture flows in a generally downward direction, and an effluent discharge tube through which the clarified effluent flows upward and out the tank. Alternatively, the separator includes an elongated vessel, or shroud, within the tank, through which the mixture flows in a generally upward direction before flowing downwardly in the tank; the clarified effluent is discharged from about the bottom of the tank. Alternatively, a separator includes both the elongated vessel and an effluent discharge tube. Alternatively, the vessel of a separator includes a coalescer; preferably, the coalescer results in an increased length of the fluid flow path through the vessel; most preferably, the coalescer is a helical spiraled vane, which results in a helical fluid flow path.

Abstract: A liquid purification and separation apparatus for separation of pollutants in stormwater runoff is disclosed. This apparatus utilizes gravitational separation and tortuosity, resulting from a plurality of baffles both perpendicular to and oblique to the primary water flow direction, to trap substances less-dense and more-dense than water. The apparatus features improved resistance to pollutant remobilization through treatment of water volume rather than flow rates, using vertically stacked water columns of varying depths to settle small particles. An overflow structure diverts excessive liquid without interfering with purification and separation, and can be placed integrally within or external to the apparatus receptacle.

Abstract: A phase separator, upflow reactor apparatuses and methods for separating phases are provided. The phase separator includes a first separation unit and a second separation unit, each of which has walls defining a coagulation area. One of the walls adjoins a deflector inclined to the horizontal and vertical. The separator also includes a plurality of parallel plates spaced from each other and vertically and horizontally inclined which each have a lower edge. The other wall of the separator adjoins one of the parallel plates and the deflector extends below and across the lower edges of the parallel plates. Each of the first and the second separation units is capable of separating a gas from a liquid by diverting the gas around one wall of each of the separation units and by creating a circulation of the liquid around at least one of the parallel plates such that liquid is directed into the coagulation area.

Abstract: Apparatus can comprise an anoxic zone, an aeration zone in communication with the anoxic zone, and a sedimentation zone in communication with the aeration and anoxic zones. The sedimentation zone may include a first outlet in a lower portion thereof adapted to recycle material. A device may be provided to control the flow rate of the recycle material. Another device may be positioned relative to a sedimentation zone inlet and adapted to manipulate a material flow profile as material travels into the sedimentation zone. A sedimentation zone may also define an inlet comprising an overlapped area. Methods for purifying a waste inlet material comprise the steps of providing an anoxic zone, an aeration zone and a sedimentation zone. The methods may comprise the step of recycling material from a first outlet in a lower portion of the sedimentation zone.

Abstract: The present invention relates to an apparatus and a process for biological wastewater purification. According to the invention an activation tank (10) is provided in which, with feed of a catalyst, wastewater constituents are degraded by degradation means (11), for example microorganisms, suspended in the wastewater. In the activation tank (10) is disposed at least one lamellae pack (50) in or on which the degradation means (11) suspended in the wastewater are separated out by sedimentation to fall as thickened sedimentation means sludge (11′) to the bottom region (15) of the activation tank (10). In the said bottom region (15) of the activation tank (10) is provided forced recirculation (20, 22) of the degradation means, which takes up the thickened degradation means sludge (11′) and recirculates it as suspended degradation means (11) back to the activation tank (10).

Abstract: A die lube recovery and recycling system includes a weir tank, a filtration assembly, and a holding tank. The weir tank receives used, dirty die lube and filters large particles therefrom. Preliminarily filtered die lube is pumped through the filtration assembly and reconditioned die lube is delivered to the holding tank. A level of reconditioned die lube in the holding tank is monitored and, the die lube is replenished with fresh die lube from a fresh die lube source when the level falls below a predetermined level. A die lube pressure booster is used to withdraw die lube from the holding tank, pressurize the withdrawn die lube, and spray the pressurized die lube on a die in a casting machine.

Abstract: The invention relates to a gravity separator for an effluent made up of a multi-phase fluid mixture comprising at least a heavy first phase and a supernatant second phase. According to the invention, said separator includes adjustment means for adjusting its geometrical separation characteristics.

Abstract: A composite fluid separator capable of isolating a first liquid from a composite fluid having a first and second liquid, in which the first and second liquids have differing specific gravities. An outer housing encloses a separation chamber. An inlet port delivers the composite fluid through an elongated spillway into the sump of the chamber. Positioned between the inlet port and the outlet port is a plurality of stacked baffles, composed of individual separation flow plates, placed in an inclined relationship. The plurality of baffles creates a flow path in which the composite fluid is forced to flow over each of the individual separation flow plates as it travels upward in the separation chamber toward the outlet port.

Abstract: A coalescer apparatus is used in oil-water separator tanks. The coalescer includes a frame that supports coalescing plates that are inclined upwardly from the bottom of the frame member. The coalescing plates run parallel with each other and are spaced equally apart. The coalescing plates have a bottom surface that is corrugated and a top surface that is flat without corrugations. Water containing oil and solids is passed through the coalescing apparatus and separation of the oil and solids from the water occurs. The solids fall to the top flat surface of the inclined coalescing plates. The inclined flat surface cause the solids to slide down the plate and out of the coalescer.

Abstract: An integrated apparatus that contains both the gravity settling mechanism and the dissolved-air floatation (DAF) mechanism in a compensating manner is provided. The said apparatus comprises a gravity settling chamber (34), a DAF chamber (42), a chamber connection channel (22), an air-dissolving device (38), a means for collecting treated water (24), and a water level control device (16). During treatment, heavy solid particles in water or wastewater can be quickly removed by gravity settling, while the remaining light solid particles and/or oil can be quickly removed by DAF. Thus, the apparatus of this invention is more effective and efficient compared with conventional clarifiers that employ only one clarification mechanism. Therefore, the apparatus of this invention is more compact and can achieve better effluent quality.

Abstract: A device is provided for the filter and collection of one or more material. The device incorporates a manifold with an inlet conduit and an outlet conduit, with an adjustable control handle on the top of the manifold and a baffle plate in the inside of the manifold. The manifold is sealed to the top opening of a collection chamber. During procedures which require withdrawal of material not to be collected, the control handle and baffle plate are adjusted to a pass-through mode which connects a internal adjustable conduit, which transverses through the baffle plate, with the lumen of the inlet and outlet conduits to form a continuous lumen with which to withdraw material not to be collected through. During procedures which require the withdrawal of material to be collected, the control handle and baffle plate are adjusted to a solids mode which orients the baffle plate to face both the lumen of the inlet and outlet conduits.

Abstract: The apparatus is a surface water purifying catch basin which uses a lamella separator to separate out fine sediment and a separate chamber to trap heavy debris, oil, and floating debris. The surface water enters an inlet chamber which is separated from a settling chamber by a divider wall that has a lower opening between the chambers and a higher overflow. The inlet chamber traps floating contaminates and those that are heavier than the water. The opening between the chambers permits the surface water to flow into and through the lamella separator. The catch basin exit is from the settling chamber, but the water can reach the exit only through the lamella separator that separates out the fine sediment in the water. All of the accumulated contaminates can be removed through access holes in the top of the catch basin.

Abstract: Apparatus for use in, for example, separating oil from water, which comprises a vortex chamber adapted to admit through an inlet a flow of oil and water, means, (e.g. a helical coil shaped wall member of a “Clock Spring Guide”), device adapted to impart a rotational movement to the admitted oil and water so as to form within the chamber a rotating fluid mass within which a nonturbulent vortex of oil floats on the water. Oil removal pipe provides means for the removal of oil from the oil vortex, and outlet means located below the level of the floating oil provides for the escape of water from the vortex chamber. Variable flow regulating means is located at or downstream of the outlet means to regulate the rate of flow of water through the chamber. A tilted corrugated plate separator housed in chamber may be interposed between the water outlet means of the vortex chamber and the variable flow regulating means to separate residual oil in the emergent water.

Abstract: A chamber having an inlet for receiving polluted storm-water runoff and an outlet for the storm water to flow out. Within the chamber are a screen, one or more baffles, a collection reservoir, and a pivotal filter. The screen is elevated for separating and suspending miscellaneous debris such as vegetative matter, paper, and plastic. The baffles increase storm-water residence time to encourage settling of particulate matter such as sand and grit. The collection reservoir has an adjustable weir for skimming off floating matter such as motor oil, other hydrocarbons, and detergents. And the pivotal filter catches clay during typical storm flows and pivots out of the way during higher flows. In addition, a method for maintaining the pollution trap includes removing the screen for cleaning, suctioning out the particulate matter and oil, and replacing the pivotal filter member.

Abstract: A chamber having an inlet for receiving polluted storm-water runoff and an outlet for the storm water to flow out. Within the chamber is a pivotal filter that catches clay during typical storm flows and pivots out of the way during higher flows. In alternative embodiments, there are included a screen, one or more baffles, and/or a collection reservoir for further dispersing, detaining, and/or filtering the storm water.

Abstract: A chamber having an inlet for receiving polluted storm-water runoff and an outlet for the storm water to flow out. Within the chamber is a screen that is elevated for separating and suspending miscellaneous debris such as vegetative matter, paper, and plastic, and that extends substantially all the way across the chamber to laterally disperse the storm water in the chamber. In alternative embodiments, there are included one or more baffles, a collection reservoir, and/or a pivotal filter for further dispersing, detaining, and/or filtering the storm water.

Abstract: A chamber having an inlet for receiving polluted storm-water runoff and an outlet for the storm water to flow out. Within the chamber are one or more baffles forming gaps and having apertures. The gaps define a longer water flow route through the chamber and the apertures disperse the storm water within the chamber. This increases storm-water residence time which encourages settling of particulate matter such as sand and grit. In alternative embodiments, there are included a screen, a collection reservoir, and/or a pivotal filter for further dispersing, detaining, and/or filtering the storm water.

Abstract: A chamber has an inlet for receiving polluted storm-water runoff and an outlet for the storm water to flow out. Within the chamber is a collection reservoir having an adjustable weir with a skimming edge for skimming off floating matter such as motor oil, other hydrocarbons, and detergents. In alternative embodiments, there are included a screen, one or more baffles, and/or a pivotal filter for further dispersing, detaining, and/or filtering the storm water.

Abstract: For increasing the capacity of a continuously operating sedimentation filtration device, the processing liquid to be cleaned is supplied before or adjacent to the filter body on opposed sides into the sedimentation container. Underneath the filter body, a comparatively high settling chamber is formed and between the filter body and the supply lines a separating plate is provided so that the processing liquid to be cleaned is guided mandatorily into the settling chamber . The cross-sections of the supply lines provided on opposed sides are comparatively large so that only minimal flow velocities of the incoming medium will occur.

Abstract: A settling tank for clarifying washing fluids with one or more walls disposed within the tank, each wall having a plurality of passages and defining a settling chamber. Preferably there is a top mounted fluid runoff opening into the tank disposed above the innermost settling chamber and at least one pump inlet disposed in an upper part of the tank outside the outermost settling chamber. Passages in the inner wall are in a lower region of the wall, and the passages in the second wall are in an upper region of the wall, and at least some of the passages are hooded to enhance a flow velocity change for fluid passing through the passages. There is optionally a sump pump having a one way valve for discharging sump sediment from the sump into a portable waste can. There is also preferably a sump tube generally curved upwardly and away from a bottom of the sump, and to which the pump is connected.

Abstract: A tubular reactor characterized by having short static mixing elements separated by coalescing zones is used to conduct multiphase liquid/liquid reactions. Small droplets of one of the phases are dispersed into the other phase by the static mixing elements. These droplets coalesce and at least partially phase separate as the mixture passes through the subsequent coalescing zone. The tubular reactor is particularly suitable for nitrating organic compounds while forming low levels of improperly nitrated by-products and low levels of nitrophenolics.

Abstract: Apparatus for circulating a fluid, for example a liquid or a gas, from a first end to a second end is disclosed. The apparatus comprises: a tube of a flexible material divided by dividing walls of a flexible material into an array of compartments or cells running the length of the tube, the compartments being arranged in rows and columns so that the tube divided by dividing walls has a honeycomb structure, with a first end of the tube on a base and a second end of the tube above the first end of the tube; first flow means and second flow means a fluid inlet into the first row of compartments; and a fluid outlet from the last row of compartments; so that fluid introduced through the fluid inlet flows either up or down the compartments in the first row, through the first or second flow means between the first and second rows, and then down or up the compartments in the second row, through the second or first flow means between the second and third rows, and so on until the fluid reaches the fluid outlet.

Abstract: A device for floccing a mixture produced during oil or gas well drilling has a vertical tank with a vertical peripheral wall having a central axis, and a bottom located in a lower end of the peripheral wall, the tank having a height which is significantly greater than a cross-section of the tank, a line for introducing the mixture through a top end of the tank into an interior of the tank so that a solid fraction of the mixture settles on the bottom, and a line for withdrawing a liquid fraction of the mixture from the interior of the tank.

Abstract: A separating device is provided for separating liquid from a slurry of liquid and solid particles. The device has a settling chamber including a filter screen spanning a liquid outlet opening at the open top end of the settling chamber. A slurry inlet, in communication with the settling chamber below the filter screen, introduces a slurry of liquid and solid particles into the settling chamber. Liquid is urged to escape from the settling chamber upwardly through the filter screen. The filter screen, being located at the top of the settling chamber, provides a more natural separation of the liquid from the solid particles by permitting the liquid to rise upwardly through the screen while the solid particles settle out in the settling chamber to be compacted at the bottom of the chamber for removal of the compacted solids from the bottom of the chamber.

Abstract: An apparatus for separating floating and non-floating particulates from drain water wherein said apparatus includes a first chamber for collecting non-floating particulates, a second chamber for collecting floating particulates, and a third chamber through which treated drain water can be discharged from the apparatus. An inlet pipe for introducing drain water into the first chamber is provided tangential to the first chamber to provide a vortex flow of drain water into said first chamber. An outlet pipe providing flow of drain water from the first chamber to the second chamber has an inlet at the vortex of drain water flow in the first chamber and an outlet that is spaced a predetermined distance from the floor of the chamber.

Abstract: An oil well system for extracting oil extracted from a reservoir via a well, includes a separator device adapted to separate oil and water from a mixture extracted from a reservoir. The separator device has a non-vertical first flow path for the mixture and being arranged along a non-vertical portion of the well, a second flow path, separate from the first flow path, for receiving water or a water enriched phase that has been separated from the mixture by the separator device, and a plurality of drain openings along a section of the first flow path. The first and second flow paths are arranged such that water or the water enriched phase in the first flow path can flow by gravity to the second flow path via the drain openings. An opening area of the drain openings, per unit area of the first flow path, decreases in a flow direction of the mixture along the first flow path.

Abstract: A three-phase separator (1) comprising a normally horizontal vessel (3) defining a liquid separation space (5) and a gas space (7), which vessel (3) has an inlet end space (1) provided with a feed inlet (21) and an outlet end space (15) provided with separate outlets (25, 26 and 27) for the three phases, which vessel (3) further comprises an inlet device (31) comprising a primary separator (35) arranged in the gas space (7) and a tilted return tray (38) arranged in the gas space (7) having a lower end (39) that is located near the inlet end wall (13) such that a passage (41) is defined between the lower end (39) and the inlet end wall (13).

Abstract: A solvent separator apparatus having a vertical accumulator tank with a top end and a bottom end, the accumulator tank being serially connected to a vertical reservoir tank having a top end and a bottom end; a down tube vertically positioned in the accumulator tank having a top end nearest the top end of the accumulator tank and a bottom end nearest the bottom end of the accumulator tank, with an inlet at the top end of the down tube and an outlet at the bottom end of the down tube; an inlet conduit connected to the inlet of the down tube, the inlet conduit entering the bottom end of the accumulator tank and defining an upward flow path within the accumulator tank to the inlet at the top end of the down tube; a heat exchanger in communication with the down tube for withdrawing heat therefrom; and a transfer conduit defining a downward flow path from the top end of the accumulator tank to the bottom end of the reservoir tank.

Abstract: In the typical embodiments disclosed in the specification, a ballasted flocculation liquid treatment arrangement includes a mixing chamber in which liquid to be treated, flocculating agents and granular material are mixed. The mixture is supplied to the bottom of a flocculating chamber adjacent to the mixing chamber through an opening in a common wall between the chambers and is maintained in suspension in the flocculating chamber by turbulence generated by a rotating blade array. Ballasted flocs are transferred from the flocculation chamber to an adjacent sludge tank through a first opening in a common wall between them and liquid which contains lighter flocs is returned to the flocculation chamber through a second opening in the common wall. Liquid from the flocculation chamber passes upwardly through a turbulence control arrangement where flocs and particulates are substantially removed and into a clarification chamber where clarified liquid is passed over a weir to an outlet.

Abstract: An apparatus for separating or segregating an insoluble or immiscible fluid mixture into its denser and less dense components is disclosed. The apparatus' serviceability is enhanced through the use of a removably secured focusing plate. The apparatus may be advantageously used to separate grease/water mixtures of commercial food preparation operations into a gray water component for disposal in sewer lines and a grease component for storage and subsequent appropriate disposal.

Abstract: A system for separating solids from a fluid stream. The system includes a first separator device mounted to a container. The container includes a settling compartment and baffle plate module, with the initial settling compartment receiving the fluid from the first separator device. The fluid stream proceeds through the baffle plate module. The solids within the fluid stream will descend to the bottom of the container. A spiral blade is positioned at the bottom of the container, with the spiral blade adapted to convey solids to a first pump member. The speed of rotation of the spiral blade may be varied. The first pump member discharges the slurry to a second separator device. The second separator device will discharge the separated fluid stream into the baffle plate module. In one embodiment, the first separator device is a linear shaker and the second separator device is a cyclone separator and linear shaker mounted in tandem.

Abstract: Device for separating two non-mixable liquids with different specific gravities such as oil and water, which device contains a first separation tank (2) with an overflow (11, 12) for each of the liquids to be separated, a coalescence filter (3) whose inlet (14) is connected via a pipe (13) to the overflow (12) of the first separation tank (2) for the liquid with the highest specific gravity and a second separation tank (4) which is connected to the outlet (19) of the coalescence filter (3), characterized in that the overflow (12) onto which the coalescence filter (3) is connected is situated higher than the inlet (14) of the coalescence filter (3) with a difference in height H1 which is such that the liquid mass in the pipe between the first separation tank (2) and the coalescence filter (3) provides for the necessary pressure to bridge the pressure drop in the coalescence filter (3) and the counterpressure of the liquid in the second separation tank (4).

Abstract: An oil/grease separation apparatus includes an inlet section for receiving a liquid flow containing water, oil/grease and gross solids. The gross solids are separated from the liquid flow and collected in the inlet section. A water jet eductor is provided having a solids extraction port located in a lower portion of the inlet section. The water jet eductor is actuated by supplying pressurized water to create a suction to extract the accumulated solids from the inlet section. The extracted solids are directed to a separator outlet or to an alternate disposal system by suitable piping.

Abstract: Dilute solutions of fermentation sales may be concentrated by extracting water using low-miscibility, low-molecular-weight secondary and tertiary amines, e.g. triethylamine (TEA), diisopropyl amine (DIA), N,N-diethylmethylamine (DEMA), and mixtures thereof. At 30° C.-55° C., which corresponds to typical fermentation temperatures, these low-molecular-weight amines or their mixtures, can extract large amounts of water from dilute aqueous solutions containing fermentation salts. Thus, dilute fermentation salt solutions can be concentrated by selectively removing water. At these low temperatures, the amine phase contains 20-35% water and a much reduced quantity of fermentation salt. When the temperature is raised, water phases out of the amine, allowing the amine to be recycled and reused to extract additional water. Using this approach, about 82.

Abstract: A device for floccing a mixture produced during oil or gas well drilling has a vertical tank with a vertical peripheral wall having a central axis, and a bottom located in a lower end of the peripheral wall, the tank having a height which is significantly greater than a cross-section of the tank, a line for introducing the mixture through a top end of the tank into an interior of the tank so that a solid fraction of the mixture settles on the bottom, and a line for withdrawing a liquid fraction of the mixture from the interior of the tank.

Abstract: A device of three-chamber type for purifying liquid in a cup-shaped vessel (17, 18) has an inlet tube (20) for the liquid at a certain level and an outlet tube (21) at a lower level than the inlet tube. The vessel is vertically divided by a substantially horizontal distribution disc (14) below the inlet and outlet tubes. The disc has at least one opening (19) and is provided with a substantially vertical distribution pipe (15) for receiving the liquid from the inlet tube (20). A first sedimentation chamber (A) is formed below the lower end of the distribution pipe (15), a second chamber (B) is formed over the lower end of the distribution pipe (15) and below the distribution disc (14) and a third chamber (C) is formed over the distribution disc (14).

Abstract: A liquid extracting apparatus in accordance with the present invention is configured so that a connection pipe 22a (suction-side pipe) of a pump 22 for extracting slurry liquid content is connected to the upper end side of a liquid content introduction path to which slurry in a tank 8 can be introduced to attain the precipitation and separation of solid content, and a number of tubes 26 are packed at the lower end portion of the liquid content introduction path 21. The present invention can provide a simple liquid extracting apparatus that can effectively extract only liquid content in the slurry (suspension) moving in the tank.

Abstract: The invention relates to an apparatus for separation of a first fluid from a mixture of at least the first fluid and a second fluid and a method for doing the same. The apparatus is preferably located downhole, but also can operate on the surface. According to the invention, the apparatus comprises:—a production pipe for flowing the mixture;—at least one settling chamber surrounding the production pipe;—at least one aperture allowing the mixture flowing into the production pipe to flow into the settling chamber; and—an exit pipe, connected to the settling chamber, allowing the first fluid to flow out of the settling chamber.

Abstract: A method and device for separating grease from waste water. The separator device includes a receptacle with an upper first part and a lower second part separated by a plate. The receptacle further has an inlet port for waste water, a discharge port for separated waste water, discharge means for grease and/or sludge, and an overflow pipe establishing a connection between the receptacle first part and the receptacle second part. Waste water is supplied through the inlet port to the upper first part, and the waste water is allowed to undergo a separation by gravity, whereby a grease layer is formed on a separated waste water layer and a sludge layer on the plate. In order to achieve a high degree of separation, separated waste water is allowed to flow through the overflow pipe to the receptacle lower second part. Grease is removed from the grease layer and/or sludge from the sludge layer through the discharge means, and separated waste water is discharged through the discharge port.

Abstract: The present invention is an apparatus and a method that separates petroleum products such as fuel oil and gasoline from other foreign constituents, such as water and organic and inorganic solids. In the present invention a petroleum product and its undesirable impurities enters a cylindrical chamber having an input port and an output port. Within the container exists a longitudinal input chamber which forces the fluid to assume a velocity, acceleration and direction as it progresses through the chamber and finally ejected through a nozzle which directs the fluid into a concave surface to produce a rotation of the fluid. Due to centrifugal and other physical forces, components of greater specific gravity are deflected at an angle relatively smaller than components having a larger specific gravity.

Abstract: An in-line storm water drain filter and baffle box is installed within a storm water drain pipe to direct storm water runoff through the storm water drain pipe and through the filter and baffle box prior to the storm water drain water passing through an outfall into a lake, pond or retention area. The filter system includes a housing having an inlet and an outlet and a plurality of chambers formed therein. A housing cover allows for access into the housing and a plurality of filter screens are mounted over each of the plurality of housing chambers for collecting trash from the storm water passing therethrough. The housing has a generally arcuate bottom. The filter system also has inlet and outlet cover frames for holding removably mounted blocker dampers for blocking the ingress and egress of storm drain water during cleaning of the filter system. An oil collection boom is removably mounted in the housing adjacent the inlet for collecting oil in the drain water entering the housing inlet.

Abstract: A separator that utilizes an arcuate inlet manifold and an arcuate baffle to increase the rate of separation for a mix of materials having different specific gravities. The separator includes an arcuate baffle that defines a separation chamber and an arcuate pipe through which a mixture of materials having specific gravities is carried into the chamber. The mixture is discharged into the separation chamber against the baffle through a series of openings disposed along the perimeter of the pipe. The baffle, pipe and openings are configured relative to one another such that mixture is discharged against the baffle at an oblique angle. In preferred versions of the invention, mixture is discharged slanting up, slanting to the side or slanting up and to the side against the baffle at an angle of 18 to 24 (most preferably at about 22°).

Abstract: The present invention relates to methods and apparatus for removing a contaminant from an object. According to one aspect, an apparatus for washing an object which has contaminant is arranged to recover the contaminant. The apparatus includes a support floor that supports an object to be washed and a basin mounted below the support floor. The basin is divided into a plurality of chambers which include a clean water chamber, a secondary water chamber, an oil containment chamber, and a contaminated water receiving chamber which receives water which is contaminated after it is flowed over the object to remove the contaminant. The contaminated water received in the contaminated water receiving chamber must pass sequentially through the oil containment chamber and the secondary water chamber prior to entering the clean water chamber.

Abstract: Wastewater can be treated using a combination of a settleable solids separator, such as a vortex separator and a membrane separation system. Removal and segregation of materials that adversely affect operation of the membrane separator earlier in the treatment process can improve water throughput, water quality and the lifespan of system components. Physical separation of settleable solids and floatable materials from the wastewater prior to treatment with a membrane separator can allow higher flow rates to be achieved.

Abstract: A sedimentation apparatus for precipitating and separating suspended solids and coagulated flocs in a liquid to be treated, so as to clarify the liquid. The sedimentation apparatus comprises a mixing chamber secured within a sedimentation tank, for mixing and stirring the liquid and an additive; and a rotary support of a distributor, functioning as a bottom of the mixing chamber, rotatable about the center axis of the mixing chamber. The bottom portion of the rotary support is formed with an opening. The sedimentation apparatus has a blade for discharging from the opening the precipitate deposited on the bottom of the rotary support. As a consequence, the precipitate can be prevented from accumulating in excess in the rotary support.

Abstract: A liquid separator (10) for separating two immiscible liquids having different specific gravities, for example, a first liquid comprising water and a second liquid comprising oil. The liquid separator (10) has a housing (12) that defines a separation chamber (14) and liquid inlet (16), a first liquid outlet (18) and a second liquid outlet (20) mounted above the first liquid outlet (18). A float 26 is positioned within separation chamber 14 to translate in the vertical direction and has a specific gravity between that of the first and second liquids so that it floats at approximately the interface (28) between the two liquid phases (30 and 32). Valve closure devices (38 and 40) contact valve seats in the valves 46 and 56 of first and second liquid outlets (18 and 20) to control the flow of separated liquids from separation chamber 14 as determined by the level of the interface (28) and the length of the valve rods (34 and 36).