A full-effect reverse osmosis membrane element includes a central tube and a reverse osmosis membrane assembly wound around the central tube. The reverse osmosis membrane assembly includes a pair of reverse osmosis membranes attached at front surfaces thereof and wound around the central tube. A water feed channel has a water inlet formed at front edges of the reverse osmosis membranes and a water outlet formed at rear edges of the reverse osmosis membranes. A water division structure is arranged in the water feed channel, and includes a first water division band forming a preset space with the central tube when the reverse osmosis membranes are in an unfolded state. The first water division band divides the water feed channel into a first flow channel having a gradually decreasing cross-section and a second flow channel in communication with the first flow channel.

The present disclosure relates to a block copolymer, a carbon dioxide separation membrane using the same and a method for preparing the same. The carbon dioxide separation membrane includes a copolymer represented by the following [Chemical Formula 1], and thus has excellent thermal, chemical and mechanical stabilities and shows high selectivity and permeability to carbon dioxide. ##STR00001##

A device for filtering and separating pressurized liquid mixtures by means of a membrane includes a substantially pressure-tight container in which the membranes are accommodated in a pressure-tight manner. The container has at least one intake for the mixture, as well as at least one outlet for the permeate separated from the mixture by means of the membranes, and at least one outlet for the retentate, also referred to as a concentrate. The pressure-tight container is made of plastic.

Embodiments of the present invention provide elements that are beneficial for use in fluid filtration. Embodiments provide elements that have variable feed spacer height, variable permeate spacer height, or both. The variable height allows flow properties to be matched to fluid volume as the filtration occurs.

The purpose of the present invention is to provide a highly reliable membrane module for removing hazardous components without the risk of a feed-source fluid and a concentrated fluid intermixing inside a hollow tube. The spiral wound separation membrane module is characterized in that: a spiral wound separation membrane element accommodated in a cylindrical container, the spiral wound separation membrane element having a structure in which a laminated body having a separation membrane, a feed-side spacer and a permeation-side spacer is wound around a porous hollow tube in a spiral shape, the feed-side spacer is positioned on a feed side of the separation membrane, the permeation-side spacer is positioned on a permeation side of the separation membrane, and a feed-side flow path and a permeation-side flow path are sealed so as not to communicate directly with each other.

Provided are a central tube for a filter cartridge and a filter device having same. The central tube (100) comprises a first half tube (1), a second half tube (2) and a membrane element (3), wherein the first half tube (1) has a first mating surface, and the first mating surface is grooved to form a first flow channel (111); the second half tube (2) has a second mating surface, the second mating surface is grooved to form a second flow channel (21), and the first half tube (1) and the second half tube (2) are butt-jointed to form a hollow, straight tube shape; and the membrane element (3) is arranged between the first half tube (1) and the second half tube (2) and seals the first flow channel (111) and the second flow channel (21), respectively.

The present invention provides a membrane filtration module comprising a housing in which the filtration membrane is disposed in a fixed positional relationship by a potting or bonding material obtained by the curing of a two component (2K) composition consisting of: a first component (A) comprising at least one compound (a) having at least two acetoacetate functional groups; and, a second component (B) comprising at least one compound (b) having at least one amino group, each said amino group being a primary or secondary amino group.

Disclosed is a membrane filter unit which includes: a filter case for housing a membrane; an inner tube housing a wastewater chamber and a hollow core tube, a middle tube housing a pure water chamber; the hollow core tube having a top opening at a top end and a bottom opening at a bottom end, and having a water collecting channel on its outer wall and positioned coaxially inside the case, wherein the top opening is adapted to open into the wastewater chamber; and a membrane having an inner peripheral surface, a top outer peripheral surface, a bottom outer peripheral surface and a side outer peripheral surface; and arranged around the core tube such that the inner peripheral surface of the membrane is spirally wound around the core tube and the side outer peripheral surface is capable of permeation of raw water through its surface.

A filter device (10), in particular for a tangential flow filtration device, has at least one fluid inlet (22), at least one retentate outlet (24) and at least one permeate outlet (26). The filter device (10) further has at least one membrane (16) which separates a retentate section (18) from a permeate section (20) in the filter device (10). Arranged in the retentate section (18) and/or in the permeate section (20) is at least one flow fitting (28) which is not formed from a woven or non-woven fabric, but from a structured plastic part, silicone part, metal part or ceramic part.

A sanitary membrane cartridge for use in reverse osmosis filtering includes an outer housing, a central core tube, and a membrane leaf wound around the central core tube to form a cylindrical filter. The cartridge further includes a sealant layer disposed around the cylindrical filter to form a sealed filter, the sealed filter disposed within the housing. The sealant layer preferably has a surface roughness value, Ra, ranging from about 0.38 m to about 0.82 m. The cartridge further includes a brine seal, disposed between the sealant layer and the housing, having one or more notches formed on an outer diameter of the brine seal such that the feed flow through the notches allows bypass flow, between the sealant layer and the housing, of 1% to 25% of a total feed flow through the sealed filter.