A process for producing nitrogen-rich air by feeding high temperature air at 150 C. or more to an air separation membrane module is described. After being placed at 175 C. for two hours, the air separation module exhibits a shape-retention ratio of 95% or more in one embodiment. The nitrogen-rich air can be fed to a fuel tank for an aircraft, for example.

The invention is directed to preparation of hollow fiber membrane devices that exhibit improved durability and mechanical strength in air separation operations such as generation of nitrogen enriched air on board aircraft. In particular the invention provides for preparation of hollow fiber membrane modules with terminal tubesheets of superior mechanical properties and improved long term durability in air separation operations.

The invention provides a method and a device for manufacturing a hollow fiber membrane module. The present invention, by penetrating the hollow fiber membrane wires into the steel wires and performing rigidization treatment, greatly improves the rigidity of the hollow fiber membrane wire module, thereby avoiding the bending and deformation of or the damage of hollow fiber membrane wire module due to a small force during the production process, which greatly improves the production efficiency of the hollow fiber membrane module. The device of the present invention is used to achieve the above-mentioned method.

An ultra-filtration membrane assembly having an exterior housing having a housing; an ultra-filtration membrane provided within the housing, the ultra-filtration membrane being having a plurality of elongated filtration fibers arranged in a spiraled coil; and one or more filaments woven around the plurality of elongated filtration fibers thus binding each of the one or more adjacent elongated filtration fibers at a predetermined axial spacing from one another.

Provided is a hollow fiber membrane module that exhibits excellent durability even when a chemical such as a radical polymerizable compound is used for a separation or mixing process. Also provided is a method for producing the hollow fiber membrane module in a highly productive manner. More specifically, there is provided a hollow fiber membrane module at least including a tubular body, a cap, a hollow fiber membrane, and an end seal portion, wherein at least a liquid contacting portion of the end seal portion is sealed with a cured product of a curable resin composition including an epoxy resin, and wherein the epoxy resin includes a polyglycidyl ether of a polycondensate of an aromatic compound containing a phenolic hydroxyl group and an aromatic compound containing a formyl group and a phenolic hydroxyl group, and there is provided a method for producing the module.

An artificial, extracorporeal system for liver replacement and/or assistance, comprises a liver dialysis device for conducting hemodialysis on a patient suffering from liver failure. The liver dialysis device comprises a first standard hollow fiber membrane dialyzer which does not allow passage of an essential amount of albumin over the membrane wall and which is perfused with the patient's blood, and a second hollow fiber membrane dialyzer which allows the passage of essential but defined amounts of albumin over the membrane wall and which receives the blood of the first standard hemodialyzer. The filtrate space is closed off from the lumen space of the hollow fibers and is populated by adsorbent material which may comprise one or more different adsorbents.

A hollow fiber (HF) membrane incorporating molybdenum trioxide (MoO.sub.3) nanoparticles. The membrane may be composed of PPSU hollow fibers that are coated or encrusted with MoO.sub.3 nanoparticles and can be made by dry-wet spinning. The hollow fiber membranes containing MoO.sub.3 nanoparticles remove lead, cadmium or other heave metals from waste water and are resistant to attachment of bacteria and fouling.

A hollow fiber cartridge for a hollow fiber membrane degassing system, comprising a tube bundle of selectively permeable membrane tubes having inner channels, the bundle including two ends, and a tube sheet at each end of the tube bundle binding the ends of tube bundle. The tube sheets are configured to mount the tube bundle within a housing of the degassing system. The tube sheets are comprised of one or more of at least one Fluorosilicone, at least one Fluorocarbon, or at least one Polysulfide.

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.

The oxygenator (10) of organic fluids comprises a container body (20); a first aperture (21) for the entry of oxygen and a second aperture (22) for the exit of an exhausted gas; a third aperture (23) for the entry of an organic fluid to be oxygenated and a fourth aperture (24) for the exit of an oxygenated organic fluid; an oxygenation chamber (30) to oxygenate the organic fluid to be oxygenated, defined inside the container body (20); and a mass (31) of capillary fibers (32) which are impermeable to liquids and porous to gases, disposed so as to be lapped by the organic fluid inside the oxygenation chamber (30), parallel to each other in a first direction (X).