Abstract: A magnetic filter assembly 1 is described which is suitable for incorporating into a fluid system such that a process fluid flows through the filter to remove ferromagnetic particles in the fluid. The filter assembly 1 comprises a housing 2 having a flow chamber. The housing also comprises one or more elongate hollow sleeves 10 extending into the flow chamber such that, in use, an exterior surface of each sleeve 10 is exposed to the process flow and an interior surface of each sleeve 10 is sealed from the process flow. Each sleeve 10 has an opening via which the interior surface of the sleeve is open or openable to the environment whilst remaining sealed from the process flow. Each sleeve has received in it a magnet 12, the magnet being removable from the sleeve via the opening. In this way, cleaning of the filter by removal of the magnets is facilitated, without exposing the process flow.

Abstract: Disclosed is a separation system including: a chamber comprising: an inlet for receiving a two-phase fluid; a first outlet for draining liquid contained in the two-phase fluid; a second outlet for egress of gas contained in the two-phase fluid; a cylindrical body disposed in the chamber having a plurality of channels through which, during use, the two-phase fluid travels from the inlet to the second outlet, and wherein the liquid within the two-phase fluid coalesces on the walls of the plurality of channels as the two-phase fluid passes through the plurality of channels and the liquid drains through the first outlet.

Abstract: A method for recovering fine tailings from a tailings pond includes selecting a desired density of fine tailings to be removed from the tailings pond. Positioning a hollow shell having a closed bottom and holes formed through a sidewall of the shell within the tailings pond such that the holes are located at a depth of a layer of the fine tailings of the desired density and such that a top of the shell is disposed above a free water surface of the pond. Causing a flow of the fine tailings of the desired density through the holes into into the shell and removing the fine tailings of the desired density from within the shell.

Abstract: A separator for separating solids from a fluid including a tray assembly, the tray assembly including a plurality of nested tray units which define a separator axis and are spaced apart from one another along the separator axis, wherein each tray unit includes comprising an inner surface facing the separator axis 16 extending outwards, away from an aperture in the tray unit disposed at the separator axis, wherein the inner surface comprises an inner portion and an outer portion, wherein the inner portion is disposed between the aperture and the outer portion, and wherein the gradient of the outer portion is greater than the gradient of the inner portion.

Abstract: An anaerobic purification device for purification of wastewater, the anaerobic purification device comprising: a reactor tank (10) configured to, when in operation, have a sludge blanket formed at the bottom part; a fluid inlet (12) for, in operation, introducing influent into the reactor tank, the fluid inlet located in the lower section of the reactor tank (10); at least one gas-collecting system (13); at least one gas-liquid separation device (30); at least one riser pipe (22) connected to the at least one gas-collecting system (13) and discharging into the gas-liquid separation device (30); a downer pipe (24) connected to the gas-liquid separation device (30) and discharging into the bottom of the reactor tank (10); and a fluid outlet (16) comprising means for, in operation, varying the height of the fluid level (19) in the reactor tank within a predetermined range, the fluid outlet arranged at the upper section of the reactor tank (10); wherein the fluid level control means comprises: a fluid valve

Abstract: A system and apparatus configured to facilitate on-site treatment of wastewater from a residence is described. The system is configured to immediately treat wastewater as it is generated, on an as-needed basis, and works to remove undissolved down solids and reduce dissolved materials concentrations to a uniform level prior to transmission of the wastewater to municipal waste water treatment facilities and/or any non-drinking application. The system employs a two-stage treatment apparatus where the first stage is configured to pre-grind and decompose undissolved solids of the wastewater and the second to reduce dissolved materials concentrations. The first stage uses turbidity meters, and the second stage uses pH, BOD and conductivity to ensure a uniform output from each stage. A fast decomposer has rotating filters which operational modes ensure that the filters do not become clogged with solids in a ‘cake’ form simultaneously.

Abstract: An ocean wave actuated gravitational desalination apparatus and system for generating potable water comprised of, a box platform with a piston pump at sea level, an inverted prism shaped subterranean water tank below sea level, and a desalination processing structure above sea level. When the ocean waves pass over the top of the box platform, the piston pump is raised to open a set of valves to let the sea water into a cylindrical chamber. When the piston goes down, the valves close and a second set of valves open to release the water into the subterranean tank to be further released into containers on a carousal structure that move on rails by gravity. The water in the containers is emptied into holding and pre-filtration tanks and forced through filters into a pipe by the actions of a hydraulic oil pump and the filtered water released for storage and use.

Abstract: A wastewater separation system for separating waste from water includes an inlet, a hydrocyclone, a decanter, and a recirculating means. The hydrocyclone receives a first amount of wastewater from the inlet and centrifugally processes the wastewater in order to remove at least some of the waste from the wastewater in order to expel treated water and a second amount of wastewater. The treated water exits the system. The decanter is coupled to the hydrocyclone for accepting the second amount of wastewater in order to separate the second amount of wastewater into a collection of waste and a third amount of wastewater. The recirculating means recirculates the third amount of wastewater back to the hydrocyclone for reprocessing.

Abstract: An anaerobic reactor (1) for treating waste water includes a reaction vessel (2) and a three phase separator (4) above the reaction vessel and arranged to receive effluent from the reaction vessel. The three phase separator includes an outer wall (10, 14) connected at its bottom to the top of the reaction vessel and a liquid outlet (42), a lid (16) closing the top of the outer wall. The lid has a gas outlet (17) above the level of the liquid outlet. The three phase separator also includes a funnel (18) arranged above the reaction vessel, a guide wall (30) spaced from and arranged radially outward of the funnel so to surround an upper aperture of the funnel and a baffle wall (36) spaced from and arranged between the guide wall and the liquid outlet.

Abstract: A purification system for separating a molecule of interest from a solution is provided and generally includes a plurality of resin processing sections, wherein each of the resin processing sections is controllably separated from each other via a configurable gate valve, wherein the configurable gate valve is configured to introduce or evacuate a fluid/resin into/out of a proximately located processing section, a plurality of inlets configured to introduce fluid and/or resin into one or more of the plurality of resin processing sections.

Abstract: A method for obtaining crystals from a mother solution operates such that mother solution is fed into a crystallisation device. Supersaturation of the mother solution is brought about by open and/or closed-loop control of the temperature (?). Seed crystals are added to the mother solution at a seeding point (Sp). The seed crystals are grown as nuclei by continuous closed-loop process control and are finally removed from the method as crystals. They form the product yield. The formation of crystal nuclei in the mother solution is countered by steps in the closed-loop process control. During the closed-loop process control and the crystallisation procedure, the position of the limit (M) of the formation of secondary nuclei is determined using sensors that detect data currently, wherein the position of the limit (M) is established as a value of the concentration (c) and the temperature (?) from these data.

Abstract: Provided are a filter device and a washing method therefor. The filter device comprises a membrane housing (1); a spacer (2) having an ion transmittance and separating the membrane housing (1) into a first chamber (11) and a second chamber (12); a membrane element (6) disposed in the first chamber (11); a first electrode (4) disposed in the first chamber (11); and a second electrode (5) disposed in the second chamber (12). The method comprises respectively connecting a positive electrode and a negative electrode to the first electrode (4) and the second electrode (5), such that the first electrode (4) and the second electrode (5), water in the first chamber (11) and water in the second chamber (12) form an electrolytic cell, thus generating acidic water or alkaline water in the first chamber (11). The acidic water and/or the alkaline water are/is used for washing the member element.

Abstract: Device for capturing and removing magnetic material from a flow of material, wherein the device includes magnet assemblies including magnet rods for capturing magnetic material in a flow of material passing the magnet assemblies and where the magnet assemblies are removably arranged to a frame assembly of the device, wherein each magnet assembly includes a set of at least two magnet rods.

Abstract: Disclosed is an apparatus for removing air and particles, such as dirt, from a fluid which includes, inter alia, an elongated pressure vessel that has a vessel wall that defines an interior chamber and a vertical axis for the apparatus. Inlet and outlet ports are formed in the vessel wall, the inlet port allowing fluid to enter the interior chamber and the outlet port allowing conditioned fluid to exit the interior chamber of the pressure vessel. A plurality of concentrically arranged cylindrical mesh screen elements are positioned within the interior chamber that release entrained air from the fluid entering the interior chamber. Additionally, a cylindrical tube is positioned within the concentrically arranged mesh screen elements for removing particles from the fluid entering the interior chamber. In certain embodiments the apparatus includes a magnetic particle collector.

Abstract: The present invention relates to a process for the separation of at least one valuable matter containing material from a dispersion comprising said at least one valuable matter containing material and at least one second material. The process according to the present invention comprises at least the steps (A) to (E) and the optional steps (F) to (H) which are described herein.

Abstract: A reactor closed to the atmosphere and method using same for nitrate removal are disclosed.

Abstract: A continuous flow granular/flocculent sludge wastewater process selects for granule biomass capable of nitrogen and phosphorus removal and controls granule size and concentration of granular and flocculent sludge for optimal nutrient, organic, and solids removal in a smaller footprint. It includes anaerobic, anoxic, and aerobic process zones, a high soluble biodegradable COD loaded first reactor in anaerobic or anoxic zones, a granular sludge classifier with recycle of underflow granular sludge to the first reactor, a secondary clarifier to settle flocculent sludge and particulates and recycle of flocculent sludge from the secondary clarifier underflow to an aerobic process zone. Wasting of sludge from the two separate recycle lines controls the bioprocess flocculent and granular sludge concentrations and SRTs. Bypass around and recycle flow to the classifier to maintain desired flow under various influent flow conditions aid control of granule size.

Abstract: The method in the disclosure is achieved by chemically reacting diluted sulfuric acid generated when industrial sulfate titanium white powder production with a titanium raw material, and controlling an acid/titanium ratio and an iron/titanium ratio so as to produce the nano catalytic wastewater treatment agent. When being used for treatment of dyeing wastewater and other alkaline wastewater, by virtue of alkaline and dilution environment in wastewater, the nano catalytic wastewater treatment agent is subjected to self-fitting hydrolysist to produce a new ecological nano titanium dioxide ultrafine particle as a catalyst for decomposing organic matters in wastewater so as to decompose the organic matters into carbon dioxide and water; a decomposed and oxidized hydrated iron compound is used as a flocculation and adsorption nano particle, achieving the purpose of removing organic matters in wastewater.

Abstract: A system and method for detection of cells is disclosed. Target cells, such as circulating tumor cells (CTCs), may be of interest. Magnetic beads may be bound to the target cells. After which, the target cells (with the magnetic beads attached thereto) may be identified using an applied magnetic field. In one example, magnetic sensors may be used to detect movement of the target cells responsive to an applied magnetic field. In another example, an optical sensor (such as a camera) may be used to detect movement of the target cells responsive to an applied magnetic field. Further, separate from identification of the target cells, the target cells may be sorted using an applied magnetic field. In this way, a magnetic field may be used in either or both of target cell identification or target cell sorting in order to detect target cells of interest.

Abstract: The present invention relates to improving the results of anaerobic digestion of organic waste especially animal manure such as chicken manure by removing the grit in the waste by digesting the waste in a slurry at a temperature of about 50° C. or more for a period of time sufficient for the grit to settle out of the slurry.