The disclosed technology relates to a water filtration and delivery system for a dialysis unit. The water nitration and delivery system including: a laminarizer, the laminizer producing a laminarizer flow; an ultrafiltration unit, the ultrafiltration unit being placed downstream and connected to the laminarizer, the ultrafiltration unit receiving the laminar flow from the laminarizer; and at least one carbon filter, the at least one carbon filter being placed downstream from the ultrafiltration unit, the at least one carbon filter receiving the laminar flow, wherein the laminar flow causes less stress on internal components of the ultrafiltration unit and the at least one carbon filter.

A disposable cell enrichment kit includes a crossflow filtration device configured to be disposed along a main loop pathway and to receive a process volume containing a biological sample and utilize crossflow filtration, via a micro-porous membrane, to retain a specific cell population in a retentate from the process volume and to remove a permeate including certain biological components from the process volume. The crossflow filtration device includes a laminated filtration unit that includes the micro-porous membrane, a first mating portion, a second mating portion, and a membrane support. The membrane support includes a first plurality of structural features that define a first plurality of openings, wherein the first plurality of structural features are coupled to the micro-porous membrane and provide support to the micro-porous membrane, and the first plurality of openings allow the permeate to flow through them after crossing the micro-porous membrane.

A central tube assembly for a filter cartridge and a manufacturing method for the central tube assembly are provided. The central tube assembly includes a first half-tube defines a first flow passage, and having a first water inlet at an end thereof and a water output hole in a side wall thereof, a filtering membrane bent to form a first membrane layer and a second membrane layer, the first half-tube being disposed between the first membrane layer and the second membrane layer; an input-water filtering net connected to the first half-tube and disposed between the first membrane layer and the second membrane layer, a second half-tube disposed outside of a bending of the filtering membrane, defining a second flow passage, and having a water input hole in a side wall thereof and a first water outlet at an end thereof, and a produced-water filtering net.

Provided is a filtration device including: a flow path that meanders; a filtration membrane that separates a supply side and a permeation side of the flow path; a first distribution port that is provided at one end of the supply side of the flow path; a second distribution port that is provided at the other end of the supply side of the flow path; a first discharge port that is provided on the permeation side of the flow path; and a second discharge port that is provided at a position different from that of the first discharge port on the permeation side of the flow path. First liquid feeding for allowing a liquid flowed in from the first distribution port to flow out from the second distribution port, and second liquid feeding for allowing a liquid flowed in from the second distribution port to flow out from the first distribution port are alternately performed. A liquid that has passed through the filtration membrane is discharged from the first discharge port while the first liquid feeding is performed, and a liquid that has passed through the filtration membrane is discharged from the second discharge port while the second liquid feeding is performed.

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.

Exemplary embodiments in desalination by direct contact membrane distillation present a cylindrical cross-flow module containing high-flux composite hydrophobic hollow fiber membranes. The present embodiments are directed to a model that has been developed to describe the observed water production rates of such devices in multiple brine feed introduction configurations. The model describes the observed water vapor production rates for different feed brine temperatures at various feed brine flow rates. The model flux predictions have been explored over a range of hollow fiber lengths to compare the present results with those obtained earlier from rectangular modules which had significantly shorter hollow fibers.

Disclosed herein are membrane device embodiments that can be used for separating blood plasma and/or blood serum from blood samples. The membrane device embodiments comprise built-in features that facilitate blood plasma and/or blood serum separation and also provide the ability to detect, quantify, and qualify analytes present in a blood sample. The membrane device embodiments are portable and just a single membrane can be used for a plethora of detection and analysis techniques. Also disclosed herein are embodiments of methods for making and using the membrane device.

A whole blood filtration device is provided with a filter membrane separating a feeding volume and a clean side of the filter membrane from each other. The feeding volume communicates with a first feeding side opening and with a second feeding side opening. The filter membrane has pores with a pore size that ensures permeability of the filter membrane to blood plasma/serum and that retains blood cells. The first feeding side opening can be coupled to a first blood pump for feeding blood from the first feeding side opening into the feeding volume so that blood plasma/serum permeates the filter membrane and blood cells, retained by the filter membrane, exit from the feeding volume through the second feeding side opening.

An ion-exchange and ultrafiltration filter system having an exterior housing having an inlet and an outlet with an ultrafiltration membrane provided within the housing along a central axis about a central portion of the housing with an ion-exchange membrane provided within the housing between the ultrafiltration membrane and the housing. The ion-exchange and ultrafiltration filter system being capable of being configured so as to provide two-step filtration in a plurality of modes, either ion-exchange to ultrafiltration, or ultrafiltration to ion-exchange.

A fiber bundle contactor may include a vessel including a first inlet; a second inlet; a mixing zone arranged in the vessel to receive a first fluid from the first inlet and a including fluid from the second inlet, wherein the mixing zone comprises a perforated plate assembly comprising a plate, a plurality of openings in the plate, and a plurality of riser pipes that extend from the plate and arranged to allow fluid flow through additional openings in the plate; and an extraction zone including a fiber bundle arranged in the vessel to receive the first fluid and the second fluid from the mixing zone.