A blood processing apparatus includes an optional heat exchanger and a gas exchanger disposed within a housing. In some instances, the gas exchanger can include a screen filter spirally wound into the gas exchanger such that blood passing through the gas exchanger passes through the screen filter and is filtered by the spirally wound screen filter a plurality of times.

Embodiments relate generally to a filter (110), for example, for attachment onto a gas detector device or a gas sensor, and attempt to improve the efficiency and service life of the filter (110). Embodiments typically comprise a dustproof membrane (114) and a waterproof membrane (113). Some embodiments may also comprise a splash-proof cap (130) and/or features to reduce negative pressure on the filter (110).

A separation and/or humidification element that employs fibrous hollow membrane tubes is provided, which may be used for water vapor transfer between different gas streams in a fuel cell application, such as to humidify the reaction gas. At least one and typically two composite end caps encapsulate ends of a bundle of the fibrous hollow membrane tubes. Each composite end cap comprises adhesive (e.g. epoxy) and a preform such as a plastic annular shroud.

A spiral wound membrane element and a method for cleaning a spiral wound membrane sheet are provided. The spiral wound membrane element comprising a perforated central tube; one or more membrane sleeves, each sleeve comprising two membrane sheets enclosed at two edges around a feed spacer sheet and wrapped around the central tube; a permeate carrier sheet attached to the central tube at a first edge opposite a second edge; and a seal on third and fourth edges of the permeate carrier sheet. The method comprises introducing two solution with different solute concentration to two sides of the spiral wound membrane sheet; establishing a concentration gradient between the first and second sides; communicating a first solvent from the first side to the second side to remove a foulant located on the second side of the membrane sheet; and collecting a waste stream that contains the foulant.

Hollow fiber cartridges and components and methods of their construction.

A hollow fiber membrane module 10 includes: a plurality of hollow fiber membranes 200; a case 100 that accommodates the plurality of hollow fiber membranes 200 and has a case main body 110 made of a resin and having openings at both ends thereof; and a pair of sealing and fixing portions 310 and 320 that seal a gap between the hollow fiber membranes in a state where a hollow inside of each of the hollow fiber membranes 200 is kept open and fix the plurality of hollow fiber membranes 200 to the case 100 on both end sides of the case 100. In the case main body 110, a reinforcement portion 115 that connects a pair of facing wall surfaces of inner wall surfaces for accommodating the plurality of hollow fiber membranes 200 is integrally provided on the pair of wall surfaces.

A degassing tube includes a first plate, a second plate and a degassing tube. The first plate has a recess portion and a flange surrounding the recess portion. The flange has a first side and a second side opposite to the first side. A tube connector is disposed protrusively from the second side and located on the flange. The second plate covers the first plate. The degassing tube is disposed in the tube connector. The tube connector is formed with a degassing opening indented from the first side. The degassing opening has a maximum width defined in the tube connector and a minimum width defined on the first side. The minimum width is less than the maximum width for making the degassing tube tightly connected in the tube connector.

The present invention provides a filter element (500) having a radial permeate discharge path (550). The filter element generally includes a closed membrane structure (510) wrapped about a core (530) in reciprocating clockwise and counterclockwise directions, forming semicircular folds of membrane about the core. The semicircular folds of membrane have opposingly situated apical ends (560) separated by a gap. The interior of the closed membrane structure (510) defines a feed channel and the exterior of the closed membrane structure defines at least one permeate channel (522). A radial permeate discharge path (550) extends through the gap between the apical ends of the semicircular folds of membrane. Systems containing, and methods of using, filter elements including radial permeate discharge paths are also provided.

Hydrogen generation assemblies, hydrogen purification devices, and their components are disclosed. In some embodiments, the devices may include a permeate frame with a membrane support structure having first and second membrane support plates that are free from perforations and that include a plurality of microgrooves configured to provide flow channels for at least part of the permeate stream. In some embodiments, the assemblies may include a return conduit fluidly connecting a buffer tank and a reformate conduit, a return valve assembly configured to manage flow in the return conduit, and a control assembly configured to operate a fuel processing assembly between run and standby modes based, at least in part, on detected pressure in the buffer tank and configured to direct the return valve assembly to allow product hydrogen stream to flow from the buffer tank to the reformate conduit when the fuel processing assembly is in the standby mode.

Provided is a method for separating, from a raw gas containing a specific gas, the specific gas using a gas separation membrane module. The gas separation membrane module includes a housing and a gas separation membrane element enclosed in the housing. The gas separation membrane element includes a gas separation membrane including a hydrophilic resin composition layer for selectively allowing for permeation of the specific gas. The method includes the steps of: increasing pressure in an interior of the gas separation membrane module; increasing a temperature in the interior of the gas separation membrane module; and feeding a raw gas to the interior of the gas separation membrane module in that order.