A forward or pressure retarded osmosis system using submerged hollow fiber membranes, a draw solution of superparamagnetic nanoparticles (preferably an iron oxide core with a silica shell that is chemically treated with a dispersant stabilizing it in a permanent suspension), that produces an osmotic pressure that drives fluid through the semipermeable membrane and a multiplicity of rigidly connected, permanent ring magnets forming layers, that maintains the locational position of the magnetic nanoparticles inside the hollow fiber membranes, preventing the draw solute particles from leaving membrane surface area. The various magnetic fields produced by the ring magnets attract the magnetic nanoparticles toward the surface area of the membrane preventing dilutive concentration polarization, thereby maximizing permeate flux rate.

The disclosure provides a hollow fiber liquid filter device provided with exhaust fiber membranes. The hollow fiber liquid filter device comprises a shell, a liquid inlet end, a liquid outlet end, a melt-blown fiber filter element, a hollow fiber liquid filtering part and a hollow fiber gas filtering part, wherein the liquid inlet end and the liquid outlet end are respectively connected to the upper end and the lower end of the shell, the melt-blown fiber filter element is arranged on the inner side of the shell, the hollow fiber liquid filtering part and the hollow fiber gas filtering part are respectively arranged on the inner side of the melt-blown fiber filter element, a liquid inlet is formed in the liquid inlet end, and ,a liquid outlet is formed in the liquid outlet end.

A water filtration module includes filtration elements, each formed from a bundle of hollow fibers. In each element, the end portions of the fibers are included in the coating blocks that do not close them, and a longitudinal hollow tube is arranged at the center of the bundle, so as to open on either side of the coating blocks. Each element includes a cap attached around the lower coating block providing a chamber in hydraulic communication with the hollow fibers and with the central tube. The set of elements are assembled removably in a housing of the module, such that an upper permeate collection chamber of the module is in hydraulic communication with the hollow fibers and the central tubes of each of the elements.

A fiber bundle cartridge for a fiber membrane degassing system includes an inner sleeve including one or more perforations and a fiber bundle positioned radially outward from the inner sleeve. The fiber bundle has an annular shape defining a central bundle axis. The perforations of the inner sleeve define a plurality of inlets and/or outlets facing radially with respect to the central bundle axis. A fiber membrane degassing system includes a housing defining a cylindrical volume having at least one inlet and at least one outlet. The system includes at least one fiber within the cylindrical volume, where fluid flowing through the cylindrical volume from the at least one inlet to the at least one outlet flows perpendicular to a longitudinal dimension of the fiber. A method of degassing a liquid includes directing a liquid volume through a fiber bundle in a direction radial to a longitudinally extending bundle axis.

An aerator device, a filter system including an aerator device, and a method of aerating a filter using an aerator device. An aerator device includes a housing having an interior cavity; a first plate in the interior cavity and defining a first cavity portion and a second cavity portion thereof, the first plate being spaced apart from a top wall of the housing to define a first opening through which the first cavity portion and the second cavity portion are in communication; and a second plate defining a first chamber and a second chamber of the second cavity portion, the first chamber and the second chamber being in communication with each other below a lower end of the second plate, the housing having an inlet opening in communication with the first cavity portion, and an outlet opening through the top wall and in communication with the second chamber.

The present invention concerns a filtration membrane bundle (30) comprising a plurality of elongated filtration fibers (40) arranged in a spiraled coil (34); and one or more filaments (50) woven around the plurality of elongated filtration fibers (40) binding one or more adjacent elongated filtration fibers (40) at a predetermined and homogeneous spacing (44,48) from one another wherein each elongated filtration fiber (40) is bound to respective adjacent elongated filtration fibers (40) in a co-planar configuration, and wherein the co-planar configuration of filtration fibers (40) are rolled into a coil (34). Furthermore, a filtration membrane assembly comprising the filtration membrane bundle (30) and a housing and method of providing the filtration membrane bundle (30) are disclosed.

A fluid degassing device can include a shell configured to retain a selectively permeable hollow fiber bundle, wherein the shell defines a first flow port and a second flow port and at least a third flow port, and a selectively permeable hollow fiber bundle having a plurality of hollow fibers disposed within the shell such that a first flow circuit is defined between the first flow port and the second flow port, and a second flow circuit is defined in fluid communication with at least the third port such that an inner channel of one or more of the hollow fibers is in fluid communication with at least the third flow port, wherein second flow circuit is partially fluidly isolated from the first flow circuit such that at least one first fluid cannot pass through a wall of one or more hollow fibers, but such that at least one second fluid can pass through the wall of the one or more hollow fibers. The shell and the fiber bundle include a non-cylindrical shape.

A dialyzer composed of: first and second dialyzation chambers, and an intermediate chamber interposed between the first and second dialyzation chambers. Each of the chambers has a respective one of a blood inlet or outlet and a dialysate inlet or outlet arranged so that blood and dialysate flow in counter-current to one another in both chambers. The intermediate chamber is connected to form a dialysate-free blood flow passage between the blood chambers and is configured to maintain a substantially uniform blood flow.

A separation membrane module comprises a hollow module container, and an element unit which is housed in the module container. The element unit comprises a plurality of connected separation membrane elements each of which includes: a separation membrane for separating components of a substance flowing to the inside of the module container; and membrane bundle securing materials for securing both ends of the separation membrane. In the element unit, a flow channel for discharging the components separated by the separation membranes to the outside of the element unit is formed. Passage members though which the components separated by the separation membranes can pass toward the flow channel for discharging are disposed at connections between the plurality of separation membrane elements such that both end surfaces of each of the passage membranes are respectively in contact with the membrane bundle securing materials of the separation membrane elements adjacent thereto.

The present invention relates to a hollow fiber membrane module provided with: a tubular casing having a first end and a second end in the axial direction; a plurality of hollow fiber membranes; a first potting part; and a second potting part, the hollow fiber membrane module further having a flow regulation structure in which a fluid flowing outside the hollow fiber membranes from the second end side toward the first end side forms a flow directed to the radial center on the second end side of the first potting part, and further forms a radial flow directed from the radial center to the radially outer peripheral side on the second end side of the first potting part.