The invention relates to a method for producing a tubular electrochemical separation unit comprising a plurality of electrochemical cells, arranged electrically in series, and comprising at least three layers, said method comprising: —a deposition step (110) of a first layer to form a first discontinuous layer (10) comprising several successive tubular modules (11) separated by spaces (12), —a deposition step (120) of a second layer, said deposition being achieved to form a second discontinuous layer (20) comprising several successive tubular modules (21) separated by spaces (22), so that tubular modules (11) are partially coated with tubular modules (21) of the second layer (20), —a deposition step (130) of a third layer, said deposition being achieved to form a third discontinuous layer (30) comprising several successive tubular modules (31) separated by spaces (32), so that tubular modules (21) are partially coated with tubular modules of the third discontinuous layer.

Composite polyether block amide (PEBA) copolymer tubes incorporate an ultra-thin PEBA layer that enables rapid moisture transfer and exchange through the tube. A composite PEBA film may include a porous scaffold support and may be formed or incorporated into the composite PEBA tube. A porous scaffold support may be coated or imbibed with PEBA to form a composite PEBA film. A composite PEBA film may be wrapped on a mandrel or over a porous scaffold support to form a composite PEBA tube. A film layer may be applied over a wrapped composite PEBA film to secure the layers together. The film layer by applied by dipping, spraying or painting.

Disclosed is a deflector disc of a disc tube membrane module, including a deflector disc body, radial water distribution ribs, an inner support ring and an outer support ring. Bulges are arranged on the front and back sides of the deflector disc body; first and second ends of the radial water distribution rib are respectively fixedly connected with an inner edge of the deflector disc body and an outer edge of the inner support ring, an annular boss is arranged on the front side of the inner support ring, a seal ring groove is respectively arranged at corresponding positions of the front and back sides of the inner support ring, multiple yielding water collecting grooves are annularly and uniformly distributed on the inner surface of the inner support ring; an inner edge of the outer support ring is fixedly connected with an outer edge of the deflector disc body.

Disclosed is a deflector disc of a disc tube membrane module, including a deflector disc body, radial water distribution ribs, an inner support ring and an outer support ring. Bulges are arranged on the front and back sides of the deflector disc body; first and second ends of the radial water distribution rib are respectively fixedly connected with an inner edge of the deflector disc body and an outer edge of the inner support ring, an annular boss is arranged on the front side of the inner support ring, a seal ring groove is respectively arranged at corresponding positions of the front and back sides of the inner support ring, multiple yielding water collecting grooves are annularly and uniformly distributed on the inner surface of the inner support ring; an inner edge of the outer support ring is fixedly connected with an outer edge of the deflector disc body.

Ammonia is made in a system that includes a conversion reactor for performing a Haber-Bosch process. Effluent streams from the conversion reactor, which include an ammonia component and excess hydrogen and nitrogen reactants, are fed to a membrane separator that includes NaA zeolite membranes disposed on one or more hollow porous supports. The NaA zeolite membranes are highly selective for the ammonia component, allowing the ammonia to be collected from a lumen of the membranes as a product and enriching the excess hydrogen and nitrogen reactants for reuse in the conversion reactor. These systems and the methods of their use are effective to replace and/or modify the energy-intensive condensation/recycling steps in the traditional Haber-Bosch process used to condense NH3 from the exiting stream of the reactor. The selective removal of ammonia by high quality NaA membranes helps to shift the ammonia evolution reaction.

A fuel filter for a fuel system includes a cylindrical frame having a pair of circular openings at longitudinal ends of the frame and a filter membrane, with the frame including a circumferential wall having an aperture and the filter membrane being disposed about an outwardly facing side of the wall and over the aperture. The frame includes tabs, such as deformable tabs, disposed adjacent at the openings for retaining the filter membrane on the frame, and the filter membrane overlaps itself when circumferentially disposed about the wall.

The present invention relates to a tangential flow separator element for separating a fluid medium for treatment into a filtrate and a retentate, said separator element having a monolithic rigid porous support (2) of rectilinear structure and having a single channel (3) arranged therein for passing the flow of the fluid medium for treatment, the outside surface (5) of the support presenting a profile that is constant. According to the invention, the monolithic rigid porous support (2) defines obstacles (9) to the flow of the fluid for filtering, which obstacles extend from the inside wall (3.sub.1) of said channel (3), are identical in material and porous texture to the support, and present continuity of material and of porous texture with the support, said obstacles (9) generating variations in the flow section of the channel.

Composite membrane tubing includes a porous scaffold support combined with polyether block amide copolymer. The composite membrane tubing has overlapping “fusion areas” that are an artifact of the manufacturing process. The methods of manufacturing above-mentioned composite membrane tubing have also been addressed. The composite membrane tubing can be reinforced with a structural mesh to further provide rigidity and strength. Composite membrane tubing or generally extruded tubing can be integrated into a multi-tube module for various applications.

A filter element comprises a membrane layer; and a feed spacer on the membrane layer, wherein the feed spacer comprises a plurality of unit cells arranged in three dimensions, wherein each of the plurality of unit cells comprises a cavity defined by a triply periodic minimal surface, and wherein the cavities of the plurality of unit cells are interconnected to allow a fluid to pass through the cavities of the plurality of unit cells.

The purpose of this invention is to provide a filtration membrane module with which is possible to improve the centrifugal separation effect of the primary-side flowpath during filtration, and the centrifugal separation effect of the area following the outer peripheral surface of the flowpath membrane element of the outer ring-shaped flowpath during backwash, and improve filtration efficiency and cleaning efficiency while curbing the accumulation of deposits on the membrane surface during filtration and during backwash. This filtration membrane module comprises: a membrane element equipped with a primary-side flowpath on the outside of a hollow cylindrical filtration surface; and a cylindrical housing positioned on the outside thereof. A flow adjuster is positioned inside the primary-side flowpath. A flow adjuster for backwash is positioned inside the secondary-side flowpath, which is an outer ring-shaped flowpath between the membrane element and the housing. The flow adjuster and the flow adjuster for backwash comprise spiral-shaped fins or the like in order to exhibit a centrifugal separation function in an area that follows the outer peripheral surface of the membrane element or the filtration surface.