A detonator positioning device for use with a detonator in a perforating gun assembly is described. The detonator positioning device is configured for electrically contactably forming an electrical connection within the perforating gun housing by contact. The detonator positioning device includes a body having a first end, a second end, and a central bore extending between the first and second ends. The central bore is adapted for receiving one or more electrically contactable components of a detonator. The detonator positioning device aligns at least one of the one or more electrically contactable components to form an electrical connection with a bulkhead assembly.

The present disclosure relates to semipermeable membranes based on acrylonitrile copolymers capable of adsorbing bacteria from fluids, methods of producing such membranes, and devices comprising such membranes.

An automatic arranging machine for membrane fiber which comprises a workbench, and a membrane fiber reel, a membrane fiber guide plate, a first membrane fiber traction apparatus, a membrane fiber cutter, a membrane fiber bracket and a second membrane fiber traction apparatus which are sequentially arranged and mounted on the workbench. The invention provides an automatic arranging machine for membrane fiber and a membrane module production device, which mainly rely on a membrane fiber automatic filling machine to accurately control the membrane fiber, and realize passing the automatic membrane fiber through the membrane fiber bracket into a membrane tube by using the membrane fiber traction apparatus to cooperate with a related mechanical walking structure. The automatic control technology utilized in the whole process is mature, the manual intervention process is less, the consumables are used less, the manufactured components are with high quality, the production efficiency is high, and the produced membrane module has a good performance consistency and can be applied to the manufacturing process of many membrane separation modules.

A hollow fiber membrane bundle configured to be used in an artificial lung and comprised of integrated hollow fiber membranes 31 has hollow portions through which a fluid passes. The hollow fiber membrane bundle is shaped as a cylinder body. In addition, the hollow fiber membrane 31 is tilted with respect to a central axis O of the cylinder body, is wound around the central axis O of the cylinder body, and satisfies the following conditions. An inner diameter d.sub.1 of the hollow fiber membrane 31 is equal to or smaller than 150 m, a tilt angle with respect to the central axis O of the cylinder body of the hollow fiber membrane 31 is equal to or smaller than 60, and a ratio D.sub.1/L of an outer diameter D.sub.1 of the cylinder body to a length L of the cylinder body is equal to or greater than 0.4.

The present invention relates to high performance, crosslinked hollow-fibre membranes and a new process for manufacturing the same.

The invention relates to a filter device for the exchange of substances, comprising a pipe section-shaped housing with a center of gravity and with two housing ends, in which housing a hollow fiber bundle consisting of semi-permeable membranes is arranged, comprising, furthermore, an end cap having a first and second opening, wherein the housing and the end cap configure a first sealing surface which connects the housing and the end cap sealingly, and wherein the first sealing surface is spaced apart further from the center of gravity of the housing than the aperture, and wherein a first fluid chamber is formed between the first sealing surface and the first opening of the end cap, via which first fluid chamber the first opening is connected to the first flow chamber, wherein the housing and the one end cap configure a second sealing surface, wherein the first and second sealing surface are not configured by way of a sealant.

The invention relates to a method of determining a permeation property of hollow-fibre membranes wherein the permeation property of the hollow-fibre membrane is determined on a hollow-fibre membrane bundle which has been introduced into a housing and has terminally open hollow-fibre membranes at a first end of the hollow-fibre membrane bundle and terminally closed hollow-fibre membranes at a second end of the hollow-fibre membrane bundle. The invention more particularly relates to a method of determining the ultrafiltration rate and/or the ultrafiltration coefficient of hollow-fibre membranes.

The invention relates to processes for the production of capillary dialyzers. The processes involve thermoforming of bundles of hollow fiber membranes. The disclosure also relates to an apparatus for thermoforming bundles of hollow fiber membranes.

A hollow fibre membrane having a coiled, a hemihelix, a helical or an undulated native form, in which the membrane can be stretched by up to 4-times its original length with no plastic deformation, and wherein the native form of the membrane is produced by the asymmetric flow of liquid polymer through an opening of a die or nozzle.

A hollow fiber membrane laminate that includes a plurality of hollow fiber membranes wound to form a plurality of layers in a cylinder shape. The hollow fiber membranes are wound around a central axis while reciprocating a feeding point of the hollow fiber membranes along a central axis. Hollow fiber membranes adjacent to each other in each respective layer are separated by a predetermined separation distance. A speed differential z is reduced for successive layers approaching an outer side of the cylinder to maintain the predetermined separation distance. The speed differential z has a value obtained by dividing a pitch of the hollow fiber membranes within a respective layer by a traverse reciprocating distance.