An object of the present invention is to provide a fluid-separation carbon membrane module that can suppress defects on a surface of a carbon membrane or breakage of the carbon membrane and suppress suction of a potting material even in a case where a carbon membrane having low ductility is used, and the main idea of the present invention is a fluid-separation carbon membrane module in which a plurality of covered carbon membranes in which at least one covering yarn is helically wound around one or two fluid-separation carbon membranes are housed in a vessel.

In some examples, a membrane module includes a fiber bundle. The fiber bundle includes a tubular first region and a tubular second region positioned around the tubular first region. One of the first or second regions includes hollow fibers oriented along an axis of the fiber bundle. Another of the first or second regions includes hollow fibers that are not colinear in a radial direction from the axis of the fiber bundle. A void fraction of the second region is different from a void fraction of the first region.

A membrane humidifier for a fuel cell, of the present invention, comprises: a middle case in which a plurality of hollow fiber membranes are accommodated; a cap case coupled to the middle case; potting parts formed at the ends of the plurality of hollow fiber membranes; an assembly member disposed between the cap case and the end of the middle case so as to provide air tight coupling therebetween; and a protrusion part extending toward the edges of the potting parts from the inside of the cap case so as to provide air tight coupling between the cap case and the potting parts.

A separation membrane module includes a separation membrane including a hydrophobic polymer, a hydrophilic polymer, and polymer A, wherein the polymer A includes a hydrophilic unit and a hydrophobic unit, and is a copolymer having an alkyl group having 2 to 20 carbon atoms at a side-chain terminal of the hydrophobic unit, the separation membrane module having a retention rate of an albumin sieving coefficient of 86% or more at 60 minutes after circulation start relative to an albumin sieving coefficient at 10 minutes after circulation start when 2 L of bovine blood containing 50 U/ml of heparin, and having a hematocrit of 30% by volume and a total protein concentration of 6 to 7 g/dl is circulated at a flow rate of 100 ml/min at 37° C. and a filtration flow rate of 10 ml/(min.Math.m.sup.2).

An inventive drug product filling device for filling a liquid drug product into containers is disclosed. The drug filling device includes a drug product preparer configured for preparing the liquid drug product and a filling station configured for filling the liquid drug product into the containers. The filling station is fluidly coupled to the drug product preparer. A degasser is fluidly interposed between the drug product preparer and the filling station. The degasser has a membrane configured for at least partially separating off gas from the liquid drug product. Methods of (i) filling a liquid drug product into containers, (ii) increasing the accuracy of the filling weight of a liquid drug product in a container, (iii) increasing the stability oxygen-sensitive active pharmaceutical ingredient in a liquid drug product, and (iv) reducing polysorbate aggregate formation in a liquid drug product are also disclosed.

The present invention relates to a hollow fiber membrane including, sequentially from the center: a first layer having a high-density sponge structure including pores with a size of 1 nm or less; a second layer including a finger-shaped structure; and a third layer having a low-density sponge structure including pores with a size of 10 to 1,000 m, and to a method for producing the hollow fiber membrane.

The present disclosure relates to capillary dialyzers for blood purification, in particular, capillary dialyzers suitable for home hemodialysis systems.

Systems, devices, and methods are provided for removing carbon dioxide from a target fluid, such as, for example, blood, to treat hypercarbic respiratory failure or another condition. A device is provided including first and second membrane components for removing dissolved gaseous carbon dioxide and bicarbonate from the fluid, which can be done simultaneously. The device can be in the form of a cartridge configured for use in a dialysis system. A method of treatment is also provided, involving drawing blood from a patient and bringing the patient's blood in contact with a first membrane component having a sweep gas passing therethrough, and a second membrane component having a dialysate passing therethrough. The dialysate's composition can be selected such that charge neutrality is maintained.

Embodiments of the invention pertain to cartridges, systems and methods for performing hemodialysis and related extracorporeal blood treatment modalities and therapies, in which blood flows in the inter fiber space and dialysate flows in the lumens of hollow fibers. Appropriate connectors and fitting orientations may be provided. There may be provided orbital distributors, fanning of fibers, and features to promote uniformity of fiber spacing in the fiber bundle. Orbital distributors may contain contoured surfaces, flow redirectors, non-uniform-conductance flow elements, through-wall distributors, and other features. There may be subdivision of the fiber bundle into two groups of fibers with separate control fluid to each group. Appropriate systems may be provided for various therapies. Flow past the fibers may be parallel, transverse or other configuration. These various features may enable long-term application to all dialysis and ultrafiltration related therapies, and also to other therapies and to applications including implantables, portables and wearables.

The present invention relates to systems and methods for filtration and/or dilution of fluids, in particular for the dialysis of blood. The systems comprise a filter device (10) having a fluid chamber (18) and comprising a first lid (20) having arranged thereon a first fluid port (22). The filter device (10) further comprises a second lid (30) having arranged thereon at least a second fluid port (32). The filter device (10) further comprises a plurality of hollow fibers (40) arranged within the housing (12), wherein each of the plurality of hollow fibers (40) comprises a semi-permeable membrane and defines a fluid channel extending longitudinally through an interior of the respective hollow fiber (40). Also, the filter device (10) comprises a fourth fluid port (50) and a fifth fluid port (52) both provided at the fluid chamber (18).