Provided herein is a membrane filter device comprising a cell top cover (A, Y) and a cell bottom cover (B, Z) covering the device, a flexible tube (35, E, F) whereas at the end of the tube, a nozzle jet (22) is also secured via conical reducer to produce upper Reynold's number and for distributing the feed fluid, within the hex hollow chamber (C, X) for storing and receiving feed fluid, a reducer chamber (C, R1, R2) for storing and receiving permeate filtrated fluid, a connector (32, 53, 56) connecting both feed chambers (A, Y, Z) and reducer chambers (A, Y, Z), a membrane assembly (M/F) comprising a layer of membrane (130) sandwiched by a pair of seal rings (P1, OR, P2) and a layer of support net (MS) for securing said membrane (M/F). Most of the joints are connected using threaded joint and flow pressure, therefore no external clamp, nuts or bolts is needed. The flexible tube and the cylindrical shape ensure uniform flow in chambers. The apparatus is therefore a user-friendly and steadfast membrane filter device.

Embodiments of the invention provide replacements for a continuous layer of feed spacer mesh in spiral-wound reverse osmosis elements and replacing such mesh with discrete regions of feed spacer supporting the inlet and outlet ends of the element and a stiffening bridge feature to bridge between these regions at the tail end of each membrane leaf comprising the element during the element rolling process. The stiffening bridge feature prevents inward deflection of the inner layer of the membrane leaf during rolling, facilitating proper sealing of the adhesive through the permeate carrier to the adjacent membrane film using known membrane rolling techniques.

A spacer (13) of the present disclosure includes a plurality of first linear portions (21) and a plurality of second linear portions (22). The plurality of first linear portions (21) and the plurality of second linear portions (22) intersect each other to form a first opening portion (31) and a second opening portion (32) each having a diagonal line (31a or 32a) parallel to a predetermined direction, an opening area of the second opening portion (32) is smaller than an opening area of the first opening portion (31), and the difference between the length of the diagonal line (31a) of the first opening portion (31) and the length of the diagonal line (32a) of the second opening portion (32) is in the range of 10 to 35% of the length of the diagonal line (31a) of the first opening portion (31).

A fluid separation apparatus comprising a fluid separation membrane is provided. The fluid separation apparatus comprises a fluid separation membrane extending in one direction and having a cross-section with a closed curve shape, wherein the fluid separation membrane has a thickness of 0.1 mm to 2 mm, and an outer diameter of 60 mm to 360 mm when the cross-section is adjusted to be circular.

The invention relates to a cross flow filtration unit, which provides a planar, rigid filter plate for filtration of liquid media, said plate having a planar membrane, which is fluid tight bonded at its edges to the surface of a partly hollow supporting plate comprising exit openings, internal flow channels, and flow areas for a first liquid medium, and the membrane being in fluid contact with said first liquid medium at its internal surface and being in fluid contact with a second liquid medium at its external surface.

Photocurable compositions and methods of preparation and use of such compositions. More particularly, photocurable compositions useful for forming topographical features on surfaces such as membrane surfaces. Methods of forming topographical features on a membrane surface using photocurable compositions.

The present invention provides a device capable of reducing the resistance and increasing the ion exchange rate in an electrodialysis, electro-deionization, or capacitive deionization apparatus and a method for producing said device. More specifically, the device is an electrodialysis spacer designed to have an ionically conductive surface of either cationic nature, anionic nature or a combination of both, which act as conductive pathways for ions as they move towards their respective electrode. The method of producing said spacer involves coating a substrate, such as a woven mesh, expanded netting, extruded netting or non-woven material, with perm-selective ionomer solutions and applying that substrate to an inert spacer material that has undergone chemical or mechanical etching.

Described are wrapped fluid treatment elements, comprising: a composite material; an interleaf; and an inner core; wherein the composite material and the interleaf form layers wrapped around the inner core. The composite material and interleaf may be wrapped in a spiral configuration around the inner core. The invention also relates to a method of separating a substance from a fluid, comprising the step of placing the fluid in contact with an inventive device or element, thereby adsorbing or absorbing the substance to the composite material contained therein.

A spiral wound membrane module is suitable for use with high temperature water that may also have a high pH, for example steam injection produced water. The module uses a membrane with a polyphenylene sulfide (PPS) backing material. The feed spacer of the module may be made from polyphenylene sulfide (PPS) or ethylene chlorotrifluoroethylene (ECTFE). The permeate carrier may be made of a woven nylon (i.e. nylon 6, 6) fabric coated with high temperature epoxy. The core tube and anti-telescoping device may be made of polysulfone. In some examples, the module may be used at a temperature of up to 130 C. Optionally, the module may be used at a pH of 9.5 or more. In a filtration method, the module may be operated at a pressure in the range of 150 to 450 psi. The module may be operated at a generally constant pressure.

A hollow fiber membrane bundle with a longitudinal extent, with a membrane bundle cross section and with a first and a second bundle end, comprising a multitude of hollow fiber membranes extending between the first and the second bundle end, and also comprising, within the membrane bundle cross section, a proportion of threads which are arranged between the hollow fiber membranes and which keep the hollow fiber membranes apart. The arrangement of the threads between the hollow fiber membranes is such that at the first bundle end and/or at the second bundle end the hollow fiber membranes protrude beyond at least some of the threads, such that the hollow fiber membrane bundle has a smaller proportion of threads in a first and/or second end region, extending from the first and/or the second bundle end, than in a bundle region, located between the first and the second bundle end, which has a maximal proportion of threads, the length of the first end region and/or the length of the second end region being 1% to 45% of the bundle length.

A membrane module with a cylindrical housing with a longitudinal extent and with a first and a second housing end, and with a housing shell extending between the first and the second housing end, and also with a housing inner wall, where a hollow fiber membrane bundle of the above type is arranged in the housing oriented in the direction of the longitudinal extent of the housing.